BELLELI COMPANY [modalit · PDF file3810 - - - BS 1503-622 Enhanced S.S. Tp 347 w.o. - ESSO Davy McKee Residfiner Fawley Residfiner Lead Reactor R-101 1 235+4.5 630.000 216 - 448 -

REFERENCE LIST

ProcessLicensors:

Chevron, UOP, ExxonMobil, Lurgi, Axens, KBR, HaldorTopsoe, Shell

ASME, AD-Merkblatter, BS5500, Stoomwezen, FinnishCode, EN 1445

Design Codes:

Materials: Carbon Steel1.25Cr-0.5Mo2.25Cr-1Mo Standard 2.25Cr-1Mo Enhanced (or Vanadium)12CrMo9-10

Length: 75.450 mm (TT)Internal Diameter: 12.000 mm

MaximumDimensions:

> 420 units built since 1966Units:

From 10 tons to 1350 tonsWeight:

PRESSURE VESSELS & COLUMNS

REFERENCE LIST - OIL & GAS VESSELS, COLUMNS & REACTORS SHEET: 1 of 20

Printed on: August 29, 2016

DESIGN CONDITIONS

USER ENGINEER PLANT TYPE LOCATION DESCRIPTION No. SIZE WEIGHT PRESS. TEMP. MATERIALS CLADDING YEAR JOB No.

[mm] [Kg.] [Bar] [°C]

1010 - - - ½ Mo S.S. Tp 321 -

OIL ADM. BOARD Snamprogetti Lube Oil Bagdad Lube Oil Hydrofinish Reactor 05-R1 1 31 20.000 61 - 332 - - 1966 66.289 A

Iraq - 19.000 - - -

2450 - - - C.S. - -

ESSO Ctip Regasification La Spezia Sulphur Absorber E-202/E-252 2 72 76.000 47 - 408 - - 1967 67.613 A

Italy - 12.000 - - -

2000 - - - C.S. - -

ESSO Ctip Regasification La Spezia Sulphur Guard Absorber 2 59 25.500 47 FV 408 - - 1967 67.613 B

Italy E-203/E-253 4.350 - - -

2450 - - - ASERA 52 - -

MONTEDISON Montedison Acrylonitrile Priolo Reactor R-1001 C 1 53 71.000 47 - 300 - - 1967 67.674

Italy - 15.000 - - -

2350 - - - ASERA 54 - -

SHELL Lummus - Cardon Hot H.P. Separator V-1003 1 50 31.000 71 - 250 - - 1968 68.798 A

Venezuela - 7.300 - - -

2000 - - - ASERA 54 - -

SHELL Lummus - Cardon Cold H.P. Separator V-1004 1 39 21.000 71 - 150 - - 1968 68.798 B

Venezuela - 7.300 - - -

2650 - - - C.S. - -

ARAMCO Aramco - Abqaiq H.P. Production Vessel D-100 1 51 137.000 42 - 593 - - 1968 68.807

Saudi Arabia, Kingdom of - 35.200 - - -

1,200\810 - - - C.S. - -

GULF Ctip - Milano Dist. Absorber T-402 A/B 1 41 19.500 73 FV 152 - - 1969 69.303 C

Italy - 16.000 - - -

1520 - - - C.S. - -

N.I.O.C. Snamprogetti - Shiraz Reactor Product Separator FV-603 1 106 50.000 190 FV 205 - - 1970 70.459 A

Iran - 8.900 - - -

2000 - - - C.S. - -

SHELL Shell - Stanlow H.P. Separator V-5223 1 50 23.000 62 FV 220 - - 1971 71.1054 A

U.K. - 6.000 - - -

1680 - - 120 ½ Mo SA 240 Tp 304L -

ESSO Foster Wheeler - Augusta H.P. & Tail Gas Separators 1 41+2 20.300 66 - 363 - - 1972 72.1144 A

Italy D-804/D-819 4.000 - - -

4460 - - - ½ Mo SA 240 Tp 405 -

ESSO Fluor - Antwerpen Reactor D1-R101 1 41+3 127.500 27 - 427 - - 1973 73.1180-01

Belgium - 18.300 - - -

4160 - - - ½ Mo SA 240 Tp 304L -

ESSO Fluor - Antwerpen Reactor D1-R201 1 43+3 85.000 32 - 427 - - 1973 73.1180-02

Belgium - 12.400 - - -

4450 - - - ½ Mo SA 240 Tp 405 -

ESSO Fluor - Antwerpen Reactor N1-R101 1 45+3 71.000 32 - 427 - - 1973 73.1180-03

Belgium - 7.300 - - -

3170 - - - ½ Mo SA 240 Tp 304L -

ESSO Fluor - Antwerpen Hot Separator Drum V1-D102 1 60+2 71.000 59 - 366 - - 1973 73.1183-05

Belgium - 11.000 - - -

LEGENDA SIZES: Inside Diameter

Thickness

Tangent-to-Tangent Length

List of Reference list (PV)1



DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2100 - - - C.S. - -

ESSO Fluor - Antwerpen Steam Drum G1-D103 1 51 53.000 50 - 288 - - 1973 73.1193

Belgium - 16.500 - - -

3350 - - - ½ Mo S.S. Tp 347 w.o. -

CONOCO Ralph M. Parsons Desulphur. Immingham Hydrodesulph. Reactor D-4151 1 63+4 120.000 45 FV 427 - - 1973 73.1238

U.K. - 14.500 - - -

4100 - - - 13 Cr Mo 4 4 S.S. Tp 308L w.o. -

NESTE OY Lummus Powerformer Porvoo Trickle Reactor DC-10401 1 95+3 112.000 57 FV 500 - - 1973 73.1241

Finland - 6.550 - - -

5815 - - - 13 Cr Mo 4 4 - -

NESTE OY Lummus Powerformer Porvoo Powerformer Reactors DC-10301/2 2 43 75.000 20 FV 565 - - 1973 73.1242-01/02

Finland - 2.200 - - -

7700 - - - 13 Cr Mo 4 4 - -

NESTE OY Lummus Powerformer Porvoo Powerformer Reactor DC-10303 1 52 142.000 19 FV 565 - - 1973 73.1242-03

Finland - 4.850 - - -

5800 - - - 13 Cr Mo 4 4 S.S. Tp 321 -

NESTE OY Lummus Powerformer Porvoo Hydrofiner Reactor DC-10201 1 52 117.000 21 FV 540 - - 1973 73.1243

Finland - 9.300 - - -

3505 - - - SA 662 B - -

ARAMCO Fluor - Al Jubail 1st Stage Refrigerant Comp. 4 41 40.000 23 FV -46 - - 1974 74.1300-01

Saudi Arabia, Kingdom of Suction Drums 6.400 - - -

3960 - - - SA 662 B - -

ARAMCO Fluor - Al Jubail Reflux Drum 1 61 94.700 30 - -40 - - 1974 74.1300-02


2400 - - - 19 Mn 5 - -

AGIP Snamprogetti - Casirate D'Adda H.P. Columns 1001 C1/200 C1 2 112 164.000 155 - 70 - - 1975 75.1316

Italy - 18.600 - - -

3,465\1,755 - - -45 9 Ni - -

N.O.C. Stone & Webster Ethylene Ras Lanuf Demethanizer Tower 1 A 19 1 66\22 241.000 38 - -112 - - 1976 76.1402

Libya - 49.100 - - -

3000 - - - BS 1501-304S/15A - -

SHELL Ralph M. Parsons - St. Fergus Separators 1V-401/2V-401 2 101 71.000 106 - -125 - - 1977 77.1430

U.K. - 5.200 - - -

3000 - - 434 1¼ Cr ½ Mo S.S. Tp 347 w.o. -

IPRAS Badger - Izmit Reactor 36 C-202 1 104+4 87.500 67 FV 550 - - 1977 77.1456

Turkey - 6.800 - - -

2555 - - - C.S. - -

IPRAS Badger - Izmit Separator 36C-205 1 72 66.500 60 - 120 - - 1977 77.1457

Turkey - 10.000 - - -

2390 - - - K.C.S. - -

A.D.N.O.C. Fluor - Das Island, Abu Dhabi Separator No. 1 14D102 1 56 41.800 52 - 85 - - 1978 78.1477-01

United Arab Emirates - 7.500 - - -

2675 - - - K.C.S. - -

A.D.N.O.C. Fluor - Das Island, Abu Dhabi Vapour Dehydrators 14D201 A/B 2 63 37.900 52 - 320 - - 1978 78.1477-03



Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3275 - - - K.C.S. - -

A.D.N.O.C. Fluor - Das Island, Abu Dhabi Separator No. 1 24D102 1 62 77.400 42 - 85 - - 1978 78.1492-02


3855 - - - K.C.S. - -

A.D.N.O.C. Fluor - Das Island, Abu Dhabi Vapour Dehydrators 24D201 A/B 2 72 72.000 42 - 320 - - 1978 78.1492-03


2700 - - - SA 537 1 - -

A.D.N.O.C. Fluor - Das Island, Abu Dhabi Separator No. 1 24D301 1 50 42.600 42 - -45 - - 1978 78.1492-05


2625 - - - K.C.S. - -

A.D.N.O.C. Fluor - Das Island, Abu Dhabi Reboiler Outlet Drum Chilldown 1 37 30.200 32 - 85 - - 1978 78.1492-07

United Arab Emirates & Demethanisat. 24D304 8.100 - - -

2900 - - - ½ Mo - -

N.I.O.C. Ralph M. Parsons - Kangan Sweet Gas K.O.Drums 4 82 49.000 89 - 122 - - 1978 78.1494

Iran S4101/4201/4301/4401 4.250 - - -

1380 - - - K.C.S. - -

MOBIL OIL Bechtel Offshore North Sea Injection Compress.Suct.Scrubber 1 120 22.500 220 - -4 - - 1980 80.1587

U.K. D-3506 2.450 - - -

3,800\2,600 - - -100 SA 203 E - -

SAUDI PETROCHEM. Brown Worldwide Serv. Ethylene Al Jubail Demethanizer Column 11C8-11C9 1 58\41 275.000 35 - 93 SA 357 1 - 1981 81.1650


2600 - - - 1¼ Cr ½ Mo S.S. Tp 304L w.o. -

I.C.I.P. Technipetrol Hydrodesulphur. Mantova Hydrodesulphurization Reactor 1 65+4.5 53.000 53 - 565 - - 1983 83.1726

Italy PV-1751 8.500 - - -

2900 - - - SA 336 F22 Q+T S.S. Tp 316L w.o. -

SHELL Lummus Hycon Pernis Cold High Pressure Separator 1 178 190.000 190 - 170 - only for sump 1985 85.1758

The Netherlands - 7.800 - - -

2150 - - - SA 516 60 Inconel 625 w.o. -

O.N.G.C. INDIA LTD. Snamprogetti BPB Offshore S. Bassein Test Separator 13-V-540 1 132.5+4 52.500 118 - 132 - - 1987 87.1780

India - 4.200 - - -

2800 - - - SA 516 60 Inconel 625 w.o. -

O.N.G.C. INDIA LTD. Snamprogetti BPB Offshore S. Bassein Production Separator 16-V-560 A/B 2 172.5+4 83.000 118 - 132 - - 1987 87.1781

India - 7.200 - - -

2438 - - - SA 387 22 2 - -

ESSO Foster Wheeler Powerformer Augusta Reactor R 851-A 1 64 40.000 21 FV 552 - - 1987 87.1789-01

Italy - 5.380 - - -

3200 - - - SA 387 22 2 - -

ESSO Foster Wheeler Powerformer Augusta Reactor R 851-B 1 83 84.000 21 FV 552 - - 1987 87.1789-02

Italy - 8.050 - - -

3810 - - - BS 1503-622 Enhanced S.S. Tp 347 w.o. -

ESSO Davy McKee Residfiner Fawley Residfiner Lead Reactor R-101 1 235+4.5 630.000 216 - 448 - - 1988 88.1802-01

U.K. - 20.400 - - -



U.K. - 20.400 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]



U.K. - 20.400 - - -

1550 - - - BS 1501-224/430B - -

ESSO Davy McKee Residfiner Fawley Compressor K.O. Drum D-107 1 116 37.000 190,8 - 88 - - 1988 88.1803

U.K. - 5.500 - - -

2285 - - - BS 1501-622 Enhanced S.S. Tp 308L w.o. -

ESSO Davy McKee Residfiner Fawley H.P. Hot Separator D-102 1 121+4.5 87.000 185,5 - 448 - - 1988 88.1803-01

U.K. - 7.950 - - -


ESSO Davy McKee Residfiner Fawley H.P. Intermediate Separator D-103 1 85+6 31.000 180,8 - 362 - (partially) 1988 88.1803-02

U.K. - 4.750 - - -

1830 - - - BS 1501-223/490B S.S. Tp 308L w.o. -

ESSO Davy McKee Residfiner Fawley H.P. Cold Separator D-104 1 95+4.5 50.000 180,8 - 175 - - 1988 88.1803-03

U.K. - 6.700 - - -

1250 - - - BS 1501-224/430B - -

ESSO Davy McKee Residfiner Fawley Recycle Gas MEA Scrubber T-101 1 90 68.500 180,8 - 175 - - 1988 88.1803-04

U.K. - 16.770 - - -

9290 - - - C.S. - -

SARAS UOP FCCU Sarroch-Cagliari FCC Regenerator 1 30 220.000 - - - - - 1988 88.1806-01

Italy - 25.000 - - -

7134 - - - A 387 11 2 A 240 Tp 410S -

SARAS UOP FCCU Sarroch-Cagliari FCC Reactor K1-R1 1 30+3 - 3 - 550 - - 1988 88.1806-02

Italy - 20.000 - - -

4346 - - - A 387 11 2 - -

SARAS UOP FCCU Sarroch-Cagliari FCC Stripper 1 27 580.000 3,8 - 550 - - 1988 88.1806-03

Italy - 13.500 - - -

1868 - - - A 516 70\A 387 5 - -

SARAS UOP FCCU Sarroch-Cagliari FCC Riser 1 16 - 4,36 - 775 - - 1988 88.1806-04\05

Italy - 24.500 - - -

3292 - - - 13 Cr Mo 4 4 DIN17155 - -

MOBIL OIL Foster Wheeler FCCU Coryton refinery, Essex FCC Stripper 1 25 43.000 4 - 547 - - 1988 88.1808-01

U.K. - 7.500 - - -

1044 - - - A 516 70 - -

MOBIL OIL Foster Wheeler FCCU Coryton refinery, Essex FCC Riser 1 12 20.300 4,5 - 343 - - 1988 88.1808-02

U.K. - 12.000 - - -

3000 - - -80 SA 182 F321 S.S. Tp 316L w.o. -

Q.G.P.C. Bechtel/Technip J.Vent. Riser Treat.Plt. Offshore Expander Feed Drums 2 180+3 110.000 155 - 85 - - 1988 88.1814-03

Qatar 5101-V-02/5102-V-02 3.700 - - -

2700 - - -80 SA 182 F347 S.S. Tp 316L w.o. -

Q.G.P.C. Bechtel/Technip J.Vent. Riser Treat.Plt. Offshore Expander Outlet Drums 2 162+3 150.000 155 - 85 - - 1988 88.1814-04

Qatar 5101-V-03/5102-V-03 8.500 - - -

4820 - - - C.S. S.S. Tp 316L w.o. -

ARCO CHEMICAL CO. Badger Butanediol Channelview Hydrogen. Settling Drum D-57226 1 105+3 63.000 62 - 150 - - 1989 89.1826

Texas, U.S. - 9.000 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4420 - - -46 SA 537 1 - -

WESTLAKE POLYMERS M.W. Kellogg Ethylene Lake Charles C2 Splitter 3303-E 5 44,5 518.000 25,5 - -50 - - 1989 89.1840

Louisiana, U.S. - 59.817 - - -

1118 - - - SA 266 2 - -

EXXON Fluor Plastic Baton Rouge H.T. Recycle K.O. Pot V-1400F 1 168 29.250 344 - 260 - - 1989 89.1847-01

Louisiana, U.S. - 2.718 - - -

762 - - - SA 266 2 - -

EXXON Fluor Plastic Baton Rouge L.T. Cooler K.O. Pot V-1430F 1 115 10.450 344 - 260 - - 1989 89.1847-02

Louisiana, U.S. - 1.295 - - -

559 - - - SA 266 2 - -

EXXON Fluor Plastic Baton Rouge H.T.Recycle K.O. Pot V-1440F 1 85 5.450 344 - 260 - - 1989 89.1847-03

Louisiana, U.S. - 1.295 - - -

6553 - - - SA 516 70 SA 240 Tp 304 -

FORMOSA PLASTIC Scientific Design RE Point Confort Scrubber & K.O. Drum G-C-115 1 60+3 467.000 21,2 - 116 - - 1989 89.1850

Texas, U.S. - 29.565 - - -

4877 - - 38 SA 516 70 - -

ARAMCO Aramco DGA Unit Shedgum DGA Contactor R 79-C-001 1 143 449.500 83,31 - 163 - - 1989 89.1854


1000 - - - BS 1501-621/31B S.S. Tp 304L w.o. -

ESSO Bechtel Lubricants Fawley Reactor R 101 1 85+3 52.600 107 - 400 - - 1989 89.1856-01

U.K. - 29.400 - - -

1000 - - - BS 1501-621/31B - -

ESSO Bechtel Lubricants Fawley Reactor R 102 1 53\85 50.200 126 - 420 - - 1989 89.1856-02

U.K. - 23.700 - - -

1000 - - - BS 1501-451/400 - -

ESSO Bechtel Lubricants Fawley Reactor R 103 1 61 22.300 119 - 230 - - 1989 89.1856-03

U.K. - 8.720 - - -

1370 - - - BS 1501-224/460B - -

ESSO Bechtel Lubricants Fawley Isom. Hot Separator D-107 1 63 14.500 118 - 230 - - 1989 89.1856-04

U.K. - 3.500 - - -

1000 - - - BS 1501-151/400 - -

ESSO Bechtel Lubricants Fawley Reactor D 108 1 60 14.600 117 - 230 - - 1989 89.1856-05

U.K. - 5.620 - - -

8,000\6,500 0,8 - - SA 516 70 - -

ENICHEM TPL Ethylene Brindisi Primary Fractionary C-1501 1 20 205.000 3,8 - 300 - - 1989 89.1857-01

Italy - 35.500 - - -

7,000\500 0,8 - - SA 516 70 - -

ENICHEM TPL Ethylene Brindisi Quench Column C-1503 1 17 136.000 3,6 - 150 - - 1989 89.1857-02

Italy - 36.500 - - -

4400 - - - SA 516 70 - -

ENICHEM TPL Ethylene Brindisi Splitter C-3 1 31 323.000 19 - 80 - - 1989 89.1857-03

Italy - 80.550 - - -

4100 - - - SA 240 Tp 304 - -

FORMOSA PLASTIC Badger Ethyl Styrene Point Confort Reactors R 2011 - R 2012 2 16 83.000 1,78 FV 648 - - 1989 89.1858-01

Texas, U.S. - 13.000 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1400 - - - SA 387 11 2 - -

FORMOSA PLASTIC Badger Ethyl Styrene Point Confort Alkylation Reactors R 101 A/S 2 28 27.000 41,3 - 475 - - 1989 89.1858-02

Texas, U.S. - 12.600 - - -

6600 - - - SA 516 70 - -

EPSILON PRODUCT CO. Rust/Lucky Polypropylene Marcus Hook C-4001 Reactor 1 97 300.000 42,4 - 180 - - 1989 89.1859

Pennsylvania, U.S. - 39.000 - - -

1070 - - - SA 387 11 2 S.S. Tp 347 w.o. -

ESSO Bechtel Lubricants Fawley Hydrotreater Stripper T-101 1 60\49+4 27.400 100,7 - 400 - (partially) 1989 89.1861-01

U.K. Hot Sep. D-102/ Cold. Sep. D-103 24.145 - - -

1570 - - - BS 1501-224/460B - -

ESSO Bechtel Lubricants Fawley Vacuum Stripper T-102 1 18 17.000 2,4 FV 400 - - 1989 89.1861-02

U.K. - 16.665 - - -

1660 - - - BS 1501-224/460B - -

ESSO Bechtel Lubricants Fawley Condens. Blowdown Drum D-118 1 12 12.000 3,5 - 400 - - 1989 89.1861-03

U.K. - 10.800 - - -

4300 - - - SA 516 70 S.S. Tp 304L w.o. -

ANDHRA PETROCHEM. Davy McKee Oxo Visag Oxo Reactor 02/D131 1 41+3 69.000 22 - 145 - - 1989 89.1870-01

India - 9.660 - - -

1830 - - - SA 387 11 2 SA 240 Tp 304L -

STATOIL A/S Statoil MHC Kalundborg CFI Reactor R-851 1 45+3.2 90.000 53,9 - 460 - - 1989 89.1871

Denmark - 27.624 - - -

3800 - - - SA 542 B 4 Enhanced S.S. Tp 316L w.o. -

SARAS Snamprogetti MHC Sarroch-Cagliari Reactor HR-101 1 126+8 348.000 109 - 440 - - 1989 89.1872-01

Italy - 16.500 - - -

4300 - - - SA 542 B 4 Enhanced S.S. Tp 316L w.o. -

SARAS Snamprogetti MHC Sarroch-Cagliari Reactor HR-102 1 143+8 400.000 109 - 440 - - 1989 89.1872-02

Italy - 16.100 - - -

6310 - - -10 Fe510-2KG UNI5869 - -

ABIBES Belleli L.P.G. Deposit Cremona L.P.G. Tank SA1/SC1 2 19 128.000 12 - 35 - - 1990 90.1876

Italy 1,000 Cu.Mts. 29.850 - - -

7000 - - -10 Fe510-2KG UNI5869 - -

ABIBES Belleli L.P.G. Deposit Cremona L.P.G. Tank DS1/DS6 6 20 336.000 12 - 35 - - 1990 90.1877

Italy 3,000 Cu.Mts. 75.450 - - -

3200 - - - SA 387 11 2 - -

VALERO REF. CO. Fluor Platformer Corpus Christi Platforming Reactor 49-RX 01-04 1 60 300.000 11 - 543 - - 1990 90.1880

Texas, U.S. - 54.000 - - -

4860 - - - SA 387 11 2 (Refractory lined) -

SARPOM Foster Wheeler Powerformer Trecate Powerforming Reactors R-301/2/3 N 3 77 149.000 39 - 343 - - 1990 90.1885

Italy (Largest) 6.300 - - -

6800 - - 260 SA 516 60 S.S. Tp 405 -

N.I.O.C. JGC/TPL Oil Refinery Arak Athmospheric Column V-102 1 22+3 300.000 3,8 FV 385 SA 516 60 SB 127 1990 90.1891-01

Iran - 49.677 - - -

9450 - - 343 SA 516 60 S.S. Tp 405 -

N.I.O.C. JGC/TPL Oil Refinery Arak Vacuum Column V-151 1 27+3 339.000 2,41 FV 454 - - 1990 90.1891-02

Iran - 44.787 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

5486 - - 147 SA 516 60 S.S. Tp 405 -

N.I.O.C. JGC/TPL Oil Refinery Arak Recycle Splitter V-639 1 22+3 150.000 3,5 FV 413 SA 516 60 - 1990 90.1891-03

Iran - 36.350 - - -

4880 - - - SA 336 F22 S.S. Tp 308L w.o. -

UNOCAL Ralph M. Parsons FCC Feed Hydrot. Wilmington Reactor 130-D-202 (R1) 1 223+3 490.000 144 - 454 - - 1991 91.1907-01

California, U.S. - 13.100 - - -

4880 - - - SA 336 F22 S.S. Tp 316 w.o. -

UNOCAL Ralph M. Parsons FCC Feed Hydrot. Wilmington Reactor 130-D-201 (R1A) 1 223+8 228.000 144 - 454 - - 1991 91.1907-02

California, U.S. - 4.950 - - -

3376 - - -50 BS 1501-224/460-LT50 - -

MOBIL OIL Ralph M. Parsons BGP St. Fergus Molecular Sieve Vessels 3 163 138.000 125 - 290 - - 1991 91.1914

U.K. D-1701 A/B/C 12.000 - - -

5600 - - - SA 516 70 SB 127 -

N.I.O.C. Snamprogetti 2nd Stage Distill Bandar Abbas Atm. Columns V-01-001, V-71-007 2 43+3\12+3 373.000 3,5 - 395 - S.S. Tp 410S 1991 91.1915

Iran - 67.960 - - -

6400 - - - SA 516 70 - -

MONTECATINI Tecnimont Spherilene Lake Charles Reactor R-202 1 61 191.000 30 - 150 - - 1991 91.1916

Louisiana, U.S. - 22.800 - - -

3360 - - - SA 387 11 2 S.S. Tp 347 w.o. -

CLARK OIL & REF. CO. M.W. Kellogg Dehydrodesulph. Hartford Hydrotreater Reactors PV 120 1/2 2 70+4.5 140.000 62 - 382 - - 1991 91.1917

Illinois, U.S. - 26.000 - - -

3200 - - - SA 541 22 B S.S. Tp 316L w.o. -

AGIP RAFFINAZIONE Snamprogetti Long Res.Hydr. Taranto H.D.M. Reactors R 4121 / R 4122 2 220+8 657.000 214 - 445 SA 542 B 4 Enhanced - 1991 91.1918

Italy - 26.500 - - -

4000 - - - SA 387 11 2 S.S. Tp 316 w.o. -

PERTAMINA JGC/Foster Wheeler Hydrocracking Balongan Gas Oil Hydrotreater 14-R-101 1 122+4.5 192.000 84 - 455 - - 1991 91.1920-01

Indonesia - 14.200 - - -

2700 - - - SA 387 11 2 S.S. Tp 347 w.o. -

PERTAMINA JGC/Foster Wheeler Hydrocracking Balongan LCO Hydrotreater 21-R-101 1 95+4.5 125.000 84 - 455 - - 1991 91.1920-02

Indonesia - 15.700 - - -

4000 - - - SA 387 11 2 - -

PERTAMINA JGC/Foster Wheeler Hydrocracking Balongan HT Shift Reactor 22-R-103 1 54 52.700 27 - 470 - - 1991 91.1921

Indonesia - 4.150 - - -

4420 - - - SA 336 F22 S.S. Tp 347 w.o. -

FINA Fluor Hydrotreating Antwerpen Reactor D8111/D8121 2 305+9 510.000 196 - 454 SA 387 22 2 S.S. Tp 309 Nb + 1992 92.1934

Belgium - 13.500 - - -

1630 - - - SA 516 70 - -

FINA Fluor Hydrotreating Antwerpen H2S Absorber F 8111/F 8121 2 98 59.400 170 - 121 - - 1992 92.1935-01

Belgium F 8111/F 8121 14.000 - - -

1830 - - - SA 516 70 - -

FINA Fluor Hydrotreating Antwerpen Cold High Pressure Separator 2 111 37.600 168 - 121 - - 1992 92.1935-02

Belgium F 8112/F 8122 8.000 - - -

1400 - - - SA 516 70 - -

FINA Fluor Hydrotreating Antwerpen Recycle Comp. K.O. Drum 2 86 16.600 170 - 121 - - 1992 92.1935-03

Belgium F 8114/F 8124 6.000 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4115 - - - SA 387 22 2 S.S. Tp 347 w.o. -

NESTE OY Neste Oy Hydrotreating Kulloo Hydrotreater Reactor DC 2101 1 155+4.5 513.000 110 - 446 SA 336 F22 - 1992 92.1939

Finland - 23.400 - - -

3657 - - - SA 387 22 2 S.S. Tp 347 w.o. -

RAFF. MEDITERRANEA Snamprogetti LC-Finer Milazzo Reactor LCF 24-R-103 1 277+8 1.350.000 209 - 454 SA 336 F22 - 1992 92.1940

Italy - 38.100 - - -


SSANGYONG OIL REF. Mitsui/Toyo Hydrocracking Onsan Reactors R-30203 A/B 2 151+4.5 251.700 165 - 430 - - 1992 92.1946

Korea - 12.050 - - -

3353 - - - SA 336 F22 S.S. Tp 347 w.o. -

SHELL Foster Wheeler Hydrocracking Deer Park Reactors V-70002/3 2 207+8 491.000 172 - 454 - - 1993 93.1949

Texas, U.S. - 20.574 - - -

4000 - - - SA 516 60 - -

BARIVEN Foster Wheeler Platformer Cardon Separator Drum 41-V-102 1 89 161.000 50 FV 226 - - 1993 93.1950

Venezuela - 11.800 - - -

7000 - - -40 FeE390KT UNI5869 - -

API Belleli L.P.G. Deposit Falconara L.P.G. Tank D-7101/8 8 31 251.000 15,7 - 45 - - 1993 93.1951

Italy 1,500 Cu.Mts. 35.000 - - -

3500 - - - 12 Cr Mo 9 10 S.S. Tp 347 w.o. -

RUHR OEL Lurgi Desulphur. Gelsenkirchen-Horst Hydrier Reactor DC-3601 1 112+4.5 613.000 88 - 450 - - 1993 93.1954

Germany - 30.410 - - -

3450 - - - SA 387 11 2 S.S. Tp 347 w.o. -

SINGAPORE REF. CO. JGC Hydrofiner - Reactor 7201-D 1 102+4.5 341.000 82 - 450 - - 1993 93.1955

Singapore - 27.760 - - -

3500 - - - SA 516 65 - -

A.D.N.O.C. Technip O.G.D. Bab/Habshan, Abu Dhabi Drum 22-V-102 1 140 240.000 110 - 93 - - 1993 93.1961-01


3350 - - - SA 516 65 - -

A.D.N.O.C. Technip O.G.D. Bab/Habshan, Abu Dhabi Drums 24-V-101/6 6 136 235.000 110 - 120 - - 1993 93.1961-02


4300 - - - SA 516 65 - -



3500 - - - SA 516 65 - -



3660 - - - SA 516 65 - -

A.D.N.O.C. Technip O.G.D. Bab/Habshan, Abu Dhabi Drum 24-V-107 A/B 2 135 435.000 77 - 120 - - 1993 93.1961-05


3960 - - - SA 516 65 - -



4570 - - - SA 516 65 - -




Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

12000 - - - SA 204/SA 516 60 SA 240 Tp 316L -

RAYONG REFINERY CO. Thai Ref. Constr. Hydrocracking Rayong High Vacuum Column - 1 1 36+3\21 370.000 3,5 - 445 - - 1993 93.1962

Thailand - 37.220 - - -


RAYONG REFINERY CO. Thai Ref. Constr. Hydrocracking Map-Ta-Phut Hot HP Separator V-1702 1 162 108.600 209 - 430 - - 1993 93.1963

Thailand - 5.000 - - -

5000 - - 450 BS 1501-622 Enhanced - -

SHELL Fluor S.G.H.P. Pernis HTS Reactor R-6601 1 82 180.000 62 - 530 - - 1993 93.1969


3000 - - - BS 1501-622 Enhanced - -

SHELL Fluor S.G.H.P. Pernis Sulphur Guard Reactor R-6602 1 50 28.000 62 - 350 - - 1993 93.1970-01


5100 - - - BS 1501-622 Enhanced - -

SHELL Fluor S.G.H.P. Pernis L.T. Shift Reactors R-6603/04 2 82 106.900 62 - 350 - - 1993 93.1970-02/03


2700 - - - BS 1501-620B - -

SHELL Fluor S.G.H.P. Pernis Methanation Reactor R-6801 1 92 39.200 61 - 500 - - 1993 93.1970-04


2500 - - - SA 387 12 2 - -

REFINERIA DE PETROLEO Foster Wheeler Platformer Concon Platforming Reactor D371-D374 1 60 151.000 19,7 - 549 - - 1993 93.1972-01

Chile - 40.700 - - -

3600 - - - TStE355 + W.DIN17102 - -

N.A.M. Comprimo PS/UGS Grijpskerk Mercury Adsorber 4 116 79.000 110 - 90 - - 1994 94.1001

The Netherlands V 1110 A/B-V 1210 A/B 2.950 - - -

3500 - - - TStE355 + W.DIN17102 - -

N.A.M. Comprimo PS/UGS Grijpskerk Vert. K.O. Sep. 1st Stage V 4101 1 140 129.000 120 - 140 - - 1994 94.1001


3000 - - - TStE355 + W.DIN17102 S.S. Tp 316L w.o. -

N.A.M. Comprimo PS/UGS Grijpskerk Regen. Settlers V 1107 / V 1207 2 144+3 156.000 110 - 290 - - 1994 94.1001


2590 - - - SA 336 F22 S.S. Tp 309L w.o. -

CONOCO/PENNZOIL Brown & Root Hydrocracking Lake Charles Hot High Pressure Separator D 11002 1 184+4.5 130.500 205 - 412 - - 1994 94.1002-01

Louisiana, U.S. - 6.400 - - -

1680 - - - SA 336 F22 - -

CONOCO/PENNZOIL Brown & Root Hydrocracking Lake Charles Hot High Pressure Separator D 12002 1 110 58.300 191 - 360 - - 1994 94.1002-02

Louisiana, U.S. - 7.188 - - -

3100 - - -14 BS 1501-225/490B-LT20 Inconel 625 w.o. -

QATAR GAS Technip Offshore Qatargas upstream d. Int.3 phases Separator D5102-D5202 2 135 145.000 154 - 88 - (two layers) 1994 94.1974-01

Qatar - 9.350 - - -

1600 - - -8 BS 1501-225/490B-LT20 Inconel 625 w.o. -

QATAR GAS Technip Offshore Qatargas upstream d. Test Separator D5001 1 85 26.000 154 - 103 - (two layers) 1994 94.1974-02

Qatar - 4.000 - - -

3250 - - - 12 Cr Mo 9 10 S.S. Tp 308L -

SHELL ABB Lummus H.C.U. Pernis Hot H.P. Separator V1102 1 203+3 166.000 209 - 455 - - 1994 94.1977-01



Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3200 - - - 12 Cr Mo 9 10 S.S. Tp 316L -

SHELL ABB Lummus H.C.U. Pernis Cold H.P. Separator V1104 1 152+3 200.000 195 - 175 - - 1994 94.1977-02


2000 - - - SA 387 11 2 - -

MANGALORE REF. Toyo Platformer Mangalore Platforming Reactor DC2401-DC2404 1 27 97.200 8,8 - 549 - - 1994 94.1979

India - 42.650 - - -

2600 - - - SA 387 11 2 - -

JILIN AROMATICS Toyo Platformer Jilin Platforming Reactor 1 31 123.500 8,8 - 549 - - 1994 94.1980

China, People's Rep. of - 42.100 - - -

4915 - - - TStE355 + W.DIN17102 S.S. Tp 316L -

N.A.M. Comprimo PS/UGS Grijpskerk Silica Gel Adsorbing Vessel 6 176+3 311.000 110 - 140 - GUNITE lining 1994 94.1982

The Netherlands V-1103/1104/1105/1203/1204/1205 8.000 - - -

3400 - - - SA 387 11 2 - -

ESSO Foster Wheeler Platformer - Platforming Reactor PR-51/2/3/4 1 50 300.000 7,8 - 549 - - 1994 94.1983

Singapore - 65.800 - - -

4876 - - - SA 336 F22 S.S. Tp 309L/347 w.o. -

LYONDELL-CITGO Bechtel Cr./Vac. & Hydr. Pasadena Hydrotreater Reactor R-66-R-001 1 185+8 790.000 109 - 454 - - 1994 94.1986

Texas, U.S. - 26.520 - - -

6928 - - -10 Fe510-2KG UNI5869 - -

I.P.E.M. Belleli L.P.G. Deposit Brindisi L.P.G. Storage Tanks 5 36 506.000 20 - 50 - - 1994 94.1988

Italy 3,000 Cu.Mts. 75.416 - - -

3963 - - - SA 336 F22 S.S. Tp 308L w.o. -

CONOCO/PENNZOIL Brown & Root Hydrocracking Lake Charles 1st Stg. Hydrocraker Reactor RA-11001 1 322+4.5 1.002.500 224 - 454 - - 1994 94.1989-01

Louisiana, U.S. - 22.428 - - -

3963 - - - SA 336 F22 S.S. Tp 308L w.o. -

CONOCO/PENNZOIL Brown & Root Hydrocracking Lake Charles 2nd Stg. Hydrocraker Reactor RA-11002 1 311+4.5 902.400 217 - 454 - - 1994 94.1989-02

Louisiana, U.S. - 20.981 - - -

2591 - - - SA 336 F22 - -

CONOCO/PENNZOIL Brown & Root Hydrocracking Lake Charles Hydrodewaxer Reactor RA-12001 1 202 643.000 208,5 - 454 - - 1994 94.1989-03

Louisiana, U.S. - 28.347 - - -

2286 - - - SA 336 F22 - -

CONOCO/PENNZOIL Brown & Root Hydrocracking Lake Charles Hydrofinisher Reactor RA-12002 1 156 466.000 200 - 360 - - 1994 94.1989-04

Louisiana, U.S. - 33.680 - - -

3200 - - - SA 350 LF2 HIC - -

YUKONG Fluor FCCU Ulsan H.P. H2S Absorber DS-V1340 1 213 274.000 169 - 232 - - 1994 94.1991

Korea - 11.780 - - -

3200 - - - SA 516 60 - -

SERAYA CHEM. Chiyoda SM/PO Seraya Island PO Reactors R-301/2/3/4/5 5 100 71.100 73 - 200 - - 1994 94.1993

Singapore - 4.500 - - -

3500 - - - SA 387 11 2 S.S. Tp 321 -

SARAS Foster Wheeler Desulphur. Sarroch-Cagliari Desulph. Reactor R 471 1 44+3 168.700 34,3 FV 405 - - 1994 94.1994

Italy - 30.200 - - -

3500 - - - SA 387 11 2 S.S. Tp 321 -

SARAS Foster Wheeler Desulphur. Sarroch-Cagliari Desulph. Reactor R 781 1 56+3 198.100 44 FV 405 - - 1994 94.1994

Italy - 28.500 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2600 - - - SA 387 11 2 SA 240 Tp 321 -

AGIP RAFFINAZIONE Agip MDDW-HDS Taranto HDS Reactor R 403 1 66+3 98.700 64 - 440 - Cladded 1995 95.1007

Italy - 15.330 - - -

4915 - - - TStE355 + W.DIN17102 S.S. Tp 316L -

N.A.M. Fluor PS/UGS Norg Silica Gel Adsorbing Vessel 6 176+3 311.000 110 - 140 - GUNITE lining 1995 95.1009

The Netherlands V-1103/1104/1105/1203/1204/1205 8.000 - - -

4,115\6,503 - - - SA 516 70 - -

QUANTUM CHEMICAL Fluor Polyethylene La Porte Reactor C-4001 X 1 35\47\56 169.000 27 - 149 - - 1995 95.1012

Texas, U.S. - 22.060 - - -

3524 - - - SA 387 11 2 S.S. Tp 304L -

ICI PAKISTAN LTD. Foster Wheeler PTA Port Kasim Dissolver Reactor D1-1301 1 107+5 128.000 99 - 325 - Cladded 1995 95.1023

Pakistan - 9.000 - - -

3,200\2,200 - - - SA 387 11 2 - -

OAO OMSKIY NPZ Eurotecnica Reforming Omsk Platforming Reactor 300-R1/2/3/4 1 54\42 235.000 12 - 549 - - 1996 96.1029

Russia - 51.650 - - -

2800 - - - SA 516 65 - -

PETROGAL S.A. ABB Lummus Global H.D.S. Porto H.P. Separator D-3702 1 62 62.500 56 - 101 - - 1996 96.1030

Portugal - 10.000 HIC + NACE - -

3300 - - - Fe510-2KW UNI5869 - -

API ENERGIA ABB Lummus H.T. IGCC Falconara H2S Absorber T-8031 1 53 223.000 60 - 65 - - 1996 96.1035

Italy - 39.500 - - -

3,300\1,900 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha Scrub Column 15-C001 1 82\47 108.000 66 - 102 - - 1996 96.1038

Qatar - 17.700 - - -

2100 - - - SA 336 F22 S.S. Tp 347 w.o. -

SLOVNAFT Fluor Daniel/MHI Hydrocracking Bratislava HP/HT Separator 11-V-102 1 154+5 62.300 263 - 454 - - 1996 96.1039-01

Slovakia - 3.700 - - -

1500 - - - SA 336 F22 - -

SLOVNAFT Fluor Daniel/MHI Hydrocracking Bratislava HP Cat. Tranf. Vessel 11-V-401 A/B 2 124 30.600 227 - 454 - - 1996 96.1039-02

Slovakia - 3.600 - - -

3000 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha Reflux Drum 15-V005 1 74 50.000 66 - 120 - - 1996 96.1040-01

Qatar - 4.700 - - -

3000 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha HP MR Separator 16-V006 1 72 177.000 58 - 80 - - 1996 96.1040-02

Qatar - 9.700 - - -

6400 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha Dry Gas Flare K.O. 84-W002 1 16 85.300 3,5 - 180 - - 1996 96.1040-03

Qatar - 27.600 - - -

5700 - - - SA 387 11 2 S.S. Tp 347 w.o. -

RELIANCE BECHTEL/UOP Refinery Jamnagar Reactors MV-RH-351-R01/MV-RH-352-R01 2 100+4 270.000 51 FV 421 - - 1997 97.1047

India - 12.700 - - -

9600 - - - SA 516 70 SA 240 Tp 410S -

RELIANCE BECHTEL/UOP Refinery Jamnagar Crude Columns MV-RD311/312-C05 1 29\54 864.000 3,5 - 413 - SB 127 Monel 1997 97.1051-01

India - 68.700 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3200 - - - SA 285 C - -

RELIANCE BECHTEL/UOP Refinery Jamnagar Diesel Stripper MV-RD311/312/Light Keros.Stripper C08/C092 18\13 40.000 4 - 8 - - 1997 97.1051-02

India - 17.050 - - -

7500 - - - SA 516 70 SA 240 Tp 410S -

RELIANCE BECHTEL/UOP Refinery Jamnagar Vacuum Columns MV-RD321/322-C05 1 15\25 445.000 2 - 265 - - 1997 97.1051-03

India - 36.600 - - -

5800 - - - SA 516 70 - -

RELIANCE BECHTEL/UOP Refinery Jamnagar Stripper Columns MV-RD321/322-C05 2 60/38 189.000 17,7 - 216 - - 1997 97.1051-04

India - 27.500 - - -

3700 - - - SA 516 70 - -

RELIANCE BECHTEL/UOP Refinery Jamnagar Stabilizer Columns MV-RD321/322-C06 2 24\28 106.000 13,4 - 241 - - 1997 97.1051-05

India - 30.700 - - -

3300 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha Scrub Column 25-C-001 1 47\82 111.500 66 - 102 - - 1997 97.1059

Qatar - 17.700 - - -

3000 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha Reflux Drum 25-V005 1 74 50.000 66 - 120 - - 1997 97.1060-01

Qatar - 4.700 - - -

3000 - - - SA 240 Tp 304 - -

RAS LAFFAN LNG CO. JGC/M.W. Kellogg L.N.G. Doha HP MR Separator 26-V006 1 72 85.530 58 - 80 - - 1997 97.1060-02

Qatar - 9.700 - - -

1372 - - - SA 542 D 4a S.S. Tp 347 w.o. -

THE NEW ZEALAND SHELL Refinery - Reactor R-351 1 30+4 11.250 60 FV 425 - - 1997 97.1067

New Zealand - 7.010 - - -

2,900\3,200 - - 265 SA 516 70 - -

BECHTEL FRANCE SA BECHTEL/UOP - Jamnagar Diesel Strip./Light Kero 311-C08/C09 - 312-C08/C094 13\18 40.800 3,9 FV 293 - - 1998 97.1051-02

India - - - - -

5900 - - 224 SA 516 70 S.S. Tp 410S -

BECHTEL FRANCE SA BECHTEL/UOP - Jamnagar Vacuum Column RD 311-C16/312-C16 1 24 445.000 2,069 FV 265 - - 1998 97.1051-03

India - - - - -

3300 - - - SA 240 Tp 304 - -

JGC-KELLOGG JGC/M.W. Kellogg - Ras Laffan-Doha HP MR Separator 25-V005 1 72 85.530 58 - 80 - - 1998 97.1060-02

Qatar - - - - -

3070 - - - SA 240 Tp 304 - -

NPC PIDEC Oleflex Bandar Iman Butane Dehydrogen.Unit R-2001 1 18\21 39.500 14 - 654 - - 1998 98.1078-01

Iran - 24.200 - - -

2400 - - - SA 240 Tp 304 - -


Iran - 24.500 - - -

2700 - - - SA 240 Tp 304 - -


Iran - 25.500 - - -

2280 - - - Inconel 600 - -

NPC PIDEC Oleflex Bandar Iman Regeneration Tower R-2501 1 7 12.000 0,7 - 565 - - 1998 98.1078-04

Iran - 10.230 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2900 - - - 2¼ Cr 1Mo ¼ V S.S. Tp 347 w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking Queesland Hydrocracking Reactor 1501-D 1 171+4.5 431.000 187 - 454 - - 1998 98.1082-01

Australia - 23.400 - - -

3500 - - - 2¼ Cr 1Mo ¼ V S.S. Tp 347 w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking Queesland Hydrotreating Reactor 1502-D 1 196+4.5 383.000 181 - 441 - - 1998 98.1082-02

Australia - 14.600 - - -

3355 - - - SA 266 4 S.S. Tp 304L w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking Queesland HP Separator 1503-F 1 202+4.5 223.100 167 - 140 - - 1998 98.1082-03

Australia - 8.020 - - -

2387 - - - SA 387 11 2 - -

HELLENIC PETROL S.A. Exxon - Tessaloniki Powerforming React. R-402 1 45 32.000 44,8 - 552 - - 1999 99.1086

Greece - - - - -

2888 - - - SA 516 70 S.S. Tp 304L w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking Queesland Cold Low Pressure Separator 1505-F 1 67+4.5 58.000 56 - 140 - - 1999 99.1094

Australia - 8.230 - - -

5000 - - -42 P 355 NL2 UNI EN 10028/3- -

I.E.S. THESI Impianti L.P.G. Deposit Raffineria IES, Mantova L.P.G. Storage Tanks S137-S138-S139 3 28 139.700 18,5 - 50 - - 1999 99.1096-01

Italy 600 Cu.Mts. 29.730 - - -

1400 - - -42 SA 516 70 - -

I.E.S. THESI Impianti L.N.G. Raffineria IES, Mantova Flash Drum V-6001 1 10 3.600 3,5 - 90 SA 350 LF2 - 1999 99.1096-02

Italy - 2.300 - - -

4600 - - 663 X6 Cr Ni 18 11 - -

BASF RAYTHEON EB\SM Ludwigshafen Primary Styrene Reactor 1 21 203.500 2 FV 800 X3 Cr Ni Mo N 17 13 - 2000 00.1102-01

Germany - 36.300 X 10 Ni Cr Al Ti 32 20H - -

4600 - - 649 X6 Cr Ni 18 11 - -

BASF RAYTHEON EB\SM Ludwigshafen Secondary Styrene Reactor 1 22 210.850 0,44 - 800 - - 2000 00.1102-02

Germany - 30.270 - - -

3800 - - - SA 387 22 2 S.S. Tp 347 w.o. -

PETROBRAS TOYO Hydrotreating Rio Grande do Sul First Hydrotreatment Reactor 1 112+7.5 156.000 87,3 - 435 - - 2001 01.1114-01

Brazil - 8.130 - - -

3800 - - - SA 387 22 2 S.S. Tp 347 w.o. -

PETROBRAS TOYO Hydrotreating Rio Grande do Sul First Hydrotreatment Reactor 1 109+7.5 182.000 84,7 - 435 - - 2001 01.1114-02

Brazil - 10.670 - - -

4500 - - - 10 CrMo 9 10 S.S. Tp 347 w.o. -

FORTUM NESTE OY Hydrotreating Porvoo Reactor 1 94+4 200.000 63 - 425 - - 2001 01.1124

Finland - 12.400 - - -

4200 - - - SA 387 11 2 S.S. Tp 347 w.o. -

TOTALFINAELF Foster Wheeler Hydrotreating Lindsay HDS Reactor 1 93+4,5 335.000 60 - 425 - - 2002 02.1128

UK - 25.520 - - -

53,2 - - -20 SA 516 70 Inconel 625 -

REACTORSAZ Doris Gas Field Phases - Condensate Coalascer 4 2,5 16.500 139 - 120 - - 2002 02.1130-01

Iran - 118 - - -

70,9 - - -20 SA 516 70 Inconel 625 -

REACTORSAZ Doris Gas Field Phases - Free Water K.O. Drum 4 3,3 64.000 139 - 120 - - 2002 02.1130-02

Iran - 394 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

47,3 - - -20 SA 516 70 Inconel 625 -

REACTORSAZ Doris Gas Field Phases - Test Separator 2 2,2 19.500 139 - 120 - - 2002 02.1130-03

Iran - 197 - - -

4270 - - - 12 CrMo 9.10 Vd 404/1 S.S. Tp 316L w.o. -

OMV Fluor H.D.S. Schwechat First Stage Reactor 1 89+4.5 302.000 74 - 415 - - 2002 02.1132

Austria - 21.220 - - -

3200 - - - SA 387 22 2 S.S. Tp 347 w.o. -

I.E.S. Paragon Litwin Hydrotreating Raffineria IES, Mantova Makfining Reactor 1 105+4.5 309.000 90,2 - 454 - - 2002 02.1136

Italy - 26.500 - - -

4200 - - -26,3 SA 542 B 4 S.S. Tp 347 w.o. -

SLOVNAFT ABB/Haldor Topsoe Gasoil Deep Desulph.Bratislava HDS Reactor 1 91+7.5 299.000 73,1 F.V. 430 - - 2003 03.1139-01

Slovakia - 19.990 - - -

4200 - - -26,3 SA 542 B 4 S.S. Tp 347 w.o. -

SLOVNAFT ABB/Haldor Topsoe Gasoil Deep Desulph.Bratislava HDS Reactor 1 85+7.5 111.000 68,2 F.V. 430 - - 2003 03.1139-02

Slovakia - 4.900 - - -

4500 - - - SA 336 F22 3 S.S. Tp 347 w.o. -

MOTOR OIL (HELLAS) Technip/Coflexip Hydrocracking Corinth MCH Reactor 1 182+4.5 687.500 110,6 - 460 - - 2003 03.1140-01

Greece - 26.605 - - -

4100 - - - SA 336 F22 3 S.S. Tp 347 w.o. -

MOTOR OIL (HELLAS) Technip/Coflexip Hydrocracking Corinth HDT Reactor 1 180+4.5 773.000 128,6 - 425 - - 2003 03.1140-02

Greece - 33.121 - - -

4600 - - - SA 387 22 2 S.S. Tp 347 w.o. -

ERG RAFFINERIE Foster Wheeler Hydrotreating Priolo Desulph. Plant 1 84+4 276.000 46 - 420 - - 2003 03.1142

Italy - 17.000 - - -

2600 - - - BS 1501-224/490B - -

CONOCO/CRYSTATECH ABB Lummus Global GmbHGas Treatment Unit Emden H2S Absorber Tag 950-401 1 55 125.000 67 - 120 - - 2004 04.1146

Germany - 23.400 - - -

3800 - - - SA 336 F22 V S.S. Tp 316L w.o. -

SUNCOR DENVER REF. Jacobs Eng. Group Inc. Hydrotreating Commerce City Gohods Reactor W-1701 1 175+4,5 613.500 151 - 426 - - 2004 04.1147

Colorado - 29.600 - - -

3962 - - - SA 516 60 - -

VEBA OIL GHANI GIR ABB Lummus Global B.V. Crude Oil Treatment Facha-Zenad Heater/Treater Desalter Package V-424 1 18 55.000 6 - 95 - - 2004 04.1148

Libya - 18.288 - - -

3300 - - - SA 387 11 2 S.S. Tp 308L w.o. -

AKER KVAERNER Kvaerner PTA Zongheng Dissolver Reactor D1-1301 / D2-1301 2 133+8 200.000 120 - 350 - - 2004 04.1151


4420 - - - SA 387 22 2 S.S. Tp 347 w.o. -

ERGMED Foster Wheeler Hydrotreating Priolo Reactor R-4001 A 1 145+4 442.000 91,75 - 454 - - 2004 04.1152-01

Italy - 19.650 - - -

4420 - - - SA 387 22 2 S.S. Tp 347 w.o. -

ERGMED Foster Wheeler Hydrotreating Priolo Reactor R-4001 B 1 145+4 421.000 91,75 - 454 - - 2004 04.1152-02

Italy - 18.820 - - -

4100 - - - SA 387 22 2 S.S. Tp 347 w.o. -

ERGMED Foster Wheeler Hydrotreating Priolo Reactor 1800-R-101 1 134+4 487.000 93,4 - 420 - - 2004 04.1152-03

Italy - 26.100 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3000 - - - SA 542 D 4a S.S. Tp 347 w.o. -

NATREF Fluor Hydrotreating Sasolburg Unifiner Reactor D15002 1 85+4 227.000 95 - 430 - - 2004 04.1153

South Africa, Rep. of - 26.160 - - -

2438 - - - SA 387 22 2 S.S. Tp 347 w.o. -

JACOBS/SUNCOR Conoco Hydrotreating Denver H.P. Hot Separator 1 131+4.5 106.000 151 F.V. 401,8 - - 2004 04.1155

Colorado, U.S. - 7.190 - - -

4267 - - - SA 336 F22 3 S.S. Tp 347 w.o. -

MOTIVA ENTERPRISES Jacobs Eng. Group Inc. Hydrotreating Port Arthur Reactor VES 35985 1 203+4 853.500 136,5 F.V. 427 - - 2004 04.1157-01

Texas, U.S. - 23.012 - - -

3963 - - - SA 336 F22 3 - -

MOTIVA ENTERPRISES Jacobs Eng. Group Inc. Hydrotreating Port Arthur Reactor VES 35986 1 185 488.000 133 F.V. 426 - - 2004 04.1157-02

Texas, U.S. - 16.078 - - -

2900 - - - SA 336 F22 V S.S. Tp 347 w.o. -

FORTUM Fortum Hydrocracking Porvoo Interstage Stripper DA 71003 1 190+4.5 300.000 202 - 468 - - 2004 04.1158-01

Finland - 14.250 - - -

2400 - - - SA 336 F22 V S.S. Tp 347 w.o. -

FORTUM Fortum Hydrocracking Porvoo Wash Tower DA-71004 1 144+4.5 118.000 186,5 - 468 - - 2004 04.1158-02

Finland - 7.200 - - -

3000 - - - SA 336 F22 V S.S. Tp 347 w.o. -

FORTUM Fortum Hydrocracking Porvoo H.P./H.T. Separator FA-71004 1 180+4.5 128.000 186,5 - 468 - - 2004 04.1158-03

Finland - 5.150 - - -

3800 - - - SA 336 F22 3 S.S. Tp 309L/347 w.o. -

FORMOSA PETROCHEMICAL FPCC Hydrocracking Mailiao GUARD REACTOR R-9751 1 306+7 709.000 223 F.V. 455 - - 2005 04.1165-01

Taiwan - 15.393 - - -

3800 - - - SA 336 F22 3 S.S. Tp 309L/347 w.o. -

FORMOSA PETROCHEMICAL FPCC Hydrocracking Mailiao MAIN REACTOR R-9752 1 303+7 1.181.000 220,6 F.V. 455 - - 2005 04.1165-02

Taiwan - 29.445 - - -

3100 - - - SA 336 F22 3 S.S. Tp 309L/347 w.o. -

FORMOSA PETROCHEMICAL FPCC Hydrocracking Mailiao HDW REACTOR R-9801 1 239+7 612.000 222,6 F.V. 415 - - 2005 04.1165-03

Taiwan - 22.422 - - -

3100 - - - SA 336 F22 3 S.S. Tp 309L/347 w.o. -

FORMOSA PETROCHEMICAL FPCC Hydrocracking Mailiao HDF REACTOR R- 9802 1 224+7 439.000 213,8 F.V. 385 - - 2005 04.1165-04

Taiwan - 15.091 - - -

2700 - - - SA 336 F22 3 S.S. Tp 309/347 -

FPCC EXXON/HYUNDAI Refinery Mailiao High Temperature Separator 1 185+6,8 201.000 208,8 - 325 SA 387 F22 2 - 2005 05.1167-01

Taiwan - 10.591 - - -

2199 - - - SA 336 F22 3 S.S. Tp 309/347 -

FPCC EXXON/HYUNDAI Refinery Mailiao High Temperature Separator 1 154+6,8 133.000 209,8 - 2280 SA 387 F22 2 - 2005 05.1167-02

Taiwan - 9.423 - - -

2895 - - - SA 350 LF2 - -

FPCC EXXON/HYUNDAI Refinery Mailiao Low Temp. Separator 1 242 222.000 204 - 150 SA 516 70 - 2005 05.1167-03

Taiwan - 8.712 - - -

4876 - - - SA 336 F22 3 S.S. Tp 347 -

MOTIVA LLC SHELL Refinery Port Arthur HTU-5 Hydrotreater Reactor 1 185+4 964.000 112,7 - 427 SA 387 F22 2 - 2005 05.1169

Texas, U.S. - 26.517 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3200 - - - SA 336 F22 V S.S. Tp 347 -

SNAMPROGETTI SNAMPROGETTI Refinery S. Nazzaro de Burgundi First Stage Reactor 1 198,8 663.400 190 - 454 SA 542 Tp D Cl. 4A - 2005 05.1172

Italy - 30.988 - - -

4495 - - - SA 336 F22 V S.S. Tp 347 -

K.N.P.C. FLUOR/CLG Refinery Kuwait Upflow Reactors 6 289+144 787.000 204 - 454 - - 2005 06.1176


4500 - - - SA 336 F22 V S.S. Tp 347 -

GRUPA LOTOS FLUOR/TECHNIP Refinery Gdansk Demetalization Reactors 2 252+5 787.000 186 - 410 - - 2006 06.1181

Poland - 20.662 - - -

6000 - - - BS1501 622 ENH - -

IPS TOYO SHELL GTL Project Ras Laffan HPC Reactors 2 144 700.000 91,7 - 400 BS 1503 622 ENH - 2006 06.1182-01

Qatar - 20.275 - - -

1500 - - - BS1501 622 ENH - -

IPS TOYO SHELL GTL Project Ras Laffan HGU Reactors 2 24 42.000 54 - 300 BS 1503 622 ENH - 2006 06.1182-02

Qatar - 17.710 - - -

3200 - - - BS1501 622 ENH - -

IPS TOYO SHELL GTL Project Ras Laffan CDW Reactors 2 45 106.000 51 - 400 BS 1503 622 ENH - 2006 06.1182-03

Qatar - 14.450 - - -

3353 - - - SA 336 F22V S.S. Tp 347 -

PETRO-CANADA BANTREL Refinery Montreal Canada Isomax Reactor D4300 1 215+4 746.000 201 - 455 - - 2006 06.1183

Canada - 29.870 - - -

5500 - - - SA 336 F22 S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak HDS Reactor 1 213+4 1.302 114 - 411 - - 2007 07.1185-01

Iran - 34.650 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Guard Reactor 1 325+4 522 218 - 425 - - 2007 07.1185-02

Iran - 7.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak First Main Reactor 1 328+4 966 216 - 440 - - 2007 07.1185-03

Iran - 17.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Second Main Reactor 1 328+4 966 214 - 450 - - 2007 07.1185-04

Iran - 17.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Third Main Reactor 1 324+4 956 212 - 450 - - 2007 07.1185-05

Iran - 17.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Forth Main Reactor 1 321+4 948 210 - 450 - - 2007 07.1185-06

Iran - 17.000 - - -

4500 - - - SA 336 F22 V S.S. Tp 347 -

KNPC FLUOR Refinery Kuwait Fixed Reactor 8 287+4.5 959 202 - 454 - - 2008 08.1190-01


4800 - - - SA 336 F22 V S.S. Tp 347 -

KNPC FLUOR Refinery Kuwait Second Stage Reactor 1 289+4 1.230 190 - 454 - - 2008 08.1190-02



Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro First stage Hydrotreating Reactor 1 268+4 700.000 205,9 - 454 - - 2008 08.1191-01

Brazil - 14.046 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -


Brazil - 14.205 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro Second stage Hydrotreating Reactor 1 284+7 560.000 217,7 - 454 - - 2008 08.1191-03

Brazil - 9.687 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro Second stage Hydrotreating Reactor 1 284+7 105.000 217,7 - 454 - - 2008 08.1191-04

Brazil - 21.587 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro Hydrocraking Reactor 1 251+7 104.000 205 - 454 - - 2008 08.1191-05

Brazil - 25.253 - - -

3978 192 - - SA 336 F22 V S.S. Tp 347 -

INEOS SHELL Refinery Lavera Pretreat Reactor 1 185 +4 419 - - 454 - - 2009 09.1193

France - 18.670 - - -

4900 181,6 - - SA 336 F22 V S.S. Tp 347 w.o. -

LUKOIL Technip Refinery Bourgas First/Second stage Reactor 2 240+4 136.400 - - 454 SA 542 Tp D Cl. 4A - 2010 10.1196-01

Bulgaria - 34.160 - - -

3100 179 - - SA 336 F22 V S.S. Tp 347 w.o. -

LUKOIL Technip Refinery Bourgas HP Separator 2 150 107.000 - - 454 SA 542 Tp D Cl. 4A - 2010 10.1196-02

Bulgaria - 3.800 - - -

2500 190,3 - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky First Stage Reactor 1 127+4 364.000 - - 454 - - 2011 11.1203-01

Russia - 30.700 - - -

3800 190,3 - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky Second Stage Reactor 1 192+4 608.000 - - 454 - - 2011 11.1203-02

Russia - 21.000 - - -

3800 171,3 - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky DHT Reactor 1 172+4 426.500 - - 454 - - 2011 11.1203-03

Russia - 14.600 - - -

4400 181 - - SA 336 F22 V S.S. Tp 437 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky VGO Reactor 1 211+4 1.285.500 - - 454 - - 2011 11.1203-04

Russia - 37.600 - - -

2800 130,4 - - - S.S. Tp 347 -

UFANEFTEKHIM PETROCHIM Refinery Ufaneftekhim Hydrocraking Reactor 1 145+4 387.200 - - 460 SA 336 F22 CL 3 - 2011 11.1204

Russia - 28.130 - - -

965 - - - SA 350 LF2 CL2 S.S. TP 309L/308L -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse HP Centrifugal Separator 2 75+8 12.000 165,7 - 260 - - 2012 12.1206

Russia - 3.660 - - -

3000 - - - SA 350 LF2 CL2 S.S. TP 309L/308L -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse Cold HP Separator 2 233+7 232.000 166 - 260 - - 2012 12.1207.01

Russia - 7.360 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2650 - - - SA 350 LF2 CL2 - -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse Receiving Separator 2 215 122.000 166 - 260 - - 2012 12.1207.02

Russia - 3.470 - - -

1980 - - - SA 336 F22 CL 3 - -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse Hot Separator 2nd Stage 2 135 80.000 184,2 - 343 - - 2012 12.1207.03

Russia - 7.860 - - -

1100 - - - SA 516 G 70 - -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse Receiving Separator 3rd Stage 3 70 14.100 104,3 - 260 - - 2012 12.1207.04

Russia - 2.600 - - -

2490 - - - SA 336 F22 CL 3 - -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse Hot HP Hydrotreating Separator 2 155 135.000 170 - 343 - - 2012 12.1207.05

Russia - 8.340 - - -

2650 - - - SA 336 F22 CL 3 - -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Tuapse Hot HP Separator 1st Stage 2 165 130.000 170 - 343 - - 2012 12.1207.06

Russia - 6.500 - - -

3350 - - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Novokuibishevsk 1st Stage Hydrocraking Reactor 1 158+4 550.000 179,2 - 434 - - 2012 12.1209.01

Russia - 31.200 - - -

3660 - - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Novokuibishevsk 2nd Stage Hydrocraking Reactor 1 181 +4 476.000 196,9 - 454 - - 2012 12.1209.02

Russia - 19.100 - - -

850 - - - SA 516 GR.70 S.S. Tp 304L -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Condensate Stripper 1 21+3 35.000 49 - 295 - - 2012 12.1210.A01

Russia - 21.175 - - -

2500 - - - SA 387 GR.11 CL.1 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Hydrogenator Reactor 1 62 45.000 52,47 - 410 - - 2012 12.1210.B01

Russia - 5.100 - - -

2500 - - - SA 387 GR.11 CL.1 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Sulphur Adsorber 2 50 36.000 52,47 - 410 - - 2012 12.1210.B02

Russia - 3.400 - - -

2900 - - - SA 336 GR.F22 CL.3 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Prereformer Reactor 1 194 103.000 46,09 - 560 - - 2012 12.1210.B03

Russia - 1.900 - - -

4100 - - - SA 387 GR.11 CL.2 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd MT Shift Converter 1 62 77.000 40,7 - 360 - - 2012 12.1210.B04

Russia - 4.300 - - -

700\1.200 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Flash Gas Scrubber 1 18\26 25.800 41,67 - 300 - - 2012 12.1210.C01

Russia - 24.300 - - -

2.400\3.600 - - - SA 516 GR.70 S.S. Tp 316L -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Stripper Column 1 18+3\32 118.890 11,27 - 420 - - 2012 12.1210.C02

Russia - 24.400 - - -

1200 - - - SA 516 GR.70 S.S. Tp 316L -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Off-Gas Scrubber 1 12+3 28.200 10,78 - 150 - - 2012 12.1210.C03

Russia - 20.500 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1.200\2.000 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Sponge Adsorber 1 18\16 33.700 10,78 - 120 - - 2012 12.1210.C04

Russia - 22.100 - - -

6000 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Product Fractionator 1 34 501.000 3,92 - 415 - - 2012 12.1210.C05

Russia - 58.100 - - -

2200 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Diesel/Kerosene Stripper 1 18 73.000 4,41 - 330 - - 2012 12.1210.C06

Russia - 20.100 - - -

2000 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Diesel Vacuum Drier 1 12 34.000 3,43 - 240 - - 2012 12.1210.C07

Russia - 5.500 - - -

1.400\2.000 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Deethanizer 1 18\22 55.800 19,12 - 215 - - 2012 12.1210.C08

Russia - 26.100 - - -

1400 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Depropanizer 1 18 49.000 20,1 - 135 - - 2012 12.1210.C09

Russia - 24.400 - - -

2.000\2.400 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Debutanizer 1 16\18 76.000 12,25 - 195 - - 2012 12.1210.C10

Russia - 31.400 - - -

1200 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd Propane Amine Treater 1 30 30.300 52 - 120 - - 2012 12.1210.C11

Russia - 18.000 - - -

5200 - - - SA 336 F22V S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd 1st Stage Hydrocracking Reactor 1 238+4 1.089.000 173,6 - 454 - - 2012 12.1210.D01

Russia - 25.300 - - -

5200 - - - SA 336 F22V S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocraking Volgograd 2nd Stage Hydrocracking Reactor 1 229+4 845.000 167,2 - 454 - - 2012 12.1210.D02

Russia - 19.400 - - -

3400 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Feed Surge Drum 1 51 63.000 36,7 - 230 - - 2012 12.1210.F01

Russia - 10.800 - - -

4300 - - - SA 336 GR.F22 CL.3 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Hot Separator 1 232 242.000 158,2 - 420 - - 2012 12.1210.F02

Russia - 5.900 - - -

4300 - - - SA 387 GR.11 CL.2 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Hot Flash Drum 1 69 84.000 42,16 - 420 - - 2012 12.1210.F03

Russia - 7.200 - - -

2700 - - - SA 516 GR.70 S.S. Tp 316L -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Cold Separator 1 168+7 120.000 152,9 - 300 - - 2012 12.1210.F04

Russia - 7.200 - - -

3600 - - - SA 516 GR.70 S.S. Tp 316L -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Cold Flash Drum 1 62+7 68.000 41,67 - 300 - - 2012 12.1210.F05

Russia - 8.200 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2400 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Recycle Gas Knockout Drum 1 134 53.000 152,6 - 175 - - 2012 12.1210.F06

Russia - 3.800 - - -

1200 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd 1st Stage Suction Drum 1 20 2.700 36,28 - 120 - - 2012 12.1210.F07

Russia - 2.600 - - -

1000 - - - SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd 2nd Stage Suction Drum 1 32 4.500 74,04 - 120 - - 2012 12.1210.F08

Russia - 2.600 - - -

5000 100,9 - - SA 336 Gr 22 V S.S. Tp 347 -

KNPC GS Hydrotreating Mina Al Ahmadi Gas oil desulfurazion 1 113+4 595.000 - - 421,1 - - 2014 14.1221

Kuwait - 31.071 - - -

4600 67,7 - - SA 387 Gr 11 Cl2 S.S. Tp 347 -

PEMEX FOSTER WHEELER Refinery Salina Cruz HDS Reactor 1 111+4 451.000 - - 425 - - 2014 14.1222

Mexico - 24.710 - - -

4600 189 - - SA 336 Gr 22 V S.S. Tp 347 -

MAVEG CB & I Refinery Krasnodar Hydrocracker Reactor 2 230+4,5 748.000 - - 454 - - 2014 14.1223.01

Russia - 20.000 - - -

4000 189 - - SA 336 Gr 22 V S.S. Tp 347 -

MAVEG CB & I Refinery Krasnodar Hydrocracker Reactor 1 200+4,5 665.000 - - 454 - - 2014 14.1223.02

Russia - 24.000 - - -

4170 169 - - SA 336 Gr 22 V S.S. Tp 347 -

MAVEG CB & I Refinery Krasnodar Separator 1 151+4,0 222.000 - - 343 - - 2014 14.1223.03

Russia - 6.910 - - -

6000 129 - - SA 336 Gr 22 V S.S. Tp 347 -

PETRONAS TECNICSA REUNIDAS Refinery Pengerang HDS Reactor 1 174+4,0 1.054.000 - - 425 - - 2014 14.1224

Malaysia - 29.419 - - -

5500 - - - SA 336 F22 V S.S Tp 347 -

PETRONAS SINOPEC Refinery Pengerang 1st Reactor 1 289+4,0 516.000 198,3 - 454 SA 542 Tp D Cl. 4A - 2015 15.1228.01

Malaysia - 7.900 - - -

5500 - - - SA 336 F22 V S.S Tp 347 -

PETRONAS SINOPEC Refinery Pengerang 2nd Reactor 3 289+4,0 851.000 198,3 - 454 SA 542 Tp D Cl. 4A - 2015 15.1228.02

Malaysia - 14.600 - - -

3400 110 - - SA 965 F321 - -

SHELL CHEMICAL LINDE Refinery Lousiana Column Ethane Dryer 2 125 12.250 - - 265 SA 240 Tp 321 - 2015 15.1231.05

USA - 5.150 - - -


Thickness



ProcessLicensors:

Chevron, UOP, ExxonMobil, Lurgi, Axens, KBR, HaldorTopsoe, Shell

ASME, AD-Merkblatter, BS5500, Stoomwezen, FinnishCode, EN 1445

Design Codes:

Materials: 12CrMo9-102.25Cr-1Mo2.25Cr-1Mo Enhanced2.25Cr-1Mo-0.25V Modified

Length: 37.600 mm (TT)Internal Diameter: 6.000 mmWall Thickness: 328 mm

MaximumDimensions:

> 60 units built since 1997( > 120 units considering 2.25Cr-1Mo)

Units:

From 10 tons to 1380 tonsWeight:

HYDROCRACKING & HYDROTREATING REACTORS (VANADIUM MODIFIED)

REFERENCE LIST - REACTORS 2.25Cr-1Mo-0.25V SHEET: 1 of 3


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1372 - - - SA 542 D 4a S.S. Tp 347 w.o. -

THE NEW ZEALAND SHELL Refinery - Reactor R-351 1 30+4 11.250 60 FV 425 - - 1997 97.1067

New Zealand - 7.010 - - -

2900 - - - 2¼ Cr 1Mo ¼ V S.S. Tp 347 w.o. -

BP Fluor Daniel Hydrocracking Queesland Hydrocracking Reactor 1501-D 1 171+4.5 431.000 187 - 454 - - 1998 98.1082-01

Australia - 23.400 - - -

3500 - - - 2¼ Cr 1Mo ¼ V S.S. Tp 347 w.o. -

BP Fluor Daniel Hydrocracking Queesland Hydrotreating Reactor 1502-D 1 196+4.5 383.000 181 - 441 - - 1998 98.1082-02

Australia - 14.600 - - -

3800 - - - SA 336 F22 V S.S. Tp 316L w.o. -

SUNCOR DENVER REF. Jacobs Eng. Group Inc. Hydrotreating Commerce City Gohods Reactor W-1701 1 175+4,5 613.500 151 - 426 - - 2004 04.1147

Colorado - 29.600 - - -

3000 - - - SA 542 D 4a S.S. Tp 347 w.o. -

NATREF Fluor Hydrotreating Sasolburg Unifiner Reactor D15002 1 85+4 227.000 95 - 430 - - 2004 04.1153

South Africa, Rep. of - 26.160 - - -

2900 - - - SA 336 F22 V S.S. Tp 347 w.o. -

FORTUM Fortum Hydrocracking Porvoo Interstage Stripper DA 71003 1 190+4.5 300.000 202 - 468 - - 2004 04.1158-01

Finland - 14.250 - - -

2400 - - - SA 336 F22 V S.S. Tp 347 w.o. -

FORTUM Fortum Hydrocracking Porvoo Wash Tower DA-71004 1 144+4.5 118.000 186,5 - 468 - - 2004 04.1158-02

Finland - 7.200 - - -

3000 - - - SA 336 F22 V S.S. Tp 347 w.o. -

FORTUM Fortum Hydrocracking Porvoo H.P./H.T. Separator FA-71004 1 180+4.5 128.000 187 - 468 - - 2004 04.1158-03

Finland - 5.150 - - -

2997 - - - SA 542 D 4A - -

CNCL ITC KBR Ammonia Yunnan Ammonia Converter (Shell) 1 104 290.000 163 - 285 - - 2005 05.1170-01


3200 - - - SA 336 F22 V S.S. Tp 347 -

SNAMPROGETTI SNAMPROGETTI Refinery S. Nazzaro de Burgundi First Stage Reactor 1 198,8 663.400 190 - 454 SA 542 Tp D Cl. 4A - 2005 05.1172

Italy - 30.988 - - -

4495 - - - SA 336 F22 V S.S. Tp 347 -

KNPC FLUOR/CLG Refinery Kuwait Upflow Reactors 6 289+144 787.000 204 - 454 - - 2005 06.1176


4500 - - - SA 336 F22 V S.S. Tp 347 -

GRUPA LOTOS FLUOR/TECHNIP Refinery Gdansk Demetalization Reactors 2 252+5 787.000 186 - 410 - - 2006 06.1181

Poland - 20.662 - - -

3353 - - - SA 336 F22V S.S. Tp 347 -

PETROCANADA BANTREL Refinery Montreal Canada Isomax Reactor D4300 1 215+4 746.000 201 - 455 - - 2006 06.1183

Canada - 29.870 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Guard Reactor 1 325+4 522.000 218 - 425 - - 2007 07.1185-02

Iran - 7.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak First Main Reactor 1 328+4 966.000 216 - 440 - - 2007 07.1185-03

Iran - 17.000 - - -


Thickness




DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Second Main Reactor 1 328+4 966.000 214 - 450 - - 2007 07.1185-04

Iran - 17.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Third Main Reactor 1 324+4 956.000 212 - 450 - - 2007 07.1185-05

Iran - 17.000 - - -

4800 - - - SA 336 F22 V S.S. Tp 347 -

SEI -SINOPEC SINOPEC Refinery Arak Forth Main Reactor 1 321+4 948.000 210 - 450 - - 2007 07.1185-06

Iran - 17.000 - - -

4500 - - - SA 336 F22 V S.S. Tp 347 -

KNPC FLUOR Refinery Kuwait Fixed Reactor 8 287+4.5 959.000 202 - 454 - - 2008 08.1190-01


4800 - - - SA 336 F22 V S.S. Tp 347 -

KNPC FLUOR Refinery Kuwait Second Stage Reactor 1 289+4 1.230.000 190 - 454 - - 2008 08.1190-02


4900 - - - SA 336 F22 V S.S. Tp 309L/347 -


Brazil - 14.046 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -


Brazil - 14.205 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro Second stage Hydrotreating Reactor 1 284+7 560.000 218 - 454 - - 2008 08.1191-03

Brazil - 9.687 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro Second stage Hydrotreating Reactor 1 284+7 1.050.000 217,7 - 454 - - 2008 08.1191-04

Brazil - 21.587 - - -

4900 - - - SA 336 F22 V S.S. Tp 309L/347 -

PETROBRAS-COMPERJ - Hydrocracking Rio de Janeiro Hydrocraking Reactor 1 251+7 1.040.000 205 - 454 - - 2008 08.1191-05

Brazil - 25.253 - - -

3978 192 - - SA 336 F22 V S.S. Tp 347 -

INEOS SHELL Refinery Lavera Pretreat Reactor 1 185 +4 419.000 - - 454 - - 2009 09.1193

France - 18.670 - - -

4900 181,6 - - SA 336 F22 V S.S. Tp 347 w.o. -

LUKOIL Technip Refinery Bourgas First/Second stage Reactor 2 240+4 1.364.000 - - 454 SA 542 Tp D Cl. 4A - 2010 10.1196-01

Bulgaria - 34.160 - - -

3100 179 - - SA 336 F22 V S.S. Tp 347 w.o. -

LUKOIL Technip Refinery Bourgas HP Separator 2 150 107.000 - - 454 SA 542 Tp D Cl. 4A - 2010 10.1196-02

Bulgaria - 3.800 - - -

2500 190,3 - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky First Stage Reactor 1 127+4 364.000 - - 454 - - 2011 11.1203-01

Russia - 30.700 - - -

3800 190,3 - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky Second Stage Reactor 1 192+4 608.000 - - 454 - - 2011 11.1203-02

Russia - 21.000 - - -


Thickness




DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3800 171,3 - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky DHT Reactor 1 172+4 426.500 - - 454 - - 2011 11.1203-03

Russia - 14.600 - - -

4400 181 - - SA 336 F22 V S.S. Tp 437 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Achinsky VGO Reactor 1 211+4 1.285.500 - - 454 - - 2011 11.1203-04

Russia - 37.600 - - -

3350 - - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Novokuibishevsk 1st Stage Hydrocraking Reactor 1 158+4 550.000 179,2 - 434 - - 2012 12.1209.01

Russia - 31.200 - - -

3660 - - - SA 336 F22 V S.S. Tp 347 -

ROSNEFT NEFTOCHIMPROJEKT Hydrocracking Novokuibishevsk 2nd Stage Hydrocraking Reactor 1 181 +4 476.000 196,9 - 454 - - 2012 12.1209.02

Russia - 19.100 - - -

5200 - - - SA 336 F22 V S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd 1st Stage VGO Reactor 1 238+4 1.089.000 177 - 454 - - 2012 12.1210.D01

Russia - 25.300 - - -

5200 - - - SA 336 F22 V S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd 2nd Stage VGO Reactor 1 225+4 845.000 170,5 - 454 - - 2012 12.1210.D02

Russia - 19.400 - - -

5000 - - - SA 336 F22 V S.S. Tp 347 -

KNPC GS E&C Refinery Mina Al-Ahmadi GOD Reactor 1 113+4 709.000 100,9 - 421 SA 542 Tp D Cl. 4A - 2014 14.1221

Kuwait - 31.757 - - -

4600 - - - SA 336 F22 V S.S. Tp 347 -

AFIPKA CB&I Hydrocracking Afipsky 1st Stage Hydrocracking Reactors 2 230+4 748.000 189 - 454 SA 542 Tp D Cl. 4A - 2015 15.1223.01

Russia 20.000 - - -

4000 - - - SA 336 F22 V S.S. Tp 347 -

AFIPKA CB&I Hydrocracking Afipsky 2nd Stage Hydrocracking Reactor 1 200+4 665.000 189 - 454 SA 542 Tp D Cl. 4A - 2015 15.1223.02

Russia 24.000 - - -

4170 - - - SA 336 F22 V S.S. Tp 347 -

AFIPKA CB&I Hydrocracking Afipsky Hot High Pressure Separator 1 151+4 222.000 169 - 343 SA 542 Tp D Cl. 4A - 2015 15.1223.03

Russia 6.910 - - -

6000 - - - SA 336 F22 V S.S. Tp 347 -

PETRONAS TECNICAS REUNIDAS Refinery Pengerang Johor HDS Reactor 1 174+4 1.054.000 126,5 - 425 SA 542 Tp D Cl. 4A - 2015 15.1224

Malaysia 29.419 - - -

5500 - - - SA 336 F22 V S.S. Tp 347 -

PETRONAS SINOPEC Refinery Pengerang Johor 1st Reactor 1 289+4 516.000 198,3 - 454 SA 542 Tp D Cl. 4A - 2015 15.1228.01

Malaysia 7.900 - - -

5500 - - - SA 336 F22 V S.S. Tp 347 -

PETRONAS SINOPEC Refinery Pengerang Johor 2nd Reactors 3 289+4 851.000 198,3 - 454 SA 542 Tp D Cl. 4A - 2015 15.1228.02

Malaysia 14.600 - - -


Thickness


ProcessLicensors:

Chevron, UOP, ExxonMobil, Axens, KBR, Shell

Carbon Steel1.25Cr-0.5Mo2.25Cr-1Mo Standard2.25Cr-1Mo-0.25V Modified12CrMo9-10

Materials:

MaximumDimensions:

Tubes length: > 10.000 mmShell Diameter: 4.900 mm

Weight: From 10 tons to 365 tons

Units: > 800 units built since 1980

Design: All TEMA Type, Bolted In, Pill Box, Breech Lock, Combined Breech Lock-Bolted In

SHELL & TUBE HEAT EXCHANGERS

REFERENCE LIST - OIL & GAS HEAT EXCHANGERS SHEET: 1 of 29


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1016 71 - 460 ½ Mo - -

CEPSA Procon - Algeciras Platforming combined 8 - 23.000 62 - 543 SA 213 T11 - 1965 65.864 A/B/C

Spain Feed Exch. 5.284 1¼ Cr ½ Mo - -

660 50 - 177 C.S. - -

POWER GAS Lummus - Cape Town BFW Heater 2 - 13.000 366 - 199 SA 179 - 1965 65.917

South Africa, Rep. of - 6.096 C.S. - -

1350 50 - 274 C.S. - -

POWER GAS Procon - Algeciras Cracked Residuum Side 1 70 36.500 25 - 426 SA 268 Tp 410 - 1966 66.350 D

Spain Stream Cooler 4.877 C.S. S.S. Tp 405 -

840 50 - 274 C.S. - -

POWER GAS Procon - Algeciras Lower Intermediate Reflux 1 50 15.500 36 - 426 SA 268 Tp 410 - 1966 66.350 F

Spain Waste Heat Boiler 4.877 C.S. S.S. Tp 405 -

1347 33 - 0 C.S. - -

ESSO Ctip - La Spezia Combined Overhead Vaporizer 2 - 26.200 97 - -190 SA 213 Tp 304 - 1967 67.600 A

Italy - 6.096 S.S. Tp 304 - -

1067 45 - -112 S.S. Tp 304 - -

ESSO Ctip - La Spezia V-101 Overhead Condenser 4 - 18.000 97 - -123 SA 213 Tp 304 - 1967 67.600 B

Italy - 6.096 S.S. Tp 304 - -

635 87 - 288 C.S. - -

CALTEX Lummus - Bahrain Feed Effluent Exch. 3 - 9.000 73 - 363 SA 213 Tp 321 & 5340 Incoloy 800 1967 67.675 A/B/C

Bahrain - 5.284 ½ Mo S.S. Tp 321 -

635 87 - 340 5 Cr ½ Mo - -

CALTEX Lummus - Bahrain Feed Effluent Exch. 2 - 9.600 73 - 393 SA 213 Tp 321 - 1967 67.675 D

Bahrain - 5.284 ½ Mo S.S. Tp 321 -

788 87 - 427 1¼ Cr ½ Mo S.S. Tp 321 -

CALTEX Lummus - Bahrain Hydrogen/Eff. Exch. 1 - 15.500 73 - 435 SA 213 Tp 321 - 1967 67.675 E

Bahrain - 6.096 ½ Mo S.S. Tp 321 -

1016 73 - 204 C.S. - -

CALTEX Lummus - Bahrain Eff. Cooler 2 - 23.200 5 - 60 SB 111 B(Al.Brass) - 1967 67.675 G

Bahrain - 6.096 C.S. Lead w.o. -

1067 40 - 250 C.S. - -

DOW CHEMICAL Lummus - Terneuzen Steam Generator 1 - 27.500 66 - 650 SA 213 Tp 316 - 1968 68.801

The Netherlands - 5.995 S.S. Tp 316/ ½ Mo - -

864 4 - 340 ½ Mo - -

B.P. Ctip - Torino Stripper Reboiler 1 - 10.600 76 - 450 SA 213 Tp 321 - 1969 69.205

Italy - 6.096 ½ Mo S.S. Tp 321 -

940 160 - 385 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

Y.P.F. Lummus - - Combined Feed Exch. 6 - 28.700 151 - 468 SA 213 Tp 347 - 1969 69.268 A/B/C

Argentina - 4.572 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

1067 51 - 285 C.S. - -

ESSO Ralph M. Parsons - Aruba Kerosene Feed/Reactor Eff. 2 - 17.000 35 - 343 SA 213 Tp 304 - 1969 69.290 B

Netherlands Antilles - 6.096 ½ Mo S.S. Tp 304L -

1067 51 - 388 C.S. - -

ESSO Ralph M. Parsons - Aruba VCO Feed/Reactor Eff. 4 - 20.000 10 - 419 SA 213 Tp 304 - 1969 69.290 E


LEGENDA DESIGN Shell Side MATERIALS: Shell Material SIZE: Shell I.D.

CONDITIONS: Tube Side Tube Material Shell thk.

Channel Material Tubes length

List of Reference list (HE)1



DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

991 51 - 421 C.S. - -

ESSO Ralph M. Parsons - Aruba Treat Gas/Reactor Eff. 1 - 11.000 41 - 421 SA 213 Tp 304 - 1969 69.290 F


940 78 - 371 C.S. - -

ESSO Ralph M. Parsons - Aruba VCO Feed/Reactor Eff. 4 - 10.700 62 - 421 SA 213 Tp 304 - 1969 69.290 G


991 78 - 385 C.S. - -

ESSO Ralph M. Parsons - Aruba VCO Feed/Reactor Eff. 2 - 20.000 65 - 421 SA 213 Tp 304 - 1969 69.290 H


864 85 - -30 K.C.S. - 71.1107/72.1118

NAM Lummus - Assen Gas/Gas Exchanger 33 - 26.000 280 - -30 SA 179 - 1971 71.1026/70/82/99

The Netherlands - 9.398 K.C.S. - 73.1234

1065 66 - 290 ½ Mo - -

SHELL Shell - Stanlow 2nd Stage Reactor 1 - 22.000 77 - 190 SA 209 T1 - 1971 71.1055 A

U.K. Feed/Eff. Exch. 6.096 C.S. - -

1093 66 - 405 ½ Mo - -

SHELL Shell - Stanlow 2nd Stage Reactor 1 - 23.000 77 - 320 SA 209 T1 - 1971 71.1055 B

U.K. Feed/Eff. Exch. 6.096 ½ Mo - -

1093 66 - 500 1¼ Cr ½ Mo S.S. Tp 321 -

SHELL Shell - Stanlow 2nd Stage Reactor 1 - 27.600 77 - 420 SA 268 Tp 410 - 1971 71.1055 C

U.K. Feed/Eff. Exch. 6.096 ½ Mo - -

1220 65 FV 340 ½ Mo S.S. Tp 321 -

SHELL Shell - Stanlow Reactor Charge/Reactor 4 - 25.000 55 FV 425 SA 213 Tp 321 - 1971 71.1065 A-D

U.K. Eff. Exch. 6.096 ½ Mo S.S. Tp 321 -

788 166 - 469 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

ENTASA Tecnicas Reunidas Hydrocracking Tarragona Charge VS Reactor No.1 1 - 28.200 201 - 399 SA 213 Tp 321 - 1973 73.1232-01

Spain Eff. Exch. 5.182 C.S. S.S. Tp 308 w.o. -

737 173 - 443 2¼ Cr 1 Mo S.S. Tp 347 w.o. -


Spain Eff. Exch. 5.182 2¼ Cr 1 Mo - -

737 173 - 357 2¼ Cr 1 Mo - -


Spain Eff. Exch. 5.182 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

915 159 - 349 ½ Mo - -

ENTASA Tecnicas Reunidas Hydrocracking Tarragona Charge VS Reactor No.2 1 - 34.000 202 - 316 SA 209 T1 - 1973 73.1232-04

Spain Eff. Exch. 6.096 C.S. - -

889 20 - 232 C.S. - -

ENTASA Tecnicas Reunidas Hydrocracking Tarragona Cold Flash Liquid Exch. 1 - 17.500 157 - 304 SA 209 T1 - 1973 73.1232-05

Spain - 5.487 ½ Mo - -

1397 60 - 316 ½ Mo S.S. Tp 321 -

CONOCO Ralph M. Parsons - Immingham Virgin Desulfurizer 1 - 34.000 67 - 260 SA 213 Tp 321 - 1974 74.1253-07

U.K. - 6.706 ½ Mo S.S. Tp 321 -

712 92 - 264 K.C.S. SB 424 N08825 -

MONSANTO Lummus - Seal Sands Feed Effluent Interchangers 4 - 17.500 92 - 264 SB 163 N08825 - 1977 77.1443

U.K. - 8.484 K.C.S. SB 424 N08825 -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118 133 - 320 1 Cr ½ Mo - -

PETROBRAS Uhde - Araucaria BFW Preheater 1 - 33.000 265 - 380 SA 213 T22 - 1977 77.1447

Brazil - 4.344 2¼ Cr 1 Mo - -

864 22 - 269 C.S. - -

EDF Lummus - Montereau BFW Heater 2 - 18.000 173 - 218 SA 179 - 1977 77.1449

France - 10.210 Fe510-1KW UNI7660 - -

1093 26 - 85 3½ Ni - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed/Residue Gas Exch. 1 - 26.500 53 - -60 SA 334 3 - 1978 78.1491-01

United Arab Emirates - 14.656 3½ Ni - -

1778 26 - -45 K.C.S. - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed Chiller No.2 1 - 37.800 53 - -45 SA 179 - 1978 78.1491-03

United Arab Emirates - 15.850 K.C.S. - -

1245 26 - -100 3½ Ni - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed/Residue Gas Exch. No.2 1 - 30.000 53 - -60 SA 334 3 - 1978 78.1491-04


966 33 - 343 C.S. - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed/Demethanizer Reeboiler 1 - 21.000 53 - 343 SA 179 - 1978 78.1491-05

United Arab Emirates - 12.800 C.S. - -

1601 26 - 85 C.S. - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed Chiller No.1 1 93 71.500 43 - 85 SA 213 Tp 304L - 1978 78.1499-02

United Arab Emirates - 14.000 C.S. S.S. Tp 304L -

1550 26 - 85 3½ Ni - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed Residue Exch. No.1 1 - 51.000 43 - -60 SA 334 3 - 1978 78.1499-03


1296 43 - 85 3½ Ni - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed/Demethanizer Feed 1 - 10.500 43 - -60 SA 334 3 - 1978 78.1499-04


1550 26 - 85 K.C.S. - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed Chiller No.2 1 125 100.000 43 - -45 SA 179 - 1978 78.1499-05

United Arab Emirates - 15.850 K.C.S. - -

1347 26 - 85 3½ Ni - -

ADNOC Fluor Daniel - Das Island, Abu Dhabi Feed Residue Exch. No.2 1 - 30.000 43 - -85 SA 334 3 - 1978 78.1499-06


1220 159 - 455 2¼ Cr 1 Mo S.S. Tp 347 w.o. 1 layer -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Feed Effluent 2 - 49.400 174 - 427 SA 213 Tp 321 - 1980 80.1600-01

Mississippi, U.S. Breech Lock Type 4.877 2¼ Cr 1 Mo S.S. Tp 347 w.o. 1 layer -

1194 11 - 418 C.S. - -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Eff./Fract. Feed 2 - 35.600 157 - 440 SA 213 Tp 321 - 1980 80.1600-02

Mississippi, U.S. Breech Lock Type 6.096 ½ Mo S.S. Tp 347 w.o. 1 layer -

966 21 - 277 C.S. - -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Eff./Stripper Feed 1 - 21.500 156 - 321 SA 209 T1 - 1980 80.1600-03

Mississippi, U.S. Breech Lock Type 6.096 ½ Mo - -

966 21 - 277 C.S. - -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Eff./Stripper Feed 1 - 21.500 156 - 321 SA 179 - 1980 80.1600-04

Mississippi, U.S. Breech Lock Type 6.096 C.S. - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

966 176 FV 454 2¼ Cr 1 Mo S.S. Tp 347 w.o. 1 layer -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Feed Effluent 12 - 44.000 199 FV 440 SA 213 Tp 321 - 1980 80.1600-05



CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Hot HPS Vapor/Recycle Gas 6 - 46.700 173 FV 440 SA 213 Tp 321 - 1980 80.1600-06



CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent 2 - 27.000 223 FV 405 SA 213 Tp 321 - 1981 81.1655-01

California, U.S. Breech Lock Type 7.316 2¼ Cr 1 Mo S.S. Tp 347 w.o. 1 layer -

737 21 - 318 C.S. S.S. Tp 410 w.o. 1 layer -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Atm.Col.Feed (HOT) 1 - 16.000 204 FV 335 SA 213 Tp 321 - 1981 81.1655-02


737 21 - 318 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Atm.Col.Feed (COLD) 1 - 15.000 204 FV 335 SB 163 (Incoloy 800) - 1981 81.1655-03

California, U.S. Breech Lock Type 7.316 1¼ Cr ½ Mo S.S. Tp 347 w.o. 1 layer -

610 225 FV 193 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Recycle Gas 1 - 16.000 202 FV 210 SA 179 - 1981 81.1655-04

California, U.S. Breech Lock Type 4.877 C.S. - -

686 21 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Atm.Col.Circ.Reflux/Recycle Gas 1 - 14.500 224 FV 245 SA 213 Tp 321 - 1981 81.1655-05

California, U.S. Breech Lock Type 7.316 ½ Mo - -


CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (HOT) 1 - 30.000 227 FV 293 SA 213 Tp 321 - 1981 81.1655-06


712 200 FV 385 ½ Mo - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (COLD) 1 - 26.000 227 FV 293 SA 209 T1 - 1981 81.1655-07



CHEVRON Bechtel Hydrocracking Richmond Inter.Reactor Quench Exch. 2 - 36.000 225 FV 430 SA 213 Tp 321 - 1981 81.1655-08


762 38 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Atm.Col. Feed Exch. 1 - 16.000 200 FV 180 SA 179 - 1981 81.1655-09



CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (COLD) 1 - 63.000 224 FV 404 SA 213 Tp 321 - 1981 81.1655-10



CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (HOT) 1 - 66.000 224 FV 404 SA 213 Tp 321 - 1981 81.1655-11


712 21 - 343 C.S. S.S. Tp 347 w.o. 1 layer -

CHEVRON Bechtel Hydrocracking Richmond Inter. Reactor Quench 1 - 11.000 211 FV 454 SA 213 Tp 321 - 1981 81.1655-12


991 38 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond RX Eff./Atm. Col. Feed (HOT) 1 - 31.000 198 FV 274 SA 209 T1 - 1981 81.1655-13

California, U.S. Breech Lock Type 7.316 ½ Mo S.S. Tp 347 w.o. 1 layer -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

991 38 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond RX Eff./Atm. Col. Feed (COLD) 1 - 30.000 198 FV 274 SA 179 - 1981 81.1655-14


508 200 FV 233 ½ Mo - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Cold Feed/Eff. Exch.(HOT) 1 - 16.000 214 FV 165 SA 209 T1 - 1981 81.1655-15


508 200 FV 233 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Cold Feed/Eff.Exch.(COLD) 1 - 16.000 214 FV 165 SA 179 - 1981 81.1655-16



CHEVRON Bechtel Hydrocracking Richmond Reactor Hot Feed/Eff.Exch.(HOT) 1 - 19.000 214 FV 326 SA 213 Tp 321 - 1981 81.1655-17

California, U.S. Breech Lock Type 7.316 2¼ Cr 1 Mo - -

534 201 FV 385 2¼ Cr 1 Mo - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Hot Feed/Eff.Exch.(COLD) 1 - 19.000 214 FV 326 SA 213 Tp 321 - 1981 81.1655-18


1474 14 FV 549 1¼ Cr ½ Mo\K.C.S. - -

Q.C.P.C. Technip - Umm Sa'id Feed Effluent Heat Exch. 1301 1 - 55.000 17 - 472 SA 213 T11 - 1981 81.1657

Qatar - 11.000 1¼ Cr ½ Mo/C.S. - -

940 133 - 420 X10 Cr Ni Mo Nb 18 10 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Hot Feed Exch.E 7401-A 1 - 46.000 133 - 435 15 Mo 3 X2 Cr Ni 18 9 1981 81.1666-01

Germany - 6.910 10 Cr Mo 9 10 X2 Cr Ni Mo 18 10 -

940 133 - 380 X10 Cr Ni Mo Nb 18 10 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Hot Feed Exch.E 7401-B 1 - 44.800 133 - 421 15 Mo 3 X2 Cr Ni 18 9 1981 81.1666-02

Germany - 6.910 13 Cr Mo 4 4 DIN17175 X2 Cr Ni Mo 18 10 -

991 133 - 346 X10 Cr Ni Mo Nb 18 10 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Hot Gas Exch.E 7402 1 - 43.500 133 - 382 13 Cr Mo 4 4 DIN17175 X2 Cr Ni 18 9 1981 81.1666-03

Germany - 5.487 13 Cr Mo 4 4 DIN17175 X2 Cr Ni 18 9 -

966 26 - 320 X10 Cu Ni Ti 18 9 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Hot Oil Exch.E 7403 1 - 40.400 133 - 346 16 Mo 5 UNI5462 X2 Cr Ni 18 9 1981 81.1666-04

Germany - 6.960 C22.8 X2 Cr Ni 18 9 -

1016 133 - 325 X10 Cr Ni Mo Nb 18 10 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Feed Exch.E 7404 1 - 53.300 133 - 325 15 Mo 3 X2 Cr Ni Mo 18 10 1981 81.1666-05

Germany - 7.950 16 Mo 5 X2 Cr Ni 18 9 -

940 133 - 291 X10 Cu Ni Ti 18 9 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Cold Gas Exch.E 7405-A 1 - 42.000 133 - 325 16 Mo 5 UNI5462 - 1981 81.1666-06

Germany - 6.173 16 Mo 5 X2 Cr Ni 18 9 -

940 133 - 291 HII DIN17155 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Cold Gas Exch.E 7405-B 1 - 44.700 133 - 325 St35.8 - 1981 81.1666-07

Germany - 6.173 C22.8 - -

966 22 - 182 HII DIN17155 - -

SHELL Edeleanu Hydrocracking Godorf Reactor Effl.Fract.Feed Exch.E 7406 1 - 38.500 133 - 210 St35.8 - 1981 81.1666-08

Germany - 7.010 C22.8 - -

1321 59 - 343 SA 302 B SA 240 Tp 410S -

CONOCO C.F. Braun - West Lake CHDS Reactor Feed Reactor Effl. 1 - 32.000 68 - 315 SA 209 T1 - 1981 81.1667-01

Louisiana, U.S. - 7.190 SA 302 B - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1143 60 - 469 1¼ Cr ½ Mo S.S. Tp 304L -

CONOCO C.F. Braun - West Lake Reactor Effl. Gas Oil Feed Exch. 4 - 21.000 70 - 407 SA 179 S.S. Tp 410S 1981 81.1667-06

Louisiana, U.S. - 6.096 - - -

2388 25,6 FV 399 C.S. - -

N.ZL.SYNTH.FUELS CO. Bechtel - - Recycle Gas/Reactor Eff. Exch. 5 - 158.500 18,8 FV 455 SA 213 Tp 304L - 1981 81.1674-01

New Zealand E 0302A - E 306A 18.288 1¼ Cr ½ Mo - -

2388 25,6 FV 399 C.S. - -

N.ZL.SYNTH.FUELS CO. Bechtel - - Recycle Gas Reactor Eff. Exch. 5 - 158.500 18,8 FV 455 SA 213 Tp 304L - 1981 81.1674-02

New Zealand E 0302B - E 306B 18.288 C.S. S.S. Tp 304L -

1397 14,9 FV 404 C.S. - -

N.ZL.SYNTH.FUELS CO. Bechtel - - Regenerator Gas Interch. 2 - 28.000 10,3 FV 538 SA 209 T1 - 1981 81.1674-03

New Zealand E-0320 A/B 7.316 1¼ Cr ½ Mo - -

1728 16,4 FV 149 C.S. S.S. Tp 304L -

N.ZL.SYNTH.FUELS CO. Bechtel - - Excess Eff. Cooler E-307 A/B 2 - 49.000 6,6 - 77 SA 213 Tp 316L - 1981 81.1674-04

New Zealand - 9.068 C.S. Epoxy coated -

1474 18,8 FV 167 C.S. S.S. Tp 304L -

N.ZL.SYNTH.FUELS CO. Bechtel - - Reactor Eff. Cooler 8 - 35.000 6,6 - 77 SA 213 Tp 316L - 1981 81.1674-05

New Zealand E-0308 A/B toE-0311 A/B 9.322 C.S. Epoxy coated -

1194 190 FV 377 C.S. S.S. Tp 347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Hot Eff.Res.Exchs.E41/42-002A/B 4 - 60.300 143 FV 405 SA 213 Tp 321 - 1981 81.1677-01

Kuwait Breech Lock Type 6.096 1¼ Cr ½ Mo S.S. Tp 347 w.o. -

966 157 FV 348 1¼ Cr ½ Mo - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Warm Eff.Rec.Gas Exch.E-41/42-003 2 - 27.000 143 FV 377 SA 213 Tp 321 - 1981 81.1677-02


966 157 FV 293 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Cool Eff. Recycle Gas 2 - 34.700 143 FV 321 SA 179 - 1981 81.1677-03

Kuwait Exchs. E 41/42-005 6.096 C.S. - -

1778 40 FV 543 SA 387 12 2 - -

NZRC Badger/Chiyoda - Whangarei Feed Effluent E-450 A 1 - 110.000 43 FV 503 SA 213 T12 - 1982 82.1685-01

New Zealand - 3.048 SA 387 12 2 - -

1778 40 FV 286 C.S. - -

NZRC Badger/Chiyoda - Whangarei Feed Effluent E-450 B 1 - 94.300 43 FV 243 SA 179 - 1982 82.1685-02

New Zealand - 3.048 C.S. - -

1194 190 FV 377 C.S. S.S. Tp 347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Hot Eff.Res.Exchs.E81/82-002A/B 4 - 60.300 143 FV 405 SA 213 Tp 321 - 1982 82.1699-01


966 157 FV 348 1¼ Cr ½ Mo - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Warm Eff.Rec.Gas Exch.E-81/82-003 2 - 27.000 143 FV 377 SA 213 Tp 321 - 1982 82.1699-02


966 157 FV 293 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Cool Eff.Rec.Gas Exch.E-81/82-005 2 - 34.700 143 FV 321 SA 179 - 1982 82.1699-03

Kuwait Breech Lock Type 6.096 C.S. - -

712 175 FV 470 3 Cr 1 Mo S.S. Tp 347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 1st Stg.make-up Hyd./Effl.Exch. E-84-100 1 - 31.400 186 FV 470 SA 213 Tp 321 - 1983 83.1707-01

Kuwait Breech Lock Type 3.048 3 Cr 1 Mo - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

712 175 FV 470 3 Cr 1 Mo S.S. Tp 347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 2nd Stg.make-up Hyd./Effl.Exch. E-84-200 1 - 31.400 186 FV 470 SA 213 Tp 321 - 1983 83.1707-02


1220 18 FV 230 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 1st Stg.Effluent Steam Gen. E-84-102 1 - 41.100 171 FV 360 SA 209 T1 - 1983 83.1707-03

Kuwait Breech Lock Type 6.096 ½ Mo - -

1270 22 - 215 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 1st Stg.Eff/H2S Strip.Feed Exch.E-84.103 1 - 54.800 169 FV 290 SA 209 T1 - 1983 83.1707-04


1220 18 FV 230 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 2nd Stg.Eff.Steam Generator E-84-202 1 - 41.100 172 FV 360 SA 209 T1 - 1983 83.1707-05


762 196 FV 200 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi HHPS Vapor/Recycle gas Exch. E-84-203 1 - 27.200 176 FV 280 SA 209 T1 - 1983 83.1707-06


915 17,25 FV 66/-56 BS 1501-224/430-LT50 - -

SHELL M.E.L. - Bacton Feed Gas Chillers E-4040/E4041 2 71 24.800 93 - 66/-56 BS 3603-CFS/410-LT50 - 1984 84.1729

U.K. - 7.925 BS 1501-224/430-LT50 - -

1372 175 FV 470 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st Stg Reactor Feed/Effl. E-14-102 AB 2 - 181.200 195 FV 470 SA 213 Tp 321 - 1984 84.1733-01

Kuwait Breech Lock Type 6.706 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

1220 16 - 232 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st Stg Reactor Effl./Steam Gen.E-14-103 1 72 36.600 170 FV 395 SA 209 T1 - 1984 84.1733-02


1270 28 - 205 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st Stg Rct.Effl/H2S Strip.Feed E-14-104 1 - 50.800 170 FV 290 SA 179 - 1984 84.1733-03


712 175 FV 470 3 Cr 1 Mo S.S. Tp 347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st State Make up H2/React.Effl.E-14-105 1 - 14.400 186 FV 470 SA 213 Tp 321 - 1984 84.1733-04

Kuwait Breech Lock Type 3.048 3 Cr 1 Mo S.S. Tp 347 w.o. -

1372 175 FV 470 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage React.Feed/Effl. E-14-107 A/B 2 - 168.600 194 FV 455 SA 213 Tp 321 - 1984 84.1733-05

Kuwait Breech Lock Type 6.400 2¼ Cr 1 Mo S.S. Tp 347 w.o. -

1220 16 - 232 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage React.Effl/Steam Gen.E-14-108 1 72 36.600 172 FV 380 SA 209 T1 - 1984 84.1733-06


839 196 FV 235 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage HHPS Vapor/Recyc.Gas E-14-109 1 - 17.500 170 FV 280 SA 179 - 1984 84.1733-07


712 176 FV 470 3 Cr 1 Mo S.S. Tp 347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage Make UP M2/React.Effl.E-14-110 1 - 14.400 186 FV 470 SA 213 Tp 321 - 1984 84.1733-08

Kuwait Breech Lock Type 3.048 3 Cr 1 Mo S.S. Tp 347 w.o. -

839 214,5 FV 425 2¼ Cr 1 Mo S.S. Tp 304L w.o. -

SHELL Lummus Hycon Pernis Liquid Feed/HCON Reactor Effluent 2 - 43.000 214,5 FV 425 SA 213 T22 S.S. Tp 304L w.o. 1985 84.1757-03








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

813 214,5 FV 425 1 Cr ½ Mo - -

SHELL Lummus Hycon Pernis Gas Feed/HHP Separator off-gas 1 - 30.000 214,5 FV 425 SA 209 T1 S.S. Tp 304L w.o. 1985 85.1757-01


610 214,5 FV 425 1 Cr ½ Mo S.S. Tp 304L w.o. -

SHELL Lummus Hycon Pernis Liquid Feed/HHP Separator Off-Gas 6 - 22.000 214,5 FV 425 SA 213 T22 S.S. Tp 304L w.o. 1985 85.1757-02


712 214,5 FV 425 2¼ Cr 1 Mo S.S. Tp 304L w.o. -

SHELL Lummus Hycon Pernis Liquid Feed/HDM Reactor Effluent 2 - 34.200 214,5 FV 425 SA 213 T22 S.S. Tp 304L w.o. 1985 85.1757-04


839 214,5 FV 425 2¼ Cr 1 Mo S.S. Tp 304L w.o. -

SHELL Lummus Hycon Pernis Gas Feed/HCON Reactor Effluent 4 - 36.000 214,5 FV 425 SA 213 T22 S.S. Tp 304L w.o. 1985 85.1757-05


889 179,4 - 455 SA 336 F22 S.S. Tp 347 w.o. 1 layer -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Feed Effluent Exch. E 1210 A/B 2 - 36.400 195,1 - 441 SA 213 Tp 321 - 1986 86.1776-01

China, People's Rep. of Breech Lock Type 7.316 SA 336 F22 S.S. Tp 347 w.o. 1 layer -

813 29,5 - 227 SA 516 70 - -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Reactor Eff./Dist.Feed Exch. E 1230 1 - 16.500 177,5 - 441 SA 213 T11 - 1986 86.1776-02

China, People's Rep. of Breech Lock Type 6.096 SA 336 F11 - -

737 176,1 - 454 SA 336 F22 S.S. Tp 347 w.o. 1 layer -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Reactor Feed/React.Eff.Exch. A/B 4 - 26.400 197,9 - 440 SA 213 Tp 321 - 1986 86.1776-03


940 173,7 - 441 SA 336 F22 S.S. Tp 347 w.o. 1 layer -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Reactor Feed/HHPS Vapor Exch. A/B 2 - 37.500 200 - 427 SA 213 Tp 321 - 1986 86.1776-04


483 172,8 - 343 SA 336 F11 - -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli HHPS Vapor/Feed Gas Exch. A/B 2 - 11.000 201,7 - 296 SA 213 Tp 321 - 1986 86.1776-05

China, People's Rep. of Breech Lock Type 6.096 SA 336 F11 - -

712 100 - 343 SA 516 70 - -

LIAOYANG PETROCHEM. Fluor Daniel Ethylene Oxide Liaoyang Cycle Gas / BFW Preheaters 2 - 16.000 24 - 343 SA 213 Tp 304 - 1987 87.1799-01

China, People's Rep. of 41-E-111/112 1.730 SA 516 70 S.S. Tp 304L -

559 100 - 343 SA 516 70 - -

LIAOYANG PETROCHEM. Fluor Daniel Ethylene Oxide Liaoyang Cycle Gas / BFW Preheater 1 - 7.800 24 - 343 SA 213 Tp 304 - 1987 87.1799-02

China, People's Rep. of 41-E-113 1.905 SA 516 70 S.S. Tp 304L -

1448 216,5 - 434 BS 1503-622/530 S.S. Tp 308L w.o. -

ESSO Davy McKee Residfiner Fawley Feed/HPHS Vapor E-102 A/B 2 - 87.000 185,5 - 448 BS 3606-304/S22 - 1988 88.1804-01

U.K. - 6.096 BS 1503-622/530 S.S. Tp 308L w.o. -

788 216,5 - 370 BS 1503-622/560 - -

ESSO Davy McKee Residfiner Fawley Treat Gas/HPHS Vapor E-103 A/B 2 - 24.000 185,5 - 370 BS 3606-304/S22 - 1988 88.1804-02

U.K. - 4.877 BS 1503-622/560 S.S. Tp 308L w.o. -

762 216,5 - 318 BS 1503-622/560 - -

ESSO Davy McKee Residfiner Fawley Treat Gas/HPHS Vapor E-103 A/B 1 - 22.000 180,8 - 362 SB 163 N08825 - 1988 88.1804-03

U.K. - 4.877 BS 1503-622/560 S.S. Tp25 22 2 -

1042 164,7 - 437 SA 387 22 2 S.S. Tp 308L w.o. -

NESTE OY FINLAND Neste Oy Hydrocracking Porvoo Reactor Feed/Eff. Exch.EA-301 A,B,C/II 3 - 38.000 153,1 - 454 SA 213 Tp 321 - 1988 88.1813

Finland Breech Lock Type 7.747 SA 336 F22 S.S. Tp 308L w.o. -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2083 37 - 85/-100 SA 240 Tp 321 - -

Q.G.P.C. Bechtel/Technip J.Vent. Gas Umm Sa'id Gas/Gas Exchanger 6103 E 01 1 - 180.000 79,5 - 85/-100 SA 213 Tp 321 - 1988 88.1823-01

Qatar - 32.665 SA 182 Tp 321 - -

1245 79,5 - 85/-60 SA 240 Tp 321 - -

Q.G.P.C. Bechtel/Technip J.Vent. Gas Umm Sa'id Demethanizer Side Reboiler 6103 E 02 1 - 30.800 37,2 - 85/-100 SA 213 Tp 321 - 1988 88.1823-02

Qatar - 9.906 SA 182 Tp 321 - -

1397 79,5 - 85/-60 SA 240 Tp 321 - -

Q.G.P.C. Bechtel/Technip J.Vent. Gas Umm Sa'id Demethanizer Reboiler 6103 E 05 1 - 38.100 37,2 - 85/-60 SA 213 Tp 321 - 1988 88.1823-03

Qatar - 9.983 SA 182 Tp 321 - -

1093 24 - 200 SB 265 3 - -

HAMILTON BROS. Brown & Root Vickers Offshore Ravenspurn Export Gas Coolers CP-X-3004 A/B 2 - 23.500 205 - 200 SB 338 3 - 1988 88.1824

U.K. - 7.316 SA 350 LF2 SB 260 3 -

2490 4 - 816 SB 409 N08810 - -

CHEVRON Badger Styrene St.James Reactor Preheater TT-4229 1 - 66.000 1,8 FV 663 SA 249 Tp 304H - 1989 89.1830

Louisiana, U.S. - 7.316 SB 409 N08810 - -

2109 27,6 - 343 SA 516 70 Refractory lined -

CONOCO Foster Wheeler FCCU Humber Catalyst Cooler X 3438 1 - 85.200 41,3 - 288 SA 213 T11 - 1989 89.1845

U.K. - 6.858 SA 516 70 - -

1093 142 - 350 SA 182 F11 S.S. Tp 347 -

K.N.P.C. JGC Hydrocracking Mina Al-Ahmadi Tube bundles for E41/E42-E81/E82/004A 4 - 23.500 - - - SA 213 Tp 321 - 1989 89.1848-01

Kuwait Breech Lock Type 6.096 - - -

1143 142 - 150 SA 266 2 Inconel 625 -

K.N.P.C. JGC Hydrocracking Mina Al-Ahmadi Tube bundles for E41/E42-E81/E82/007A-B 4 - 18.800 - - - INCOLOY 880 - 1989 89.1848-02


1829 6 - 490 SA 387 11 1 - -

FINA Foster Wheeler C.C.R. Antwerp Combined Feed Exch. 2 - 142.000 10 - 540 SA 213 T11 - 1989 89.1869

Belgium Rod Baffles Type 23.495 SA 387 11 1 - -

1448 109 - 440 SA 336 F316L - -

SARAS Snamprogetti Hydrocracking Sarroch Charge Effluent Exch. 4 - 60.000 109 - 440 SA 213 Tp 316L - 1989 89.1874-01

Italy - 8.000 SA 336 F316L - -

940 109 - 340 SA 516 70 - -

SARAS Snamprogetti Hydrocracking Sarroch Effluent-BFW Exch. 1 - 18.000 17 - 330 SA 268 Tp 410 - 1989 89.1874-02

Italy Rod Baffles Type 6.046 SA 240 Tp 304L - -

3201 25 - 343 SA 516 70 - -

UNION CARBIDE Bechtel - Taft Cycle Gas Exchanger 1 161 215.000 25 - 343 SA 249 Tp 304 - 1990 90.1878

Louisiana, U.S. Rod Baffles Type 10.364 SA 516 70 SA 240 Tp 304L -

1093 24 - 200 SB 265 3 - -

HAMILTON BROS. Brown & Root Vickers Offshore Ravenspurn Intercoolers GC-X-3104 A/B/C 3 - 24.000 205 - 200 SB 338 3 - 1990 90.1882

U.K. - 7.316 SA 350 LF2 SB 265 3 -

1372 88 - 143 SA 516 70 SB 265 1 -

B.P. Brown & Root Vickers Offshore Bruce Field Dehydrator inlet Cooler X 06300 A/B 2 - 34.600 17 - 50 SB 338 2 - 1990 90.1883-01

U.K. - 7.800 SA 516 70 SB 265 1 -

1194 17 - 50 SB 265 3 - -

B.P. Brown & Root Vickers Offshore Bruce Field Export Compr. Suc. Cooler X 07301 A/B/C 2 - 18.500 88 - 102 SB 338 2 - 1990 90.1883-02

U.K. - 4.040 SA 516 70 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118 17 - 50 SB 265 3 - -

B.P. Brown & Root Vickers Offshore Bruce Field Export Compr. Suc. Cooler X 07301 A/B/C 3 - 18.100 155 - 148 SB 338 3 - 1990 90.1883-03

U.K. - 4.293 SA 350 LF2 - -

1626 50 - 270 SA 516 70 - -

SAMSUNG Haldor Topsoe Acetic Acid Ulsan Waste Heat Boiler E-1306 1 - 35.600 23,5 - 975 SA 209 T1 - 1990 90.1884

South Korea - 10.618 SA 204 B Refractory lined -

458 26,5 FV 239 SA 333 6 SB 265 2 -

SAFCO Chiyoda Melamine Dammam Carbamate Heater 16-E-204 1 - 7.000 229 FV 225 SB 338 3 - 1990 90.1890

Saudi Arabia, Kingdom of - 6.223 SA 266 2 - -

788 186 - 410 SA 336 F22 S.S. Tp 347 w.o. -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 A/B 2 - 23.000 166 - 455 SA 213 Tp 321 - 1990 90.1892

Turkey Breech Lock Type 5.000 SA 336 F22 S.S. Tp 347 w.o. -

788 186 - 370 SA 336 F22 S.S. Tp 347 w.o. -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 C/D 2 - 23.800 166 - 425 SA 213 Tp 321 - 1990 90.1892


788 186 - 300 SA 336 F11 - -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 E/F 2 - 21.600 166 - 375 SA 213 Tp 321 - 1990 90.1892


788 186 - 220 SA 266 2 - -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 G/H 2 - 22.000 166 - 315 SA 260 Tp 405 - 1990 90.1892


1829 6 - 540 SA 387 11 1 - -

BARIVEN Foster Wheeler Platformer Cardon Combined Feed Exch. 41-E-301 A/B 2 - 142.000 10 - 490 SA 213 T11 - 1991 91.1924

Venezuela Rod Baffles Type 23.495 SA 387 11 1 - -

1372 11,6 - 66 Fe410-1KW UNI5869 - -

SARAS Snamprogetti/IDI Alkylation Sarroch Heat Exchanger A1-E8 A/B 2 - 25.000 8,2 - 70 Fe35 - 1991 91.1926

Italy Rod Baffles Type 6.096 Fe410-1KW UNI5869 - -

2058 17,4 - 110 SA 516 70 - -

PETRAMINA JGC/Foster Wheeler Exor 1 Balongan C3 Splitter Reboiler 1 - 101.000 27 - 120 SA 179 (High Flux Type) - 1991 91.1927

Indonesia - 16.000 SA 516 70 - -

1931 28,2 - 545 SA 387 11 2 - -

NATREF Badger Platformer Sasolburg Combined Feed Exch. C-14007 1 - 160.000 38 - 500 SA 213 T11 - 1992 92.1931

South Africa, Rep. of - 26.924 SA387-11CL2 - -

813 140 - 240 SA 516 70 - -

NESTE OY Neste Oy Hydrotreating Kulloo Recycle Gas Heater EA-34002 1 - 14.000 106 - 350 SAF 2205 - 1992 92.1941

Finland - 2.770 SA 516 70 S.S. Tp 309LNB w.o. -

1194 120 - 415 SA 387 11 2 S.S. Tp 309LNB w.o. -

NESTE OY Neste Oy Hydrotreating Kulloo Reactor Feed Effl.H.E.EA-34000 A/F 6 - 40.500 108 - 445 SA 213 Tp 321 - 1992 92.1941

Finland Breech Lock Type 6.096 SA 336 F11 S.S. Tp 309LNB w.o. -

864 163,5 - 380 2¼ Cr 1 Mo - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6906 A/B 2 - 24.800 182 - 318 SA 213 Tp 304L S.S. Tp 347 w.o. 1992 92.1943-01

The Netherlands R-6902 Effl.-Recycle Gas Ex. 6.096 2¼ Cr 1 Mo shell side -

1245 182 - 384 5 Cr - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6905 A/B 2 - 58.000 164,8 - 409 SA 213 Tp 304L S.S. Tp 347 w.o. 1992 92.1943-02

The Netherlands R-6901 Feed-R6902 Eff.Ex. 6.096 2¼ Cr 1 Mo tube side -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1245 182 - 288 1¼ Cr ½ Mo - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6907 1 - 54.200 163,5 - 317 SA 213 Tp 304L S.S. Tp 347 w.o. 1992 92.1943-03

The Netherlands R-6901 Feed-HPHS Vapor Exch. 6.096 1¼ Cr ½ Mo tube side -

1245 182 - 192 C.S. - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6908 1 - 54.200 163,2 - 288 SAF 2205 Incoloy 825 1992 92.1943-04

The Netherlands Recycle Gas-HPHS Vapor Exch. 6.096 C.S. tube side -

1245 15,8 - 148 C.S. - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6909 A/D 2 - 38.100 163,2 - 175 SAF 2205 Incoloy 825 1992 92.1943-05

The Netherlands HPHS Vapor Condenser 6.096 C.S. tube side -

1245 182 - 437 2¼ Cr 1 Mo - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6910 1 - 66.500 182 - 450 SA 213 Tp 347 S.S. Tp 347 w.o. 1992 92.1943-06

The Netherlands R-6901 Feed-Effluent Exch. 6.096 2¼ Cr 1 Mo tube side & shell side -

1423 7,4 - 409 C.S. - -

ESSO Fluor Daniel Hydrocracking Rotterdam E-6904 A/B 2 - 67.600 165,8 - 450 SA 213 Tp 347 S.S. Tp 347 w.o. 1992 92.1943-07

The Netherlands R6902 Eff.Ex.-Fractionar feed 6.096 2¼ Cr 1 Mo tube side -

1194 70 - 320 SA 387 11 2 S.S. Tp 321 w.o. -

SINGAPORE REF. CO. JGC Hydrofiner Singapore Low Temp. Comb. Feed Exchanger 8 - 27.000 89 - 290 SA 213 Tp 321 - 1993 93.1956-01

Singapore 7201C-A/E/B/F and C/G/D/H 6.096 SA 387 11 2 S.S. Tp 321 w.o. -

1194 49 - 340 SA 516 60 S.S. Tp 321 w.o. -

SINGAPORE REF. CO. JGC Hydrofiner Singapore Reactor Effl. Stripper Feed Exch. 2 - 22.000 73 - 380 SA 213 Tp 321 - 1993 93.1956-02

Singapore 7202 CA/CB 4.877 SA 516 60 S.S. Tp 321 w.o. -

940 73 - 450 SA 387 11 2 S.S. Tp 321 w.o. -

SINGAPORE REF. CO. JGC Hydrofiner Singapore High Temp. Comb. Feed Exchanger 4 - 17.500 89 - 375 SA 213 Tp 321 - 1993 93.1956-03

Singapore 7203 C-A/C and B/D 6.096 SA 387 5 2 - -

889 146 - 371 SA 266 2 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Hot Fresh Feed Exch. E-1101 1 - 25.500 133 - 435 SA 213 Tp 321 - 1993 93.1965-01

China, People's Rep. of Breech Lock Type 5.000 SA 336 F22 S.S. Tp 347 w.o. -

889 150 - 365 SA 336 F11 S.S. Tp 347 w.o. -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Hot Recycle Gas Exch. E-1102 1 - 22.500 132 - 399 SA 213 Tp 321 - 1993 93.1965-02

China, People's Rep. of Breech Lock Type 3.506 SA 336 F22 S.S. Tp 347L w.o. -

889 147 - 293 SA 336 F11 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Cold Fresh Feed Exch. E-1103 A/B 2 - 21.400 130 - 371 SA 213 Tp 321 - 1993 93.1965-03


889 152 - 245 SA 336 F11 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Cold Recycle Gas Exch. E-1104 1 - 22.800 128 - 287 SA 213 Tp 321 - 1993 93.1965-04


889 16,2 - 214 SA 516 70 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Feed Effluent Exch. E 1210 A/B 2 - 12.900 127 - 252 SA 213 Tp 321 - 1993 93.1965-05

China, People's Rep. of - 5.000 SA 336 F11 S.S. Tp 347L w.o. -

839 5 FV -75/120 WStE315 - -

SHELL Fluor Daniel S.G.H.P. Pernis Claus Gas Cooler E-6514 1 - 6.800 3,5 FV -75/120 SA 334 6 - 1993 93.1968-11

The Netherlands - 4.877 WStE315 - -

1423 68 - 200 WStE315 S.S. Tp 304L w.o. -

SHELL Fluor Daniel S.G.H.P. Pernis Demin. Water Preheater E-6606 A/B 2 - 23.300 16 - 200 SA 213 Tp 304L - 1993 93.1968-12

The Netherlands - 3.404 HII DIN17155 S.S. Tp 304L w.o. -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1194\1930 16 - -75/120 TStE315 + W - -

SHELL Fluor Daniel S.G.H.P. Pernis Main Cooler E-6702 1 - 25.000 70 - -75/120 SA 334 6 - 1993 93.1968-13

The Netherlands - 7.316 TStE315 + W - -

1245\2082 16 - -75/120 TStE315 + W - -

SHELL Fluor Daniel S.G.H.P. Pernis Methanol Chiller E-6703 1 - 27.500 61 - -75/120 SA 334 6 - 1993 93.1968-14

The Netherlands - 6.884 TStE315 + W - -

3201 7 FV 200 HII DIN17155 - -

SHELL Comprimo Sulph. Rec. Unit Pernis 1st Sulphur Condenser E-702 1 - 102.500 4 - 343 SA 179 - 1993 93.1968-21

The Netherlands - 10.973 HII DIN17155 - -

2794 7 FV 200 HII DIN17155 - -

SHELL Comprimo Sulph. Rec. Unit Pernis 2nd Sulphur Condenser E-703 1 - 76.000 4 - 350 SA 179 - 1993 93.1968-22


2794 7 FV 200 HII DIN17155 - -

SHELL Comprimo Sulph. Rec. Unit Pernis 3rd Sulphur Condenser E-704 1 - 65.600 4 - 350 SA 179 - 1993 93.1968-23


2693 7 FV 200 HII DIN17155 - -

SHELL Comprimo Sulph. Rec. Unit Pernis Scot Gas Cooler E-802 1 - 58.000 4 FV 200 SA 179 - 1993 93.1968-24


1093 7 FV 200 HII DIN17155 - -

SHELL Comprimo SCOT Unit Pernis Regenerator Reboiler E-905 A/B 2 - 11.700 8 FV 200 SA 213 Tp 321 - 1993 93.1968-25


1093 7 FV 200 HII DIN17155 - -

SHELL Comprimo Regenerators Unit Pernis Regenerator Reboiler E-955 A/B 2 - 11.700 8 FV 200 SA 213 Tp 321 - 1993 93.1968-26


1296 4 - 250 HII DIN17155 - -

SHELL Comprimo S.R.U. Feed Sys. Pernis Combined Feed Gas Heaters E-053/054 2 - 8.800 20 FV 250 SA 179 - 1993 93.1968-27


1700\810 4 - 400 HII DIN17155 - -

SHELL Comprimo SCOT Unit Pernis E-801 B 1 - 21.600 78 FV 400 SA 268 Tp 410 Inconel 600 1993 93.1968-28

The Netherlands - 7.316 WStE355 DIN17102 - -

2005\1400 4 - 400 HII DIN17155 - -

SHELL Comprimo SCOT Unit Pernis E-801 A 1 - 50.800 78 FV 400 SA 179 - 1993 93.1968-28

The Netherlands - 7.316 WStE355 DIN17102 - -

1220 25 FV 300 HII DIN17155 - -

SHELL Lummus Hydrocracking Pernis HCU Feed/Hydrowax Exch. E-1301 A/B 2 - 22.700 27 FV 395 SA 213 Tp 316Nb - 1993 93.1968-31


1016 22 FV 300 HII DIN17155 - -

SHELL Lummus Hydrocracking Pernis Depropanizer Reboiler E-1510 1 - 14.200 24 FV - SA 179 - 1993 93.1968-32


1931 17 - 560 SA 387 11 2 - -

REFINERIA DE PETROLEO Foster Wheeler Platformer Concon Combined Feed Exchanger C-371 1 - 145.000 20 - 510 SA 213 T11 - 1993 93.1972-02

Chile - 20.066 SA387-11CL2 - -

635 186 - 371 SA 336 F22 S.S. Tp 347 w.o. -

LANZHOU PETR. & CHEM. Sinopec Lube Oil Hydro. Lanzhou HDF React.Feed/Eff.H.E.E-101A/B/C/D 4 - 16.200 175 - 395 SA 213 Tp 321 - 1994 94.1981








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

788 188 - 392 SA 336 F22 S.S. Tp 347 w.o. -

LANZHOU PETR. & CHEM. Sinopec Lube Oil Hydro. Lanzhou HDR React.Feed/Eff.H.E.E-101A/B/C 3 - 27.600 176 - 447 SA 213 Tp 321 - 1994 94.1981


1220 172 - 410 SA 336 F22 S.S. Tp 347 w.o. -

YUKONG Fluor Daniel FCCU Ulsan HHPS Vapor/Total Gas E 1330 1 - 56.700 229 - 360 SA 213 Tp 321 - 1994 94.1990

South Korea Breech Lock Type 6.096 SA 336 F22 S.S. Tp 347 w.o. -

1220 173 - 454 SA 336 F22 S.S. Tp 347 w.o. -

YUKONG Fluor Daniel FCCU Ulsan Reactor Feed/Effl. Exch. E 1310/11 2 - 55.000 216 - 384 SA 213 Tp 321 - 1994 94.1990

South Korea Breech Lock Type 6.096 SA 336 F22 S.S. Tp 347 w.o. -

2540\1524 5,7 - 180 SA 516 70 - -

YUKONG Fluor Daniel FCCU Ulsan Effluent LP Steam Gen. E 1340 1 - 36.000 170 - 250 SB 163 N08825 Incoloy 825 w.o. 1994 94.1990

South Korea Breech Lock Type 6.096 SA 336 F11 on tubesheet -

1448 50 FV 405 SA 204 B - -

ENEL Belleli Power plant 175 MWMonfalcone BFW Heater AP1 1 - 27.700 215,7 - 285 16 Mo 5 UNI5462mod - 1994 94.1999

Italy - 10.110 Fe510-1KW UNI7660 - -

889 196 - 275 SA 336 F11 S.S. Tp 347 w.o. -

ZHEN HAI REF.& CHEM. Sinopec Hydrocracking Ningbo Reactor Eff./Cold Recycle E 303 1 - 24.000 176 - 348 SA 213 Tp 321 - 1994 94.1003


1042 192 - 375 SA 336 F22 S.S. Tp 347 w.o. -

ZHEN HAI REF.& CHEM. Sinopec Hydrocracking Ningbo Reactor Eff./Hot Fr. Feed E 302A/B 2 - 35.000 177 - 398 SA 213 Tp 321 - 1994 94.1003


1042 192,2 - 375 SA 336 F22 S.S. Tp 347 w.o. -

ZHEN HAI REF.& CHEM. Sinopec - Zhen Hai Zhejiang Prov. Breech Lock E-302 A/B 2 103 37.500 177 - 398 SA 213 Tp 321 - 1995 94.1003-01

China, People's Rep. of - 660 SA 336 F22 S.S. Tp 347L -

889 196,2 - 725 SA 336 F11 S.S. Tp 347 w.o. -

ZHEN HAI REF.& CHEM. Sinopec - Zhen Hai Zhejiang Prov. Breech Lock E-303 1 91 25.000 175,8 - 348 SA 213 Tp 321 - 1995 94.1003-02

China, People's Rep. of - 660 SA 336 F11 S.S. Tp 347L w.o. -

940 115 - 455 SA 387 22 1 S.S. Tp 347 w.o. -

THAI PETROCHEM. IND. Stone & Webster Refinery Rayong Reactor Effl./Feed Exch. E-002 A/B 2 - 32.300 138 - 370 SA 213 Tp 321 - 1995 95.1016-01

Thailand Breech Lock Type 7.925 SA 336 F22 S.S. Tp 347 w.o. -

610 138 - 235 SA 516 70 - -

THAI PETROCHEM. IND. Stone & Webster Refinery Rayong Rec. Gas/HHPS Gas Exch.E-003 A/B 2 - 11.500 115 - 246 SA 179 - 1995 95.1016-02

Thailand Breech Lock Type 4.572 SA 105N - -

1524 183 - 438 SA 336 F22 S.S. Tp 347 w.o. -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura 1st Stg React.Effl./Hot Feed Exch.E-101 1 - 107.000 165 - 455 SA 213 Tp 321 - 1995 95.1017-01

Saudi Arabia, Kingdom of - 7.925 SA 336 F22 S.S. Tp 347 w.o. -

1270 188 - 377 SA 336 F22 S.S. Tp 347 w.o. -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura 1st Stg React.Effl./Rec.Gas Exch.E-102 1 - 57.600 164 - 399 SA 213 Tp 321 - 1995 95.1017-02


1194 183 - 349 SA 336 F22 S.S. Tp 347 w.o. -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura 1st Stg React.Effl./Cold Feed Exch.E-103 1 - 41.500 163 - 377 SA 213 Tp 321 - 1995 95.1017-03


1448 108 - 327 SA 387 22 2 - -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura Reactor Effl./Debutanizer FD Exch.E-104 1 - 56.000 162 - 355 SA 213 Tp 321 - 1995 95.1017-04








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

966 190 - 285 SA 336 F11 - -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura Hot Sep./1st.Stg Rec.Gas Exch.E-105 A/B 2 - 38.500 161 - 288 SA 268 Tp 410 - 1995 95.1017-05

Saudi Arabia, Kingdom of - 5.487 SA 336 F11 - -

1067 179 - 282 SA 336 F11 - -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura Hot Sep./2nd.Stg Rec.Gas Exch.E-206A/B/C 3 - 26.700 161 - 288 SA 268 Tp 410 - 1995 95.1017-06

Saudi Arabia, Kingdom of - 3.048 SA 336 F11 - -

1423 172 - 399 SA 336 F22 S.S. Tp 347 w.o. -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura 2nd Stg React.Effl./Hot Feed Exch.E-230 1 - 72.000 165 - 427 SA 213 Tp 321 - 1995 95.1017-07


1270 179 - 355 SA 336 F22 S.S. Tp 347 w.o. -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura 2nd Stg React.Effl./Rec.Gas Exch.E-231 1 - 53.600 164 - 399 SA 213 Tp 321 - 1995 95.1017-08


1143 175 - 305 SA 336 F11 - -

SAUDI ARABIAN OIL CO. Bechtel Hydrocracking Ras Tanura 2nd Stg Rea.Effl/Cold Feed Exch.E-232A/B 2 - 44.900 163 - 332 SA 213 Tp 321 - 1995 95.1017-09


813 152 - 226 SA 516 70 - -

K.N.P.C. Belleli Refinery Mina Abdulla Recycle Gas Preheater E-12-105/205 2 - 23.500 131 - 288 SA 213 Tp 321 S.S. Tp 347 w.o. 1995 96.1020

Kuwait Breech Lock Type 6.096 SA 182 F1 S.S. Tp 347 w.o. -

1702 10 FV 65 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Treated Gas Cooler 1/2 E-1105 2 - 65.700 60 - -20/80 SA 213 Tp 304L - 1996 96.1031-01

Nigeria - 7.316 SA 516 60 - -

1524\2210 10,4 FV -45/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Drain Recooler 1/2 E-1401 2 - 42.500 60 - -45/75 SA 210 A1 - 1996 96.1031-02

Nigeria - 7.646 SA 516 60 - -

1420\2794 10,4 FV -65/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Feed Gas/HP-MP C3 Evap. 1/2 E-1402 2 - 47.000 60 - -65/75 SA 210 A1 - 1996 96.1031-03

Nigeria - 9.144 SA 516 60 - -

1550\2794 10,4 FV -60/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Feed Gas/HP-MP C3 Evap. 1/2 E-1403 2 - 47.600 60 - -60/75 SA 210 A1 - 1996 96.1031-04

Nigeria - 9.144 SA 516 60 - -

2337 20 FV -20/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island LR MR Aftercooler 1/2 E-1410 2 - 107.400 13,5 FV 0/65 SA 179 - 1996 96.1031-05

Nigeria - 9.144 SA 516 60 - -

2363 37 FV 0/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island HP MR Aftercooler 1/2 E-1411 2 - 112.450 25 FV 0/65 SA 179 Finned - 1996 96.1031-06

Nigeria - 7.316 SA 516 60 - -

2312 60 FV 0/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island HP MR Aftercooler 1/2 E-1420 2 - 140.500 40 FV 0/65 SA 179 Finned - 1996 96.1031-07

Nigeria - 9.144 SA 516 60 - -

2057\4495 10,4 FV -45/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island MR/HHP C3 Evap. 1/2 E-1421 2 - 120.600 60 - -45/80 SA 210 A1 - 1996 96.1031-08

Nigeria - 11.176 SA 516 60 - -

2057\3810 10,4 FV -50/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island MR/HP C3 Evap. 1/2 E-1422 2 - 139.400 60 - -50/75 SA 210 A1 - 1996 96.1031-09

Nigeria - 14.986 SA 516 60 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2083 19 FV -45/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Propane Desuperheater 1/2 E-1430 2 - 50.600 13 FV 65 SA 210 A1 - 1996 96.1031-10

Nigeria - 6.096 SA 516 60 - -

2490 19 - -45/80 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Propane Cond. 1/2 E-1431 A/B/C 6 - 152.900 13 FV 65 SA 210 A1 Finned - 1996 96.1031-11

Nigeria - 12.500 SA 516 60 - -

2566 19 - -45/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Propane Subcooler 1/2 E-1432 2 - 79.200 13 FV -45/65 SA 210 A1 - 1996 96.1031-12

Nigeria - 7.316 SA 516 60 - -

785\1270 20,4 - -20/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Depropanizer Reboiler 1/2 E-1560 2 - 12.000 20 - -20/200 SA 179 - 1996 96.1031-13

Nigeria - 4.877 SA 516 60 - -

1800\2820 13,3 FV 148 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Regenerator Reboiler 1/2 E-1102 2 - 44.500 20 - 200 SA 213 Tp 304L - 1996 96.1031-21

Nigeria - 5.000 SA 516 60 - -

1042 3,5 FV 148 SA 240 Tp 304L - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Regen. Overhead Cond. 1/2 E-1103 2 - 15.000 10 FV 65 SA 213 Tp 304L - 1996 96.1031-22

Nigeria - 7.595 SA 516 60 - -

1800\2590 10,4 FV -65/75 SA 240 Tp 304 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Scrub Gen. Cond. 1/2 E-1404 2 - 50.000 60 - -115/75 SA 213 Tp 304 - 1996 96.1031-23

Nigeria - 4.800 SA 240 Tp 304 - -

2082\3606 10,4 FV -60/75 BS 1501-224/430-13 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island MR/MP C3 Evaporator 1/2 E-1423 2 - 124.000 60 - -60/75 SA 179 - 1996 96.1031-24

Nigeria - 13.513 BS 1501-224/430-13 - -

2108\3606 10,4 FV -65/75 BS 1501-304S/11 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island MR/LP C3 Evaporator 1/2 E 1424 2 - 118.000 60 - -88/75 SA 179 - 1996 96.1031-25

Nigeria - 12.500 BS 1501-304/S11 - -

610\1118 10,4 FV -60/75 BS 1501-224/430-13 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island LPG Recycl./Reinj.Cooler 1/2 E-1580 2 - 6.000 30,4 - -70/150 SA 179 - 1996 96.1031-26

Nigeria - 4.877 BS 1501-224/430-13 - -

1400\2005 10,4 FV -65/75 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Deethanizer Cond. 1/2 E-1551 2 - 32.800 23 - -89/150 SA 213 Tp 304 - 1996 96.1031-27

Nigeria - 8.000 SA 240 Tp 304L - -

610\1143 23,8 - -89/150 BS 1501-224/430-13 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Heat Exchanger 1/2 E-1550 2 - 6.400 20 - -89/150 SA 179 - 1996 96.1031-28

Nigeria - 4.877 BS 1501-224/430-13 - -

762\1194 31 - -46/125 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Heat Exchanger 1/2 E-1540 2 - 10.400 20,7 - -46/200 SA 179 - 1996 96.1031-31

Nigeria - 4.877 SA 516 60 - -

1321 7,2 - -8/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Heat Exchanger 1/2 E-1571 2 - 22.300 10 FV -8/65 SA 179 - 1996 96.1031-31

Nigeria - 7.316 SA 516 60 - -

966 19 - -46/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Heat Exchanger 1/2 E-1561 2 - 14.800 13,1 FV 46/65 SA 210 A1 - 1996 96.1031-32

Nigeria - 7.800 SA 516 60 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118\1956 8,1 - -8/150 SA 516 60 - -

NIGERIA LNG LTD. T.S.K.J. N.G.L. Bonny Island Heat Exchanger 1/2 E-1570 2 - 14.000 20 - -8/200 SA 179 - 1996 96.1031-33

Nigeria - 5.000 SA 516 60 - -

813 8,1 - -2/15 SA 515 60 S5 - -

NIGERIA LNG LTD. LNG - Bonny Island Condensate Prod. Cooler 1/2-E-1572 2 12 5.695 10 FV -4/13 SA 179 - 1996 96.1031-35

Nigeria - 3.810 SA 516 60 S5 - -

991 216 - 440 SA 182 F22 3 - -

MITSUBISHI Fluor Daniel Hydrocracking Bratislava Hydrog. Pre-Heat Exch. 11 E 101 1 79 26.000 38,5 - 454 SA 213 Tp 321 - 1996 96.1043-01

Slovak Republic - 3.048 SA 387 22 2 - -

839 38,5 - 360 SA 387 5 1 - -

MITSUBISHI Fluor Daniel Hydrocracking Bratislava Hydrog. Pre-Heat Exch. 11 E 104 A/B 2 19 11.000 216 - 360 SA 213 T5 - 1996 96.1043-02

Slovak Republic - 3.660 SA 387 22 2 - -

1296 34,3 FV 372 SA 387 11 2 S.S. Tp 321 -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR N° 4 Comb.Feed Exch.ME-RH471-S06 1 24 24.500 42,1 - 321 SA 213 Tp 304 - 1997 97.1064-01

India - 7.010 SA 387 11 2 - -

1093 26,4 FV 355 SA 387 5 2 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR Product Fract.Feed 361/362-S21-S31-S41 6 19 16.300 23,5 - 343 SA 268 Tp 410 - 1997 97.1064-02

India - 7.316 SA 387 5 2 - -

1296 26,4 FV 355 SA 516 70 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR Strip.BTM-HOT Feed RH 351-S13E/352-S13E2 21 30.300 23,5 - 343 SA 179 - 1997 97.1064-03

India - 9.144 SA 516 70 - -

1296 27,4 FV 343 SA 516 70 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR React.Effl.Stripp.Cold 351/352 S15 A/B/C/D 8 25 29.600 40 FV 367 SA 213 T11 - 1997 97.1064-04

India - 4.877 SA 387 11 2 - -

1601 27,4 FV 343 SA 516 70 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR React.Effl.LP Steam RH-351/352-S07 2 26 17.000 41,1 FV 375 SA 213 T11 - 1997 97.1064-05

India - 2.440 SA 387 11 2 - -

2007 50 FV 343 SA 516 70 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR React.Effl.LP Steam 351/352-S05 2 51 17.000 43,1 FV 406 SA 213 T11 - 1997 97.1064-06

India - 3.660 SA 387 11 2 - -

2007 28,4 FV 343 SA 516 70 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR React.Effl.MP Steam RH-351/352-S06 2 30 41.000 42,1 FV 399 SA 213 T11 - 1997 97.1064-07

India - 3.660 SA 387 11 2 - -

1499 22 FV 343 SA 516 70 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR MP Steam Generator ME-RH 471-S08 1 19 11.000 33,3 FV 372 SA 213 T11 - 1997 97.1064-08

India - 3.506 SA 387 11 2 - -

813 44,1 FV 394 SA 387 11 2 - -

BECHTEL FRANCE SA Bechtel Refinery JAMNAGAR React Effl-Recycle Gas RH 351/352-S02 2 19 4.700 57,3 FV 343 SA 268 Tp 410 - 1997 97.1064-09

India - 2.210 SA 387 11 2 - -

1093 102,9 FV 427/177 SA 387 22 2 S.S. Tp 347 -

BECHTEL FRANCE SA Bechtel Hydrotreating JAMNAGAR Hydr.-VGO Unionfining RH 361/362-S02/S324 57 19.091 84,3 FV 454/177 SA 213 Tp 321 - 1997 97.1065-01

India - 2.490 SA 387 11 2 S.S. Tp 347 -

1321 126 - 427 SA 266 2 S.S. Tp 347 -


India - 3.506 SA 387 11 2 S.S. Tp 347 -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

940 102,9 FV 404/177 SA 387 11 2 - -


India - 1.500 SA 387 11 2 S.S. Tp 347 -

1601 126,5 - 396 SA 266 2 S.S. Tp 347 -


India - 5.995 SA 387 11 2 S.S. Tp 347 -

1397 104,9 FV 256/177 SA 387 11 2 - -

BECHTEL FRANCE SA Bechtel Hydrotreating JAMNAGAR Hydr.-VGO Unionfining RH 361/362-S09A 2 63 36.946 76,4 FV 291/177 SA 213 T11 - 1997 97.1065-05

India - 4.496 SA387-11CL2 - -

1397 104,9 FV 256/177 SA 387 11 2 - -

BECHTEL FRANCE SA Bechtel Hydrotreating JAMNAGAR Hydr.-VGO Unionfining RH 361/362-S09B 2 63 36.946 76,4 FV 291/177 SA 213 T11 - 1997 97.1065-06

India - 4.496 SA387-11CL2 - -

1093 103,9 FV 343/177 SA 387 11 2 - -

BECHTEL FRANCE SA Bechtel Hydrotreating JAMNAGAR Hydr.-VGO Unionfining RH 361/362-S07 2 51 21.108 78,4 - 347/177 SA 268 Tp 410 - 1997 97.1065-07

India - 3.988 SA 387 11 2 - -

1016 38,5 FV 250 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Feed/LGO Product Exch. 2 25 17.700 25,8 FV 380 SA 249 Tp 316L - 1998 98.1077-01

United Arab Emirates - 6.096 SA 516 65 S.S. Tp 316L -

1042 38,7 FV 250 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Feed/HGO Product Exch. 2 26 18.200 25,8 FV 405 SA 249 Tp 316L - 1998 98.1077-02

United Arab Emirates - 6.096 SA 516 65 S.S. Tp 316 -

1220 38,7 FV 230 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Feed/ATM Resid Exch. 4 29 28.300 35 FV 385 SA 249 Tp 316L - 1998 98.1077-03

United Arab Emirates - 6.096 SA 516 65 S.S. Tp 410S -

1220\2235 11,9 FV 285 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi HGO Kerosene Reboiler 2 28 23.400 17,9 FV 405 SA 249 Tp 316L - 1998 98.1077-04

United Arab Emirates - 6.096 SA 516 65 S.S. Tp 410S -

1168\2185 11,9 FV 380 SA 516 65 S.S. Tp 316L -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi LGO Kerosene Reboiler 2 16\25 24.000 17,9 FV 405 SA 249 Tp 316L - 1998 98.1077-05

United Arab Emirates - 6.096 SA 516 65 S.S. Tp 316L -

534 12,1 - 80 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Caustic Solution Cooler 1 10 2.500 8,1 - 75 SB 338 2 - 1998 98.1077-06

United Arab Emirates - 5.487 SB 265 2 - -

1296 25,8 FV 160 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Feed/Preflash Tower Ovhd Exch. 12 30\23 28.600 38,7 FV 145 SA 214 - 1998 98.1077-07

United Arab Emirates - 6.096 SA 516 65 - -

1296 25,8 FV 230 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Feed/Kerosene PA Exch. 4 23 28.100 38,7 FV 160 SA 214 - 1998 98.1077-08


1321 25,8 - 295 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Feed/LGO PA Exch. 4 23 28.400 38,7 - 210 SA 214 - 1998 98.1077-09


1650\2260 12,7 FV 285 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi LGO PA Kerosene Reboiler 2 20 34.000 18,9 FV 315 SA 214 - 1998 98.1077-10








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1347 10,9 FV 100 SA 516 60 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Stabilizer Overhead Trim Condenser 2 14 17.100 9,9 - 75 SA 179 - 1998 98.1077-11


864\1725 12,4 FV 170 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Kerosene PA Stabilizer Reboiler 2 15 12.500 18,6 FV 250 SA 179 - 1998 98.1077-12


785\1575 12,2 FV 170 SA 516 65 - -

ADNOC Snamprogetti Condensate ProcessingRuwais, Abu Dhabi Kerosene PRO Stabilizer Reboiler 2 14 8.000 18,6 FV 270 SA 179 - 1998 98.1077-13


2058 6,5 - 555/288 SA 240 Tp 304 - -

NPC Pidec Oleflex Bandar Iman Hot Combined Feed Exch. 2 18 115.000 4,5 - 605/288 SA 213 Tp 304 - 1998 98.1078-05

Iran - 18.288 SA 240 Tp 304 - -

788 176 - 434 SA 387 22 2 S.S. Tp 347 w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking BP REF (BULWER ISLAND)HCR Feed/Effl.Exch. 1501C 1 55 13.430 194 - 434 SA 213 Tp 321 - 1998 98.1083-01

Australia - 4.268 SA 336 F22 S.S. Tp 347 w.o. -

1245 175 - 416 SA 387 22 2 S.S. Tp 347 w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking BP REF (BULWER ISLAND)HDT Feed/Effl.Exch. 1502C 1 81 43.630 182 - 416 SA 249 Tp 321 - 1998 98.1083-02


1169 174 - 412 SA 387 22 2 S.S. Tp 347 w.o. -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking BP REF (BULWER ISLAND)HCR Feed/Effl. Exch. 1503C 1 76 32.661 195 - 412 SA 249 Tp 321 - 1998 98.1083-03


1067 116 - 380 SA 516 70 - -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking BP REF (BULWER ISLAND)Effl./Stripper Feed Exch. 1504C 1 68 36.059 173 - 406 SA 213 Tp 321 - 1998 98.1083-04

Australia - 6.096 SA 387 22 2 S.S. Tp 347 w.o. -

915 196 - 363 SA 387 22 2 - -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking BP REF (BULWER ISLAND)Effl./Feed Gas Exch. 1507C 1 68 21.010 172 - 380 SA 249 Tp 321 - 1998 98.1083-05


1194 114 - 343 SA 516 70 - -

IPM - FLUOR CANADA Fluor Daniel Hydrocracking BP REF (BULWER ISLAND)Effl./LPS Liquid Exch. 1508C 1 66 51.900 171 - 343 SA 213 T11 - 1998 98.1083-06

Australia - 7.316 SA 387 22 2 - -

991 32,2 - 165 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Top Pump.Vac.Gasoil/Feed EA-1001A/B/C/D/E/F/G/H8 22 12.600 21,5 - 190 SA 179 - 1999 99.1095-01

Egypt - 5.995 SA 516 70 - -

940 28 - 195 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Sec.Cold Val.Res./Feed Exch. EA-1002 1 19 11.350 32,2 - 171 SA 179 - 1999 99.1095-02

Egypt - 5.995 SA 516 70 - -

940 215 - 315 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Middle Pump/Feed Exch. EA-1003 1 15 10.650 322 - 220 SA 179 - 1999 99.1095-03

Egypt - 5.995 SA 516 70 - -

889 21,5 - 319 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Med.Waxy Dist./Feed Exch. EA-1004 1 14 9.350 32,2 - 230 SA 179 - 1999 99.1095-04

Egypt - 5.995 SA 516 70 - -

788 21,5 - 339 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Heavy Waxy Dist./Feed Exch. EA-1005 1 12 7.400 32,2 - 238 SA 179 - 1999 99.1095-05

Egypt - 5.995 SA 516 70 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

940 26,1 - 404 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Black Oil/Feed Exch. EA-1006 1 14 8.650 32,2 - 246 SA 179 - 1999 99.1095-06

Egypt - 5.995 SA 516 70 - -

839 28 - 335 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria First Cold Vac.Res/Feed Exch. EA-1007 A/B 2 14 8.600 32,2 - 272 SA 179 - 1999 99.1095-07

Egypt - 5.995 SA 516 70 - -

1143 21,5 - 362 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Low Pump./Feed Exch. EA-1008 1 14 15.700 32,2 - 300 SA 179 - 1999 99.1095-08

Egypt - 5.995 SA 516 70 - -

889 21,5 - 390 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria BTM Pump./Feed Exch. EA-1009 1 12 9.200 32,2 - 319 SA 199 T5 - 1999 99.1095-09

Egypt - 5.995 SA 387 5 2 - -

788 28 - 366 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Hot Vac.Res./Feed Exch. EA-1010 A/B 2 13 7.650 32,2 - 332 SA 199 T5 - 1999 99.1095-10

Egypt - 5.995 SA 387 5 2 - -

508 18,2 - 241 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Heavy Waxy Dist./LP Steam EA-1011 1 10 2.950 12,1 - 175 SA 179 - 1999 99.1095-11

Egypt - 5.995 SA 516 70 - -

458 18,9 - 362 SA 387 5 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Extra Heavy Waxy Dist./LP Steam EA-1012 1 10 2.740 12,6 - 175 SA 179 - 1999 99.1095-12

Egypt - 5.995 SA 516 70 - -

458 26,1 - 248 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Black Oil/LP Steam EA-1013 1 10 2.800 17 - 175 SA 179 - 1999 99.1095-13

Egypt - 5.995 SA 516 70 - -

940 28 - 275 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Vacuum Res./LP Steam Gen. EA-1014 1 19 11.200 18,7 - 175 SA 179 - 1999 99.1095-14

Egypt - 5.995 SA 516 70 - -

712 18,9 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Extra Heavy W.D./Temp.Water EA-1015 1 11 4.850 12,7 - 115 SA 179 - 1999 99.1095-15

Egypt - 5.995 SA 516 70 - -

788 16,5 - 168 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Med.Waxy Dist./Temp W.Spare EA-1016 1 12 6.300 11,1 - 115 SA 179 - 1999 99.1095-16

Egypt - 5.995 SA 516 70 - -

788 18,2 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Heavy Waxy Dist./T.W.Exch. EA-1017 1 12 6.300 12,2 - 115 SA 179 - 1999 99.1095-17

Egypt - 5.995 SA 516 70 - -

788 27,1 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Black Oil/Temp.W.Exch. EA-1018 1 15 7.150 17,4 - 115 SA 179 - 1999 99.1095-18

Egypt - 5.995 SA 516 70 - -

839 28 - 178 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Vac.Res./T.W.Exch. EA-1019 A/B 2 17 7.900 18,7 - 115 SA 179 - 1999 99.1095-19

Egypt - 5.995 SA 516 70 - -

331 17,6 - 270 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Spindle Oil/LP Steam Gen. EA-1020 1 10 1.850 11,7 - 170 SA 179 - 1999 99.1095-20

Egypt - 5.995 SA 106 B - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

331 16,5 - 231 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Med.Waxy D./B.F.W.Exch. EA-1021 A/B 2 10 1.410 13,9 - 175 SA 179 - 1999 99.1095-21

Egypt - 5.995 SA 106 B - -

254 10,8 - 140 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Soft W./Steam Gen.Blow.Exch. EA-1022 1 8 850 16,1 - 65 SA 179 - 1999 99.1095-22

Egypt - 5.995 SA 106 B - -

788 18,2 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria MWD/HWD/Temp.W.SP.Exch. EA-1027 1 12 6.300 12,2 - 115 SA 179 - 1999 99.1095-23

Egypt - 5.995 SA 516 70 - -

839 28 - 178 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria B.O. & V.R./Temp.Wat.Exch. EA-1028 A/B 2 17 7.900 18,7 - 115 SA 179 - 1999 99.1095-24

Egypt - 5.995 SA 516 70 - -

940 19,2 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Light Waxy D./Temp.W.Exch. EA-1033 1 14 9.100 12,8 - 115 SA 179 - 1999 99.1095-25

Egypt - 5.995 SA 516 70 - -

508 17,7 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Spindle Oil/Temp.W.Exch. EA-1034 1 10 2.600 11,8 - 115 SA 179 - 1999 99.1095-26

Egypt - 5.995 SA 516 70 - -

940 19,2 - 185 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Spindle Oil/Temp.W.Spare EA-1035 1 14 9.100 12,8 - 115 SA 179 - 1999 99.1095-27

Egypt - 5.995 SA 516 70 - -

331 7,4 - 150 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Seal Oil/Temp.W.Exch. EA-1036 1 10 1.350 11 - 115 SA 179 - 1999 99.1095-28

Egypt - 5.995 SA 106 B - -

661 20,9 - 207 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria VGO & TPA/LP Steam Gen. EA-1037 1 10 4.350 13,9 - 175 SA 179 - 1999 99.1095-29

Egypt - 5.995 SA 516 70 - -

661 19,2 - 292 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Light WA.Dist./LP Steam EA-1038 1 10 4.650 12,8 - 175 SA 179 - 1999 99.1095-30

Egypt - 5.995 SA 516 70 - -

254 14,7 - 135 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Flush.Oil/LP Steam Heater EA-1042 1 8 850 9,8 - 175 SA 179 - 1999 99.1095-31

Egypt - 5.995 SA 106 B - -

585 14,5 - 160 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Stripped Feed/BTM Exch. EA-2001 A/B 2 10 4.000 13,5 - 125 SA 213 Tp 304L - 1999 99.1095-32

Egypt - 5.995 SA 516 70 - -

1194 6,1 - 175 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Stripper Reboiler EA-2002 1 13 11.800 5,2 - 160 SA 213 Tp 304L - 1999 99.1095-33

Egypt - 5.995 SA 516 70 - -

483 14,5 - 100 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Stripp.Water Trim Cooler EA-2003 1 10 2.600 9,8 - 70 SA 179 - 1999 99.1095-34

Egypt - 5.995 SA 516 70 - -

991 87,3 - 390 SA 387 12 2 S.S. Tp 347 w.o. -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria React.Effl./Feed Exch. EA-4001 A 1 47 18.150 74,5 - 480 SA 213 Tp 321 - 1999 99.1095-35

Egypt - 5.995 - - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

991 87,3 - 390 SA 387 12 2 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria React.Effl./Feed Exch. EA-4001 B 1 45 17.600 74,5 - 480 SA 213 Tp 321 - 1999 99.1095-36

Egypt - 5.995 - - -

991 87,3 - 310 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria React.Effl./Feed Exch. EA-4001 C 1 42 18.800 74,5 - 430 SA 213 T12 - 1999 99.1095-37

Egypt - 5.995 - - -

813 71,6 - 200 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Hot HP Sep.W.Trim Cooler EA-4002 1 34 11.460 48,1 - 70 SA 179 - 1999 99.1095-38

Egypt - 5.995 SA 516 70 - -

305 20,3 - 341,6 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Spill Back/Up Compress. EA-4003 1 9 1.200 13,7 - 158 SA 179 - 1999 99.1095-39

Egypt - 5.995 SA 106 B - -

483 8,3 - 200 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Stripper Overhead W.Cond. EA-4005 1 10 2.400 6,9 - 70 SA 179 (min.sil.0.19%) - 1999 99.1095-40

Egypt - 5.995 SA 516 70 - -

762 14,7 - 155 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Gasoil Product Water Trim EA-4006 1 12 5.800 9,8 - 70 SA 179 (min.sil.0.15%) - 1999 99.1095-41

Egypt - 5.995 SA 516 70 - -

585 11,8 - 170 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Deb.Feed/Stripper BTM EA-4007 1 10 3.550 14,7 - 340 SA 179 - 1999 99.1095-42

Egypt - 5.995 SA 516 70 - -

1067 9,8 - -40/90 SA 240 Tp 304L - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Deb.Overhead Condenser EA-4008 1 8 9.000 7 - 70 SA 334 1 - 1999 99.1095-43

Egypt - 5.995 SA 516 70 - -

788 12,5 - 220 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Debutanizer Reboiler EA-4009 1 12 5.700 18,6 - 294 SA 179 - 1999 99.1095-44

Egypt - 5.995 SA 516 70 - -

458 14,7 - 94 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Naphta Prod.Wat.Trim EA-4010 1 10 2.250 9,8 - 70 SA 179 - 1999 99.1095-45

Egypt - 5.995 SA 516 70 - -

331 10,7 - 175 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Continuos Blowd. Cooler EA-1351 A/B 2 10 1.000 16,2 - 100 SA 213 Tp 304 - 1999 99.1095-46

Egypt - 3.000 SA 312 Tp 304 - -

331 5,1 - 125 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria LP Flash Drum Vent Cond. EA-1451 1 10 950 16,2 - 100 SA 213 Tp 304 - 1999 99.1095-47

Egypt - 3.000 SA 240 Tp 304 - -

331 5,1 - 125 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria HP Flash Drum EA-1452 1 10 950 16,2 - 100 SA 213 Tp 304 - 1999 99.1095-48

Egypt - 3.000 SA 240 Tp 304 - -

458 13,7 - 125 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Rejected Cond.Cooler EA-1453 1 10 2.600 9,3 - 70 SA 179 - 1999 99.1095-49

Egypt - 5.995 SA 516 70 - -

254 7,4 - 194 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria SRGO Flushing Heater EA-4011 1 8 850 6,1 - 347 SA 179 - 1999 99.1095-50

Egypt - 5.995 SA 106 B - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

508 5,9 - 160 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Lean/Rich Dea Exch. EA-6001 A/B 2 10 6.100 8,8 - 130 SA 213 Tp 304 - 1999 99.1095-51

Egypt - 5.995 SA 516 70 - -

1220 6,1 - 160 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Amine Reg.Reboiler EA-6002 - 13 9.850 6,1 - 175 SA 213 Tp 304L - 1999 99.1095-52

Egypt - 5.995 SA 516 70 - -

508 58,8 - 70 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Trim Cooler TP Rec. EA-6004 1 21 6.150 87,3 - 100 SA 179 - 1999 99.1095-53

Egypt - 5.995 SA 516 70 - -

305 16,7 - 70 SA 106 B - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Lean Dea Cooler EA-6005 1 9 1.200 25 - 130 SA 179 - 1999 99.1095-54

Egypt - 5.995 SA 516 70 - -

585 8,8 - 175 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Moduslops Cooler EA-4013 1 10 3.300 6,9 - 70 SA 179 (min.sil.0.15%) - 1999 99.1095-55

Egypt - 5.995 SA 516 70 - -

381 38 - 170 SA 516 70 - -

TECNICAS REUNIDAS Tecnicas Reunidas - Alexandria Make Upcompr./Interstage Cooler EA-4004 1 10 2.150 25,5 - 70 SA 179 (min.sil.0.15%) - 1999 99.1095-56

Egypt - 5.995 SA 516 70 - -

1474 157,3 - 369 SA 387 22 1 S.S. Tp 347 w.o. -

SKEC ABB Hydrocracking Madero React.Feed/React.Effl. 030-U-502-E-03 A/B 2 131 88.000 143,9 - 437 SA 213 Tp 347 - 1999 99.1097-01

Mexico - 4.877 SA 387 22 1 S.S. Tp 347 w.o. -

1372 142,9 - 365 SA 387 11 2 W.O. -

SKEC ABB Hydrocracking Madero Feed Oil/React.Effl.Exch. 030-U-502-E-04 A/B2 89 122.000 157 - 276 SA 213 T9 - 1999 99.1097-02

Mexico - 7.316 SA 182 F9 - -

813 156,4 - 277 SA 516 70 - -

SKEC ABB Hydrocracking Madero Recycle Gas/Hot HP Vapor 030-U-502-E-05 A/B2 62 44.000 141,5 - 305 SA 213 T5 - 1999 99.1097-03

Mexico - 4.877 SA336F5 - -

1067 7,3 - 75 SB 424 N08825 - -

SKEC ABB Hydrocracking Madero Hot HP Vapor Trim 030-U-502-E-07 1 8 10.500 140 - 170 SB 163 N08825 - 1999 99.1097-04

Mexico - 3.660 SB 425 N08825 - -

940 155,6 - 371 SA 387 22 1 S.S. Tp 347 w.o. -

PEMEX Samsung Hydrotreating Tulo React.Feed/React.Effluent Exchanger 2 73 29.000 143,9 - 436 SA 213 Tp 347 - 2000 00.1100-01

Mexico - 5.310 SA 336 F22 1 S.S. Tp 347 w.o. -

991 142,9 - 375 SA 387 11 2 S.S. Tp 347 w.o. -

PEMEX Samsung Hydrotreating Tulo Feed Oil/React.Effluent Exchanger 2 55 23.800 160 - 300 SA 213 T9 - 2000 00.1100-02

Mexico - 4.877 SA 336 F9 - -

610 156,4 - 277 SA 516 70 - -

PEMEX Samsung Hydrotreating Tulo Recycle Gas/Hot HP Vapor Exchanger 2 42 18.200 141,5 - 305 SA 213 T5 - 2000 00.1100-03

Mexico - 3.660 SA336F5 - -

712 13,7 - 49 SA 516 70 - -

PEMEX Samsung Hydrotreating Tulo Hot HP Vapor Trim Exchanger 1 13 6.100 139,5 - 170 SB 163 N08825 - 2000 00.1100-04

Mexico - 2.440 SB 425 N08825 - -

4293 3 FV 343 P355 NH - -

BASF Raytheon EB\SM Plant Ludwigshafen Feed Vaporizer Preheater W2311 1 17 210.000 2 FV 343 St35.8 - 2000 00.1101-01

Germany - 10.897 P355 NH - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4293 3 FV 649 X6 Cr Ni 18 11 - -

BASF Raytheon EB\SM Plant Ludwigshafen Feed Effluent Exchanger W2312 1 25 150.000 2 FV 649 X6 Cr Ni 18 11 - 2000 00.1101-02

Germany - 8.992 X6 Cr Ni 18 11 - -

4191 55 - 300 P355 NH - -

BASF Raytheon EB\SM Plant Ludwigshafen HP Steam Generator W2313 1 101 110.000 2 FV 649 St35.8 - 2000 00.1101-03

Germany - 4.547 X6 Cr Ni 18 11\Inconel600- -

3048 2 - 838 X10 Ni Cr Al Ti 32 20H\X3 Cr Ni Mo N 17 13- -

BASF Raytheon EB\SM Plant Ludwigshafen Reactor Reheater W2211 1 81\52 120.000 1 - 590 X3 Cr Ni Mo N 17 13 - 2000 00.1103-01

Germany - 7.925 X6 Cr Ni 18 11 - -

1448 10,67 - 250 SA 516 60 - -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul First Reactor Feed Preheater Exchanger 1 - 32.000 97,12 - 175 SA 179 - 2001 01.1115-01

Brazil Breech Lock Type 6.096 SA 266 4 - -

1372 95,94 - 245 SA 387 11 2 S.S. Tp 347 w.o. -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Second Reactor Feed Preheater Exchanger 1 - 41.000 78,3 - 300 SA 213 Tp 347 - 2001 01.1115-02

Brazil Breech Lock Type 6.096 SA 387 11 2 - -

1372 95,26 - 302 SA 387 11 2 S.S. Tp 347 w.o. -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Reactor Feed Effluent Exchanger 1 - 41.000 79,09 - 361 SA 213 Tp 347 - 2001 01.1115-03

Brazil Breech Lock Type 6.096 SA 336 F11 - -

1372 94,37 - 369 SA 387 11 2 S.S. Tp 347 w.o. -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Reactor Feed Effluent Exchanger 1 - 43.000 79,97 - 412 SA 213 Tp 347 - 2001 01.1115-04

Brazil Breech Lock Type 6.096 SA 336 F11 S.S. Tp 347 w.o. -

1372 93,39 - 418 SA 387 11 2 S.S. Tp 347 w.o. -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Reactor Feed Effluent Exchanger 1 - 43.000 81 - 435 SA 213 Tp 347 - 2001 01.1115-05

Brazil Breech Lock Type 6.096 SA 336 F11 S.S. Tp 347 w.o. -

1372 5,88 - 60 SA 516 60 - -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Reactor Feed Final Cooler 2 - 18.000 77,69 - 170 SA 179 - 2001 01.1115-06

Brazil Breech Lock Type 6.096 SA 266 4 - -

1994 - - 85 A 516 60+S5 - -

NIOC (TECTUBI) Petropars/Daelim/MSA/IdroOil-Gas South Pars - Iran Gas/Gas Exchanger 6 83 106.000 78 - - A 334 6 - 2001 01.1116

Iran - 9.144 A 516 60+S5 - -

889 148,9 - 454,5 SA 387 22 2 S.S. Tp 347 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta Reactor N° 1 Effluent Hot Rec. Gas Exch. 1 57+4wo 26.300 163,1 - 426,7 SA 249 Tp 321 - 2001 01.1119-01

Canada Breech Lock Type 6.096 SA 336 F22 3 S.S. Tp 347 -

1347 148,2 - 435 SA 387 22 2 S.S. Tp 347 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta Reactor N° 1 Effluent Gas Oil Feed Exch. 4 83+4wo 54.000 160 - 407 SA 249 Tp 321 - 2001 01.1119-02

Canada Breech Lock Type 6.096 SA 336 F22 3 S.S. Tp 347 -

915 147,2 - 399 SA 387 22 2 S.S. Tp 347 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta Reactor N° 1 Effluent Medium Rec. Gas Exch.1 54+4wo 26.500 164,1 - 321 SA 249 Tp 321 - 2001 01.1119-03

Canada Breech Lock Type 6.096 SA 336 F11 3 - -

1245 112,7 - 315,5 SA 387 11 2 - -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta HHPS Vapor Stripper Feed Exch. 2 55 41.400 146,5 - 371 SA 268 Tp 405 - 2001 01.1119-04

Canada Breech Lock Type 4.268 SA 336 F22 3+W.O. S.S. Tp 347 -

1016 146,5 - 302 SA 387 11 2 INCONEL 625 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta HHPS Vapor Recycle Gas Exch. 2 57+6.4wo 34.100 190 - 265,5 SB 704 N06625 - 2001 01.1119-05








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118 112,7 - 235 SA 516 70 - -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta HHPPS Vapor Trim Condenser 2 51 39.000 146,5 - 274 SA 789 S31803 - 2001 01.1119-06

Canada Breech Lock Type 6.096 SA 266 2 - -

1524 122 - 345 BS 1501-224.490B - -

I F I ABB Fertilizer Cork Methanator Eff. BFW Heater 1 31 72.200 29 - 450/250 BS.3606-621-420 - 2002 02.1127

Ireland - 10.540 - - -

1016 206,8 - 447 SA 336 F22 V S.S. Tp 347 -

K.N.P.C. KNPC/Dan Trading Refinery Shuaiba R.H. Reactor Overhead H2 Feed Exchanger 4 82 34.000 206,8 - 361 SA 213 Tp 321 - 2002 02.1129-01

Kuwait Breech Lock Type 6.096 SA 336 F22 V - -

864 7,58 - 290 SA 336 F22 V S.S. Tp 347 -

K.N.P.C. KNPC/Dan Trading Refinery Shuaiba Reactor Effluent Raw Light Diesel H.E. 1 12 14.460 159,2 - 334 SA 213 Tp 321 - 2002 02.1129-02


1347 77,4 - 437 SA 387 11 2 TP 347 -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Hot Recycle Gas Exchanger 1 38+4.5wo 38.700 93,2 - 408 SA 213 Tp 321 - 2002 02.1137-01

Turkey Breech Lock Type 6.096 SA 387 11 2 - -

1347 77,4 - 390 SA 387 11 2 - -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Hot Feed Exchanger 4 38+4.5wo 48.200 141,2 - 376 SA 213 Tp 304 - 2002 02.1137-02


1235 73,5 - 297 SA 387 11 2 - -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Cold Feed Exchanger 4 36 35.700 141,2 - 297 SA 268 Tp 410 - 2002 02.1137-03


1372 72,6 - 297 - - -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Cold Recycle Gas Exchanger1 39 38.300 93 - 246 SA 199 T11 - 2002 02.1137-04

Turkey Breech Lock Type 6.096 - - -

840 118 FV 358 SA 387 11 2 S.S. Tp 347 -

NATREF Fluor / Sasol Refinery Sasolburg Feed Effluent Exchanger ( Hot service ) 1 40/50+4.5wo 19.200 91 FV 405 SA 213 Tp 321 - 2004 04.1156-01

South Africa, Rep. of - 7.200 SA 387 11 2 S.S. Tp 347 -

840 118 FV 314 SA 387 11 2 S.S. Tp 347 -

NATREF Fluor / Sasol Refinery Sasolburg Feed Effluent Exchanger ( Cold service ) 1 40/50+4.5wo 19.200 91 FV 361 SA 213 Tp 321 - 2004 04.1156-02


705 95 FV 391 SA 387 11 2 S.S. Tp 347 -

NATREF Fluor / Sasol Refinery Sasolburg Recycle Gas vs Reactor Effluent Exchanger 1 27+4.5wo 7.300 88 FV 361 SA 213 Tp 321 - 2004 04.1156-03


470 77 FV 280 SA 387 11 2 - -

NATREF Fluor / Sasol Refinery Sasolburg HHPS Vapour / Recycle Gas Exchanger 1 20 3.200 97 FV 184 SA 213 T11 - 2004 04.1156-04

South Africa, Rep. of - 4.877 SA 516 70 - -

710 92 FV 305 SA 516 70 - -

NATREF Fluor / Sasol Refinery Sasolburg Feed / Stripper Bottoms Exchanger 1 31 11.700 120 FV 165 SA 179 - 2004 04.1156-05

South Africa, Rep. of - 6.096 SA 516 70 - -

4978 2,45 FV 610 SA 240 Tp 304H - -

FCFC Stone & Webster EB\SM Plant Yunlin Feed Effluent Exchanger E-202 1 25 235.000 1,76 FV 649 SA 213 Tp 304H - 2004 04.1159-01

Taiwan - 9.831 SA 240 Tp 304H - -

4826 46 FV 285 SA 516 70 - -

FCFC Stone & Webster EB\SM Plant Yunlin HP Steam WHB E-203 1 100 145.000 1,76 FV 433 SA 213 T22 - 2004 04.1159-02

Taiwan - 2.540 SA 516 70/Inconel600 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4900 2,45 FV 350 SA 516 70 - -

FCFC Stone & Webster EB\SM Plant Yunlin Feed Vaporizer E-201 1 16 365.000 1,76 FV 350 SA 179 - 2004 04.1159-03

Taiwan - 11.446 SA 516 70 - -

1150 228,5 - 410 SA 336 M F22 3 S.S. Tp 309L -

FPCC HEC Refinery Mailiao Feed Reactor Effluent Exchanger 6 112 55.678 211,8 - 455 SA 213 M TP347 S.S. Tp 347 2005 05.1168-01

Taiwan Breech Lock Type 6.100 SA 336 M F22 3 - -

899 139,2 - 265 SA 516 M 485 S.S. Tp 304L -

FPCC HEC Refinery Mailiao HTS Overhead/LTS Bottom Exchanger 1 55 29.417 208,9 - 325 SB 423 M08825 - 2005 05.1168-02


899 234,3 - 215 SA 266 M Gr 2 S.S. Tp 304L -

FPCC HEC Refinery Mailiao HTS Overhead/Treat Gas Exchangerr 1 89 30.597 205,9 - 240 SA 789 M S31803 - 2005 05.1168-03

Taiwan Breech Lock Type 6.100 SA336 M F11 CL 3 - -

800 229,5 - 395 SA 336 M F22 3 S.S. Tp 309L -

FPCC HEC Refinery Mailiao Feed/HDW Reactor Effluent Exchanger 4 78 21.725 215,7 - 415 SA 213 M TP347 - 2005 05.1168-04


500 242,2 - 240 SA 336 M F11 3 - -

FPCC HEC Refinery Mailiao HTS Overhead/Treat Gas Exchangerr 1 50 11.700 209,9 - 280 SA 213 M Gr - 2005 05.1168-05


595 138,3 - 95 SA 516 M 485 - -

FPCC HEC Refinery Mailiao HTS Ttrim Cooler Exchanger 1 50 23.700 206,9 - 182 SA 179 M - 2005 05.1168-06

Taiwan Breech Lock Type 6.100 SA 266 M 2 - -

1143 202 - 482 SA 336 M F22V S.S. Tp 347 -

SHENUA GROUP CORP. SEI Coal Liquefaction Inmer Membrane/Make up Hydrogen Feed Effluent 2 91 54.000 223 - 450 SA 213 M Tp321 - 2005 05.1175-01

Mongolia - 6.096 SA 336 M F22V - -

1143 201 - 370 SA 336 M F22 3 S.S. Tp 347 -

SHENUA GROUP CORP. SEI Coal Liquefaction Inmer T-Start/Effluent 1 88 60.000 180 - 350 SA 213 M Tp321 - 2005 05.1175-02

Mongolia - 6.096 SA 336 M F22 3 - -

1601 176 - 454 SA 336 F22 3 S.S. Tp 347 -

MOTIVA BECHTEL / JACOBS Refinery Port Arthur B.L. Type Heat Exchangers 2 121 + 4 82.300 191 - 399 SA 213 TP347 - 2007 07.1186-01

USA Breech Lock Type 5.029 SA 336 F22 3 S.S. Tp 347 -

1372 175 - 457 SA 336 F22 3 S.S. Tp 347 -

MOTIVA BECHTEL / JACOBS Refinery Port Arthur Bolted in Heat Exchangers 4 104+4.8 71.200 190 - 399 SA 213 TP347 - 2007 07.1186-02

USA - 5.944 SA 336 F22 3 S.S. Tp 347 -

1524 174 - 427 SA 336 F22 3 S.S. Tp 347 -

MOTIVA BECHTEL / JACOBS Refinery Port Arthur B.L. Type Heat Exchangers 3 110+4 76.600 191 - 371 SA 213 TP347 - 2007 07.1186-03

USA Breech Lock Type 5.334 SA 336 F22 3 S.S. Tp 347 -

4220 203 - 426 SA 336 F22 V S.S. Tp 347 -

LUKOIL Technip Refinery Bourgas HP Heat Exchangers 2 98 92.000 254 - 354 SA 213 Tp 317 - 2010 10.1196-03

Bulgaria - 7.315 SA 336 F22 S.S. Tp 317 -

810 179 - 154 SA 336 F22 V S.S. Tp 347 -

LUKOIL Technip Refinery Bourgas HP Heat Exchanger 1 61 35.000 203 - 426 SA 213 M Tp321 - 2010 10.1196-04

Bulgaria - 6.096 SA 336 F22 S.S. Tp 347 -

1325 139 - 410 SA 965M F347 - -

PETROBRAS PETROBRAS Refining Rio de Janeiro B.L. Type Heat Exchangers 12 78,5 46.000 126 - 430 SA 213 M 347 - 2010 10.1200-01

Brazil - 5.486 SA 387MGr22CL2 S.S. Tp347 -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1236 139 - 410 SA 965M F347 - -

PETROBRAS PETROBRAS Refining Rio de Janeiro B.L. Type Heat Exchangers 4 69,5 28.300 127 - 430 SA 213 M 347 - 2010 10.1200-02

Brazil - 2.438 SA 387MGr22CL2 S.S. Tp347 -

1047 205 - 343 SA336 Gr F22 - -

YOOBASE SKEC Refining Ulsan B.L. Type Heat Exchangers 2 80 36.500 184 - 298 SA213 T22 - 2011 11.1202-01

Korea - 6.100 SA 336 F22 - -

1310 204 - 400 SA 965 Y Gr 321 - -

YOOBASE SKEC Refining Ulsan B.L. Type Heat Exchangers 4 103 51.800 191 - 467 SA 213 TP 329 SS Tp 347 2011 11.1202-02

Korea - 6.100 SA 387 Gr 22 CL - -

550 205 - 343 SA 336 Gr F22 - -

YOOBASE SKEC Refining Ulsan B.L. Type Heat Exchangers 1 46 11.500 183 - 183 SA 213 TF22 - 2011 11.1202-03

Korea - 6.100 SA 336 F22 - -

1250 202,5 - 454 SA 336 F22 CL3 SS Tp 347 -

SK LUBRICANTS SKEC Refining Ulsan B.L. Type Heat Exchangers 2 114 71.500 225,2 - 374 SA 213 Tp. 321 - 2011 11.1205-01

Korea - 6.100 SA 336 F22 CL3 SS Tp 3447 -

1500 49,3 - 420 SA 516 Gr 485 - -

SK LUBRICANTS SKEC Refining Ulsan HP Steam Generator 1 47 35.700 200,9 - 420 SB 163 NO8825 - 2011 11.1205-02

Korea Breech Lock Type 4.880 SA 336 F22 Cl3 Inconel 625 -

580 231 - 217 SA 336 F22 CL3 - -

SK LUBRICANTS SKEC Refining Ulsan B.L. Type Heat Exchangers 1 55 2.840 199,6 - 298 SB 163 UNS NO8825 - 2011 11.1205-03

Korea - 4.880 SA 336 F22 CL3 Alloy 625 -

1500 6,3 - 200 SA 516 Gr 485 - -

SK LUBRICANTS SKEC Refining Ulsan LP Steam Generator 1 20 26.800 199 - 270 SB 163 NO8825 - 2011 11.1205-04


1350 79 - 390 SA387Gr11CL2 SS Tp 347 -

TUPRAS LG Eng. Constr. Co. Refining Izmir Pill Breech Reactor Effluent Hot Feed Exchangers4 38 48.200 144 - 376 SA213 TP 304 - 2012 12.1208

Turkey - 6.096 SA336 F22 CL3 SS Tp 3447 -

1350 161,4 - 454 SA 336 GR.F22 CL.3 S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Reactor Effluent/Recycle Gas Hot Exchanger 1 78+4 62.100 179 - 454 SA 213 Tp 321 - 2012 12.1210.E01

Russia - 6.000 SA 336 GR.F22 CL.3 S.S. Tp 347 -

1440 160,9 - 454 SA 336 GR.F22 CL.3 S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Reactor Effluent/Feed Hot Exchanger 2 83+4 81.000 210,8 - 435 SA 213 Tp 321 S.S. Tp 347 2012 12.1210.E02


1550 160,4 - 435 SA 336 GR.F22 CL.3 S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Reactor Effluent/Recycle Gas Cold Exchanger1 85+4 80.550 180 - 430 SA 213 Tp 321 - 2012 12.1210.E03


1550 160 - 430 SA 336 GR.F22 CL.3 S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Reactor Effluent/Feed Medium Exchanger 2 84+4 96.200 210,8 - 430 SA 213 Tp 321 S.S. Tp 347 2012 12.1210.E04


1300 120,6 - 365 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Reactor Effluent/Stripper Bottoms Exchanger2 70 60.900 159,7 - 445 SA 213 Tp 321 S.S. Tp 347 2012 12.1210.E05


1325 158,9 - 420 SA 336 GR.F22 CL.3 S.S. Tp 347 -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Reactor Effluent/Feed Cold Exchanger 2 71+4 75.650 210,8 - 420 SA 213 Tp 321 S.S. Tp 347 2012 12.1210.E06








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1300 158 - 420 SA 336 GR.F22 CL.3 - -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Hot Separator Vapor/Recycle Gas Hot Exchanger1 74 57.600 180,9 - 405 SA 213 Tp 321 - 2012 12.1210.E07

Russia - 7.400 SA 336 GR.F22 CL.3 - -

1275 157,5 - 415 SA 336 GR.F22 CL.3 - -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Hot Separator Vapor/Feed Exchanger 2 70 63.900 210,8 - 415 SA 213 T22 - 2012 12.1210.E08

Russia - 8.000 SA 336 GR.F22 CL.3 - -

1350 117,7 - 300 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Hot Separator Vapor/Stripper Feed Hot Exchanger1 65 56.900 157 - 385 SA 213 T22 - 2012 12.1210.E09

Russia - 6.000 SA 336 GR.F22 CL.3 - -

1250 156,2 - 395 SA 336 GR.F22 CL.3 - -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Hot Separator Vapor/Recycle Gas Cold Exchanger2 68 43.500 181,9 - 355 SA 213 T22 - 2012 12.1210.E10

Russia - 6.100 SA 336 GR.F22 CL.3 - -

1300 115,7 - 300 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrocracking Volgograd Hot Separator Vapor/Stripper Feed Cold Exchanger1 64 50.600 155,5 - 310 SA 213 T22 - 2012 12.1210.E11

Russia - 6.000 SA 336 GR.F22 CL.3 - -

710 52,48 - 260 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Feed Preheater/Vaporizer 2 - 6.600 48,56 - 290 SA 179 - 2013 13.1210.G01

Russia - 5.300 SA 516 GR.70 - -

740 48,56 - 490 SA 387 GR.11 CL.2 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Feed Preheater 1 - 13.300 52,48 - 410 SA 213 T11 - 2013 13.1210.G02

Russia - 10.500 SA 387 GR.11 CL.2 - -

900 40,71 - 320 SA 387 GR.11 CL.2 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd 1st BFW Preheater 2 - 9.000 52 - 250 SA 213 T11 - 2013 13.1210.G03

Russia - 3.800 SA 516 GR.70 - -

800 40,71 - 360 SA 387 GR.11 CL.2 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd 2nd BFW Preheater 1 - 6.450 51,99 - 250 SA 213 T11 - 2013 13.1210.G04

Russia - 3.000 SA 516 GR.70 - -

1380 40,71 - 300 SA 516 GR.70 S.S. Tp 304 -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd 3rd BFW Preheater 2 - 25.000 51,99 - 200 SA 213 Tp.304L - 2013 13.1210.G05

Russia - 5.400 SA 516 GR.70 - -

870 40,71 - 120 SA 240 304L - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Process Gas Water Cooler 1 - 9.500 6,87 - 120 SA 213 Tp.304L - 2013 13.1210.G06

Russia - 6.200 SA 516 GR.70 - -

720 9,81 - 260 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Reformer/Shift Section Start-Up Cooler 1 - 5.900 6,87 - 120 SA 179 - 2013 13.1210.G07

Russia - 7.000 SA 516 GR.70 - -

720 9,81 - 260 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Reformer/Shift Section Start-Up Heater 1 - 3.700 48,56 - 295 SA 179 - 2013 13.1210.G08

Russia - 3.800 SA 516 GR.70 - -

260 3,43 - 150 SA 516 GR.70 - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Boiler Blowdown Cooler 1 - 400 6,87 - 120 SA 179 - 2013 13.1210.G09

Russia - 1.900 SA 516 GR.70 - -

330 50,52 - 285 SA 240 304L - -

LUKOIL TECNICAS REUNIDAS Hydrogen ProductionVolgograd Process Condensate Feed/Effluent Exchanger 2 - 1.600 50,52 - 255 SA 213 Tp.304L - 2013 13.1210.G10

Russia - 5.000 SA 240 304L - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1270 176,8 - 454 SA 336 GR.F22 CL.3 SS Tp 347 -

LUBEREF SAMSUNG Refinery Yanbu HCR Feed /Effluent Exchanger B.L. type 2 82+8,5 51.000 194,5 - 431 SA 213 Tp 321 - 2013 13.1214.01

Saudi Arabia, Kingdom of Breech Lock Type 4.877 SA 336 GR.F22 CL.3 SS Tp 347 -

686 197,8 - 288 SA 336 GR.F22 CL.3 - -

LUBEREF SAMSUNG Refinery Yanbu HCR HHPS Vapor/Recycle Gas Exchanger B.L. type2 47 12.000 169,4 - 316 SA 213 Tp 321 - 2013 13.1214.02


686 197,8 - 288 SA 336 GR.F22 CL.3 SS Tp 347 -

LUBEREF SAMSUNG Refinery Yanbu HCR HHPS Vapor/Recycle Gas Exchanger B.L. type1 57 12.350 169,4 - 316 SB 444 Gr 1 N066 25 - 2013 13.1214.03


711 173,1 - 431 SA 336 GR.F22 CL.3 SS Tp 347 -

LUBEREF SAMSUNG Refinery Yanbu HCR Reactor Effluent Exchanger/Frac. Feed Exchanger Pill Breech type2 52+8,5 22.200 133,2 - 343 SB 444 Gr 1 N066 25 - 2013 13.1214.04


711 170,8 - 360 SA 336 GR.F22 CL.3 SS Tp 347 -

LUBEREF SAMSUNG Refinery Yanbu Second HCR Feed/Effluent Exchanger B.L. type2 41+8,5 15.000 197,1 - 300 SA 213 Tp 321 - 2013 13.1214.05


767 190,7 - 292 SA 336 GR.F22 CL.3 - -

LUBEREF SAMSUNG Refinery Yanbu DW Feed/HDF Efleuent Exchanger B.L. Type 2 50 18.800 166,7 - 343 SA 213 Gr T 22 - 2013 13.1214.06

Saudi Arabia, Kingdom of Breech Lock Type 6.096 SA 336 GR.F22 CL.3 - -

838 187,4 - 400 SA 336 GR.F22 CL.3 SS Tp 347 -

LUBEREF SAMSUNG Refinery Yanbu DW Feed/DW Effluent Exchanger B.L.Type 2 54+8,5 22.100 173,1 - 428 SA 213 Tp 321 - 2013 13.1214.07


482 165,1 - 343 SA 336 GR.F22 CL.3 - -

LUBEREF SAMSUNG Refinery Yanbu DW HHPS Vapor/Recycle Gas Exchanger Pill Breech type2 30 7.400 190 - 260 SA 213 Gr T 22 - 2013 13.1214.08

Saudi Arabia, Kingdom of Breech Lock Type 5.735 SA 336 GR.F22 CL.3 - -

1500 176 - 454 SA 336 GR.F22 CL.3 SS Tp 347 -

TOTAL TECNICAS REUNIDAS Refinery Optara Breech Lock type Heat Exchangers 2 96+5 83.900 205 - 400 SA 213 Tp 321 - 2013 13.1215

Belgium - 6.096 SA 336 GR.F22 CL.3 SS Tp 347 -

1301 2,757 - 204,4 SA 516 GR.70 - -

KNPC KNPC Refinery Mina Abdulla Pill Breech H.E. First Stage Effleunt/H2S Stripper Feed1 18 55.500 16,89 - 287,8 SB 444 Gr 1 N066 25 INCONEL 625 2014 14.1219

Kuwait - 7.620 SA 266 GR 2 INCONEL 625 -

1600 235 - 355 SA 336 GR F11 CL 3 - -

OCI NITROGEN KBR Hydrogen ProductionGELEEN Ammonia Feed Effluent Hexchanger 1 133 251.742 235 - 350 SA 213 GR T 11 - 2014 14.1220

Netherlands - 19.047 SA 336 GR F11 CL 3 - -

1372 201,3 - 254 SA 387 Gr 22 Cl 2 - -

MOTIVA JACOBS Refinery Port Arthur First stage HHPS / Recycle gas exchanger 2 90 80.400 170,6 - 299 SB 163 N08825 - 2015 14.1225.01

TEXAS Breech Lock Type 7.316 SA 336 GR.F22 CL.3 Inconel 625 -

1600 190,9 - 399 SA 387 Gr 22 Cl 2 SS Tp 347 -

MOTIVA JACOBS Refinery Port Arthur Second stage Reactor feed / effluent exchanger3 103+5 110.800 176,1 - 450 SA 213 TB 347 - 2015 14.1225.02

TEXAS Breech Lock Type 7.316 SA 336 Gr F22 CL 3 SS Tp 347 -

2260 37,9 - 315,55 SA 516 GR 70 - -

MOTIVA JACOBS Refinery Port Arthur First stage effluent MP steam generators 2 38 68.000 172,3 - 329,44 SB 163 UNS NO8825 - 2015 14.1225.03

TEXAS Kettle 6.858 SA 336 Gr F22 CL 3 SS Tp 347 -

1371 48,6 - 273,8 SA 516 GR 70 - -

MOTIVA JACOBS Refinery Port Arthur Second stage HHPS Vapor / CLPS liquid exchanger2 33 54.200 170,9 - 293,3 SB 163 UNS NO8825 - 2015 14.1225.04

TEXAS - 7.315 SA 336 Gr F22 Cl 3 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

- 174,1 - 426,7 - - -

MOTIVA JACOBS Refinery Port Arthur DHT Reactor Feed/Effluent Exchanger/Bundles only3 - 18.256 191 - 371 SA 213 TP 347 - 2015 15.1229

TEXAS Breech Lock Type/Bundle only 5.334 - - -





ProcessLicensors:

Chevron, UOP, ExxonMobil, Axens, KBR, Shell

1.25Cr-0.5Mo2.25Cr-1Mo Standard2.25Cr-1Mo-0.25V Modified12CrMo9-10

Materials:

MaximumDimensions:

Tubes length: > 10.000 mmShell Diameter: 1.600 mm


Units: > 200 units built since 1980

Design: Breech Lock ( proprietary design)Bolted In, Combined Breech Lock-Bolted In

HIGH PRESSURE HEAT EXCHANGERS (BREECH LOCK CLOSURE)

REFERENCE LIST - BREECH LOCK HEAT EXCHANGERS SHEET: 1 of 8


DESIGN CONDITIONS

USER ENGINEER/Licensor PLANT TYPE LOCATION DESCRIPTION No. SIZE WEIGHT PRESS. TEMP. MATERIALS CLADDING YEAR JOB No.

[mm] [Kg.] [Bar] [°C]

1220 65 FV 340 ½ Mo S.S.Tp321

SHELL Shell Hydrocracking Stanlow Reactor Charge/React Eff. Exch. 4 - 25.000 55 FV 425 SA213Tp321 1971 71.1065

U.K. Breech Lock type 6096 ½ Mo S.S.Tp321

966 21 - 277 C.S. - -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Eff./Stripper Feed 1 - 21.500 156 - 321 SA209T1 - 1980 80.1600-03

Mississippi, U.S. Breech Lock Type 6.096 ½ Mo - -

966 21 - 277 C.S. - -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Eff./Stripper Feed 1 - 21.500 156 - 321 SA179 - 1980 80.1600-04

Mississippi, U.S. Breech Lock Type 6.096 C.S. - -

966 176 FV 454 2¼ Cr 1 Mo S.S.Tp347 w.o. 1 layer -

CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Reactor Feed Effluent 12 - 44.000 199 FV 440 SA213Tp321 - 1980 80.1600-05

Mississippi, U.S. Breech Lock Type 7.316 2¼ Cr 1 Mo S.S.Tp347 w.o. 1 layer -


CHEVRON Ralph M. Parsons Hydrocracking Pascagoula Hot HPS Vapor/Recycle Gas 6 - 46.700 173 FV 440 SA213Tp321 - 1980 80.1600-06

Mississippi, U.S. Breech Lock Type 6.096 2¼ Cr 1 Mo S.S.Tp347 w.o. 1 layer -


CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent 2 - 27.000 223 FV 405 SA213Tp321 - 1981 81.1655-01

California, U.S. Breech Lock Type 7.316 2¼ Cr 1 Mo S.S.Tp347 w.o. 1 layer -

737 21 - 318 C.S. S.S.Tp410 w.o. 1 layer -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Atm.Col.Feed (HOT) 1 - 16.000 204 FV 335 SA213Tp321 - 1981 81.1655-02


737 21 - 318 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Atm.Col.Feed (COLD) 1 - 15.000 204 FV 335 SB163 (Incoloy 800) - 1981 81.1655-03

California, U.S. Breech Lock Type 7.316 1¼ Cr ½ Mo S.S.Tp347 w.o. 1 layer -

610 225 FV 193 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Recycle Gas 1 - 16.000 202 FV 210 SA179 - 1981 81.1655-04


686 21 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Atm.Col.Circ.Reflux/Recycle Gas 1 - 14.500 224 FV 245 SA213Tp321 - 1981 81.1655-05



CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (HOT) 1 - 30.000 227 FV 293 SA213Tp321 - 1981 81.1655-06


712 200 FV 385 ½ Mo - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (COLD) 1 - 26.000 227 FV 293 SA209T1 - 1981 81.1655-07



CHEVRON Bechtel Hydrocracking Richmond Inter.Reactor Quench Exch. 2 - 36.000 225 FV 430 SA213Tp321 - 1981 81.1655-08


762 38 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Eff./Atm.Col. Feed Exch. 1 - 16.000 200 FV 180 SA179 - 1981 81.1655-09



CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (COLD) 1 - 63.000 224 FV 404 SA213Tp321 - 1981 81.1655-10



CHEVRON Bechtel Hydrocracking Richmond Reactor Feed Effluent (HOT) 1 - 66.000 224 FV 404 SA213Tp321 - 1981 81.1655-11





List of Reference list BREECH LOCK.xls



DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

712 21 - 343 C.S. S.S.Tp347 w.o. 1 layer -

CHEVRON Bechtel Hydrocracking Richmond Inter. Reactor Quench 1 - 11.000 211 FV 454 SA213Tp321 - 1981 81.1655-12


991 38 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond RX Eff./Atm. Col. Feed (HOT) 1 - 31.000 198 FV 274 SA209T1 - 1981 81.1655-13

California, U.S. Breech Lock Type 7.316 ½ Mo S.S.Tp347 w.o. 1 layer -

991 38 - 260 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond RX Eff./Atm. Col. Feed (COLD) 1 - 30.000 198 FV 274 SA179 - 1981 81.1655-14


508 200 FV 233 ½ Mo - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Cold Feed/Eff. Exch.(HOT) 1 - 16.000 214 FV 165 SA209T1 - 1981 81.1655-15


508 200 FV 233 C.S. - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Cold Feed/Eff.Exch.(COLD) 1 - 16.000 214 FV 165 SA179 - 1981 81.1655-16



CHEVRON Bechtel Hydrocracking Richmond Reactor Hot Feed/Eff.Exch.(HOT) 1 - 19.000 214 FV 326 SA213Tp321 - 1981 81.1655-17


534 201 FV 385 2¼ Cr 1 Mo - -

CHEVRON Bechtel Hydrocracking Richmond Reactor Hot Feed/Eff.Exch.(COLD) 1 - 19.000 214 FV 326 SA213Tp321 - 1981 81.1655-18


1194 190 FV 377 C.S. S.S.Tp347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Hot Eff.Res.Exchs.E41/42-002A/B 4 - 60.300 143 FV 405 SA213Tp321 - 1981 81.1677-01

Kuwait Breech Lock Type 6.096 1¼ Cr ½ Mo S.S.Tp347 w.o. -

966 157 FV 348 1¼ Cr ½ Mo - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Warm Eff.Rec.Gas Exch.E-41/42-003 2 - 27.000 143 FV 377 SA213Tp321 - 1981 81.1677-02


1194 190 FV 377 C.S. S.S.Tp347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Hot Eff.Res.Exchs.E81/82-002A/B 4 - 60.300 143 FV 405 SA213Tp321 - 1982 82.1699-01


966 157 FV 348 1¼ Cr ½ Mo - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Warm Eff.Rec.Gas Exch.E-81/82-003 2 - 27.000 143 FV 377 SA213Tp321 - 1982 82.1699-02


966 157 FV 293 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi Cool Eff.Rec.Gas Exch.E-81/82-005 2 - 34.700 143 FV 321 SA179 - 1982 82.1699-03


712 175 FV 470 3 Cr 1 Mo S.S.Tp347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 1st Stg.make-up Hyd./Effl.Exch. E-84-100 1 - 31.400 186 FV 470 SA213Tp321 - 1983 83.1707-01


712 175 FV 470 3 Cr 1 Mo S.S.Tp347 w.o. -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 2nd Stg.make-up Hyd./Effl.Exch. E-84-200 1 - 31.400 186 FV 470 SA213Tp321 - 1983 83.1707-02


1220 18 FV 230 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 1st Stg.Effluent Steam Gen. E-84-102 1 - 41.100 171 FV 360 SA209T1 - 1983 83.1707-03


1270 22 - 215 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 1st Stg.Eff/H2S Strip.Feed Exch.E-84.103 1 - 54.800 169 FV 290 SA209T1 - 1983 83.1707-04








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1220 18 FV 230 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi 2nd Stg.Eff.Steam Generator E-84-202 1 - 41.100 172 FV 360 SA209T1 - 1983 83.1707-05


762 196 FV 200 C.S. - -

K.N.P.C. Lummus Hydrocracking Mina Al-Ahmadi HHPS Vapor/Recycle gas Exch. E-84-203 1 - 27.200 176 FV 280 SA209T1 - 1983 83.1707-06


1372 175 FV 470 2¼ Cr 1 Mo S.S.Tp347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st Stg Reactor Feed/Effl. E-14-102 AB 2 - 181.200 195 FV 470 SA213Tp321 - 1984 84.1733-01

Kuwait Breech Lock Type 6.706 2¼ Cr 1 Mo S.S.Tp347 w.o. -

1220 16 - 232 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st Stg Reactor Effl./Steam Gen.E-14-103 1 72 36.600 170 FV 395 SA209T1 - 1984 84.1733-02


1270 28 - 205 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st Stg Rct.Effl/H2S Strip.Feed E-14-104 1 - 50.800 170 FV 290 SA179 - 1984 84.1733-03


712 175 FV 470 3 Cr 1 Mo S.S.Tp347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 1st State Make up H2/React.Effl.E-14-105 1 - 14.400 186 FV 470 SA213Tp321 - 1984 84.1733-04

Kuwait Breech Lock Type 3.048 3 Cr 1 Mo S.S.Tp347 w.o. -

1372 175 FV 470 2¼ Cr 1 Mo S.S.Tp347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage React.Feed/Effl. E-14-107 A/B 2 - 168.600 194 FV 455 SA213Tp321 - 1984 84.1733-05

Kuwait Breech Lock Type 6.400 2¼ Cr 1 Mo S.S.Tp347 w.o. -

1220 16 - 232 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage React.Effl/Steam Gen.E-14-108 1 72 36.600 172 FV 380 SA209T1 - 1984 84.1733-06


839 196 FV 235 C.S. - -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage HHPS Vapor/Recyc.Gas E-14-1091 - 17.500 170 FV 280 SA179 - 1984 84.1733-07


712 176 FV 470 3 Cr 1 Mo S.S.Tp347 w.o. -

K.N.P.C. C.F. Braun Hydrocracking Mina Abdulla 2nd Stage Make UP M2/React.Effl.E-14-1101 - 14.400 186 FV 470 SA213Tp321 - 1984 84.1733-08

Kuwait Breech Lock Type 3.048 3 Cr 1 Mo S.S.Tp347 w.o. -

889 179,4 - 455 SA336F22 S.S.Tp347 w.o. 1 layer -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Feed Effluent Exch. E 1210 A/B 2 - 36.400 195,1 - 441 SA213Tp321 - 1986 86.1776-01

China, People's Rep. of Breech Lock Type 7.316 SA336F22 S.S.Tp347 w.o. 1 layer -

813 29,5 - 227 SA516-70 - -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Reactor Eff./Dist.Feed Exch. E 1230 1 - 16.500 177,5 - 441 SA213T11 - 1986 86.1776-02

China, People's Rep. of Breech Lock Type 6.096 SA336F11 - -

737 176,1 - 454 SA336F22 S.S.Tp347 w.o. 1 layer -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Reactor Feed/React.Eff.Exch. A/B 4 - 26.400 197,9 - 440 SA213Tp321 - 1986 86.1776-03


940 173,7 - 441 SA336F22 S.S.Tp347 w.o. 1 layer -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli Reactor Feed/HHPS Vapor Exch. A/B 2 - 37.500 200,1 - 427 SA213Tp321 - 1986 86.1776-04


483 172,8 - 343 SA336F11 - -

QILU PETROCHEMICAL Hua Lu Eng.Co. Hydrocracking Shengli HHPS Vapor/Feed Gas Exch. A/B 2 - 11.000 201,7 - 296 SA213Tp321 - 1986 86.1776-05

China, People's Rep. of Breech Lock Type 6.096 SA336F11 - -

1042 164,7 - 437 SA387-22CL2 S.S.Tp308L w.o. -

NESTE OY FINLAND Neste Oy Hydrocracking Porvoo Reactor Feed/Eff. Exch.EA-301 A,B,C/II 3 - 38.000 153,1 - 454 SA213Tp321 - 1988 88.1813

Finland Breech Lock Type 7.747 SA336F22 S.S.Tp308L w.o. -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1093 142 - 350 SA182F11 S.S.Tp347 -

K.N.P.C. JGC Hydrocracking Mina Al-Ahmadi Tube bundles for E41/E42-E81/E82/004A 4 - 23.500 - - - SA213Tp321 - 1989 89.1848-01


1143 142 - 150 SA266CL2 Inconel 625 -

K.N.P.C. JGC Hydrocracking Mina Al-Ahmadi Tube bundles for E41/E42-E81/E82/007A-B 4 - 18.800 - - - INCOLOY 880 - 1989 89.1848-02


788 186 - 410 SA336F22 S.S.Tp347 w.o. -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 A/B 2 - 23.000 166 - 455 SA213Tp321 - 1990 90.1892

Turkey Breech Lock Type 5.000 SA336F22 S.S.Tp347 w.o. -

788 186 - 370 SA336F22 S.S.Tp347 w.o. -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 C/D 2 - 23.800 166 - 425 SA213Tp321 - 1990 90.1892


788 186 - 300 SA336F11 - -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 E/F 2 - 21.600 166 - 375 SA213Tp321 - 1990 90.1892


788 186 - 220 SA266CL2 - -

TUPRAS JGC Hydrocracking Kirikkale Combined Feed Exch. E 1351 G/H 2 - 22.000 166 - 315 SA260Tp405 - 1990 90.1892


1194 120 - 415 SA387-11CL2 S.S.Tp309LNB w.o. -

NESTE OY Neste Oy Hydrotreating Kulloo Reactor Feed Effl.H.E.EA-34000 A/F 6 - 40.500 108 - 445 SA213Tp321 - 1992 92.1941

Finland Breech Lock Type 6.096 SA336F11 S.S.Tp309LNB w.o. -

889 146 - 371 SA266CL2 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Hot Fresh Feed Exch. E-1101 1 - 25.500 133 - 435 SA213Tp321 - 1993 93.1965-01

China, People's Rep. of Breech Lock Type 5.000 SA336F22 S.S.Tp347 w.o. -

889 150 - 365 SA336F11 S.S.Tp347 w.o. -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Hot Recycle Gas Exch. E-1102 1 - 22.500 132 - 399 SA213Tp321 - 1993 93.1965-02

China, People's Rep. of Breech Lock Type 3.506 SA336F22 S.S.Tp347L w.o. -

889 147 - 293 SA336F11 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Cold Fresh Feed Exch. E-1103 A/B 2 - 21.400 130 - 371 SA213Tp321 - 1993 93.1965-03


889 152 - 245 SA336F11 - -

JILIN CHEMICAL IND.CO. Sinopec Hydrocracking Jilin Cold Recycle Gas Exch. E-1104 1 - 22.800 128 - 287 SA213Tp321 - 1993 93.1965-04


635 186 - 371 SA336F22 S.S.Tp347 w.o. -

LANZHOU PETR. & CHEM. Sinopec Lube Oil Hydro. Lanzhou HDF React.Feed/Eff.H.E.E-101A/B/C/D 4 - 16.200 175 - 395 SA213Tp321 - 1994 94.1981


788 188 - 392 SA336F22 S.S.Tp347 w.o. -

LANZHOU PETR. & CHEM. Sinopec Lube Oil Hydro. Lanzhou HDR React.Feed/Eff.H.E.E-101A/B/C 3 - 27.600 176 - 447 SA213Tp321 - 1994 94.1981


1220 172 - 410 SA336F22 S.S.Tp347 w.o. -

YUKONG Fluor Daniel FCCU Ulsan HHPS Vapor/Total Gas E 1330 1 - 56.700 229 - 360 SA213Tp321 - 1994 94.1990

South Korea Breech Lock Type 6.096 SA336F22 S.S.Tp347 w.o. -

1220 173 - 454 SA336F22 S.S.Tp347 w.o. -

YUKONG Fluor Daniel FCCU Ulsan Reactor Feed/Effl. Exch. E 1310/11 2 - 55.000 216 - 384 SA213Tp321 - 1994 94.1990

South Korea Breech Lock Type 6.096 SA336F22 S.S.Tp347 w.o. -

2540\1524 5,7 - 180 SA516-70 - -

YUKONG Fluor Daniel FCCU Ulsan Effluent LP Steam Gen. E 1340 1 - 36.000 170 - 250 SB163 (Incoloy 825) Incoloy 825 w.o. 1994 94.1990

South Korea Breech Lock Type 6.096 SA336F11 on tubesheet -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

889 196 - 275 SA336F11 S.S.Tp347 w.o. -

ZHEN HAI REF.& CHEM. Sinopec Hydrocracking Ningbo Reactor Eff./Cold Recycle E 303 1 - 24.000 176 - 348 SA213Tp321 - 1994 94.2003


1042 192 - 375 SA336F22 S.S.Tp347 w.o. -

ZHEN HAI REF.& CHEM. Sinopec Hydrocracking Ningbo Reactor Eff./Hot Fr. Feed E 302A/B 2 - 35.000 177 - 398 SA213Tp321 - 1994 94.2003


940 115 - 455 SA387-22CL1 S.S.Tp347 w.o. -

THAI PETROCHEM. IND. Stone & Webster Refinery Rayong Reactor Effl./Feed Exch. E-002 A/B 2 - 32.300 138 - 370 SA213Tp321 - 1995 95.1016-01

Thailand Breech Lock Type 7.925 SA336F22 S.S.Tp347 w.o. -

610 138 - 235 SA516-70 - -

THAI PETROCHEM. IND. Stone & Webster Refinery Rayong Rec. Gas/HHPS Gas Exch.E-003 A/B 2 - 11.500 115 - 246 SA179 - 1995 95.1016-02

Thailand Breech Lock Type 4.572 SA105N - -

813 152 - 226 SA516-70 - -

K.N.P.C. Belleli Refinery Mina Abdulla Recycle Gas Preheater E-12-105/205 2 - 23.500 131 - 288 SA213Tp321 S.S.Tp347 w.o. 1995 96.1020

Kuwait Breech Lock Type 6.096 SA182F1 S.S.Tp347 w.o. -

1448 10,67 - 250 SA516-60 - -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul First Reactor Feed Preheater Exchanger 1 - 32.000 97,12 - 175 SA179 - 2001 01.1115-01

Brazil Breech Lock Type 6.096 SA266-4 - -

1372 95,94 - 245 SA38711-CL2 S.S.Tp347 w.o. -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Second Reactor Feed Preheater Exchanger 1 - 41.000 78,3 - 300 SA213Tp347 - 2001 01.1115-02

Brazil Breech Lock Type 6.096 SA38711-CL2 - -

1372 95,26 - 302 SA38711-CL2 S.S.Tp347 w.o. -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Reactor Feed Effluent Exchanger 1 - 41.000 79,09 - 361 SA213Tp347 - 2001 01.1115-03

Brazil Breech Lock Type 6.096 SA336F11 - -

1372 94,37 - 369 SA38711-CL2 S.S.Tp347 w.o. -


Brazil Breech Lock Type 6.096 SA336F11 S.S.Tp347 w.o. -

1372 93,39 - 418 SA38711-CL2 S.S.Tp347 w.o. -


Brazil Breech Lock Type 6.096 SA336F11 S.S.Tp347 w.o. -

1372 5,88 - 60 SA516-60 - -

PETROBRAS Toyo Hydrotreating Rio Grande do Sul Reactor Feed Final Cooler 2 - 18.000 77,69 - 170 SA179 - 2001 01.1115-06

Brazil Breech Lock Type 6.096 SA266-4 - -

889 148,9 - 454,5 SA 387 22 2+W.O. S.S.Tp347 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta Reactor N° 1 Effluent Hot Rec. Gas Exch. 1 57+4wo 26.300 163,1 - 426,7 SA 249Tp 321 - 2001 01.1119-01

Canada Breech Lock Type 6.096 SA 336 F22 3 S.S.Tp347 -

1347 148,2 - 435 SA 387 22 2+W.O. S.S.Tp347 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta Reactor N° 1 Effluent Gas Oil Feed Exch. 4 83+4wo 54.000 160 - 407 SA 249Tp 321 - 2001 01.1119-02

Canada Breech Lock Type 6.096 SA 336 F22 3 S.S.Tp347 -

915 147,2 - 399 SA 387 22 2+W.O. S.S.Tp347 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta Reactor N° 1 Effluent Medium Rec. Gas Exch.1 54+4wo 26.500 164,1 - 321 SA 249Tp 321 - 2001 01.1119-03


1245 112,7 - 316 SA 387 11 2 - -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta HHPS Vapor Stripper Feed Exch. 2 55 41.400 146,5 - 371 SA 268Tp 405 - 2001 01.1119-04

Canada Breech Lock Type 4.268 SA 336 F22 3+W.O. S.S.Tp347 -

1016 146,5 - 302 SA 387 11 2+W.O. INCONEL 625 -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta HHPS Vapor Recycle Gas Exch. 2 57+6.4wo 34.100 190 - 265,5 SB 704 N06625 - 2001 01.1119-05








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118 112,7 - 235 SA 516-70 - -

CANADA EDMONTON SNC LAVALIN Unicracking Edmonton - Alberta HHPPS Vapor Trim Condenser 2 51 39.000 146,5 - 274 SA 789 S31803 - 2001 01.1119-06

Canada Breech Lock Type 6.096 SA 266 Gr.2 - -

1016 206,8 - 447 SA 336 F22 V S.S.Tp347 -

K.N.P.C. KNPC/Dan Trading Refinery Shuaiba R.H. Reactor Overhead H2 Feed Exchanger4 82 34.000 206,8 - 361 SA 213 TP321 - 2002 02.1129-01


864 7,58 - 290 SA 336 F22 V S.S.Tp347 -

K.N.P.C. KNPC/Dan Trading Refinery Shuaiba Reactor Effluent Raw Light Diesel H.E. 1 12 14.460 159,2 - 334 SA 213 TP321 - 2002 02.1129-02


1347 77,4 - 437 SA 387 11 2 TP 347 -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Hot Recycle Gas Exchanger1 38+4.5wo 38.700 93 - 408 SA 213 TP321 - 2002 02.1137-01


1347 77,4 - 390 SA 387 11 2 - -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Hot Feed Exchanger 4 38+4.5wo 48.200 141,2 - 376 SA 213 TP304 - 2002 02.1137-02


1235 73,5 - 297 SA 387 11 2 - -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Cold Feed Exchanger 4 36 35.700 141,2 - 297 SA 268 TP410 - 2002 02.1137-03


1372 72,6 - 297 - - -

TUPRAS LG Eng. Constr. Co. DHP Project Izmir Reactor Effluent/Cold Recycle Gas Exchanger1 39 38.300 93,2 - 246 SA 199 T11 - 2002 02.1137-04

Turkey Breech Lock Type 6.096 - - -

1150 228,5 - 410 SA 336 M F22 CL3 S.S. Tp 309L -

FPCC HEC Refinery Mailiao Feed Reactor Effluent Exchanger 6 112 55.678 211,8 - 455 SA 213 M TP347 S.S. Tp 347 2005 05.1168-01

Taiwan Breech Lock Type 6.100 SA 336 M F22 CL 3 - -

899 139,2 - 265 SA 516 M Gr 485 S.S. Tp 304L -

FPCC HEC Refinery Mailiao HTS Overhead/LTS Bottom Exchanger 1 55 29.417 208,9 - 325 SB 423 UNS MO 8825 - 2005 05.1168-02


899 234,3 - 215 SA 266 M Gr 2 S.S. Tp 304L -

FPCC HEC Refinery Mailiao HTS Overhead/Treat Gas Exchangerr 1 89 30.597 205,9 - 240 SA 789 M UNS 531803 - 2005 05.1168-03

Taiwan Breech Lock Type 6.100 SA336 M F11 CL 3 - -

800 229,5 - 395 SA 336 M F22 CL3 S.S. Tp 309L -

FPCC HEC Refinery Mailiao Feed/HDW Reactor Effluent Exchanger 4 78 21.725 215,7 - 415 SA 213 M TP347 - 2005 05.1168-04


500 242,2 - 240 SA 336 M F11 CL3 - -

FPCC HEC Refinery Mailiao HTS Overhead/Treat Gas Exchangerr 1 50 11.700 209,9 - 280 SA 213 M Gr - 2005 05.1168-05


595 138,3 - 95 SA 516 M Gr 485 - -

FPCC HEC Refinery Mailiao HTS Ttrim Cooler Exchanger 1 50 23.700 206,9 - 182 SA 179 M - 2005 05.1168-06

Taiwan Breech Lock Type 6.100 SA 266 M Gr 2 - -

1601 176 - 454 SA 336 F22 CL3 S.S. Tp 347


Licensor Chevron USA 5.029 SA 336 F22 CL 3 S.S. Tp 347

1524 174 - 427 SA 336 F22 CL3 S.S. Tp 347


Licensor Chevron 5.334 -

1325 139 410 SA 965M F347 -

PETROBRAS PETROBRAS Refinery RNEST B.L. Type Heat Exchangers 12 78,5 46.000 126 430 SA213M 347 - 2010 10.1200

Brazil 5.486 SA387MGr22CL2 S.S Tp 347







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1236 139 410 SA 965M F347 -

PETROBRAS PETROBRAS Refinery RNEST B.L. Type Heat Exchangers 4 69,5 28.300 127 430 SA213M 347 - 2010 10.1200

Brazil 2.438 SA387MGr22CL2 S.S Tp 347

1047 205 343 SA 336 Gr F 22

YOOBASE SKEC Refinery Ulsan B.L. Type Heat Exchangers 2 80 36.500 184 298 SA 213 T22 - 2011 11.1202-01

Korea 6.100 SA 336 F22

1310 204 400 SA 965M Gr 321

YOOBASE SKEC Refinery Ulsan B.L. Type Heat Exchangers 4 103 51.800 191 367 SA 213 TP 321 SS Tp 347 2011 11.1202-02

Korea 6.100 SA 387 Gr 22 Cl 2

550 205 343 SA 336 Gr F 22

YOOBASE SKEC Refinery Ulsan B.L. Type Heat Exchangers 1 46 11.500 183 183 SA 213 T22 - 2011 11.1202-03

Korea 6.100 SA 336 F22

1250 202,5 - 454 SA 336 F22 CL3 SS Tp 347 -

SK LUBRICANTS SKEC Refinery Ulsan B.L. Type Heat Exchangers 2 114 71.500 225,2 - 374 SA 213 Tp. 321 - 2011 11.1205-01

Korea - 6.100 SA 336 F22 CL3 SS Tp 3447 -

1500 49,3 - 420 SA 516 Gr 485 - -

SK LUBRICANTS SKEC Refinery Ulsan HP Steam Generator 1 47 35.700 200,9 - 420 SB 163 NO8825 - 2011 11.1205-02


580 231 - 217 SA 336 F22 CL3 - -

SK LUBRICANTS SKEC Refinery Ulsan B.L. Type Heat Exchangers 1 55 2.840 199,6 - 298 SB 163 UNS NO8825 - 2011 11.1205-03

Korea - 4.880 SA 336 F22 CL3 Alloy 625 -

1500 6,3 - 200 SA 516 Gr 485 - -

SK LUBRICANTS SKEC Refinery Ulsan LP Steam Generator 1 20 26.800 198,5 - 270 SB 163 NO8825 - 2011 11.1205-04


1.270 176,8 - 454 SA 336 F22 CL3 SS Tp 347

LUBEREF SAMSUNG/Chevron Refinery Yanbu HCR Feed/Effluent Exchanger 2 82+8.5wo 51.000 194,5 - 431 SA 213 TP 321 2013 13.1214-01

Saudi Arabia Breech Lock Type 4.877 SA 336 F22 CL3 SS Tp 347

686 197,8 - 288 SA 336 F22 CL3

LUBEREF SAMSUNG/Chevron Refinery Yanbu HCR HHPS Vapor/Recycle Gas Exchanger 2 47 12.000 169,4 - 316 SA 213 Tp. 321 2013 13.1214-02


686 197,8 - 288 SA 336 F22 CL3 SS Tp 347

LUBEREF SAMSUNG/Chevron Refinery Yanbu HCR HHPS Vapor/Recycle Gas Exchanger 1 57 12.350 169,4 - 316 SB 444 Gr.1 N06625 2013 13.1214-03


711 173,1 - 431 SA 336 F22 CL3 SS Tp 347

LUBEREF SAMSUNG/Chevron Refinery Yanbu HCR Reactor Effl. Ex./Frac. Feed Exch. 2 52+8.5 22.200 133,2 - 343 SB 444 Gr.1 N06625 2013 13.1214-04

Saudi Arabia 6.500 SA 336 F22 CL3 SS Tp 347

711 170,8 - 360 SA 336 F22 CL3 SS Tp 347

LUBEREF SAMSUNG/Chevron Refinery Yanbu 2nd HCR Feed/Effleunt Exchanger 2 41+8.5 15.000 197,1 - 300 SA 213 Tp. 321 2013 13.1214-05


767 190,7 - 292 SA 336 F22 CL3

LUBEREF SAMSUNG/Chevron Refinery Yanbu DW Feed/HDF Effluent Exchanger 2 50 18.800 166,7 - 343 SA 213 Gr.T 22 2013 13.1214-06

Saudi Arabia Breech Lock Type 6.096 SA 336 F22 CL3

838 187,4 - 400 SA 336 F22 CL3 SS Tp 347

LUBEREF SAMSUNG/Chevron Refinery Yanbu Dw Feed / DW Effluent Exhcanger 2 54+8.5 22.100 173,1 - 428 SA 213 Tp. 321 2013 13.1214-07


482 165,1 - 343 SA 336 F22 CL3

LUBEREF SAMSUNG/Chevron Refinery Yanbu DW HHPS Vapor/Recycle Gas Exchanger 2 30 7.400 190,1 - 260 SA 213 Gr.T 22 2013 13.1214-08

Saudi Arabia 5.735 SA 336 F22 CL3







DESIGN CONDITIONS

USER ENGINEER/LICENSOR PLANT TYPE LOCATION DESCRIPTION No. SIZE WEIGHT PRESS. TEMP. MATERIALS CLADDING YEAR JOB No.

[mm] [Kg.] [Bar] [°C]

1.500 454 SA 336 Gr F22 Cl.3 SS Tp 347

OPTARA TECNICAS REUNIDAS Refinery Belgium B.L. Type Heat Exchangers 2 96+5 83.900 400 SA 213 Tp321 2013 13.1215

6.096 SA 336Gr F22 Cl.3 SS Tp 347

1.372 201,3 - 254 SA 387 Gr 22 Cl 2

MOTIVA JACOBS/Chevron Refinery Port Arthur B.L. Type Heat Exchangers 2 90 80.400 170,6 - 299 SB 163 N08825 2015 15.1225

Texas, USA 7.316 SA 336 Gr F22 Cl.3 Inconel 625

1.600 190,9 399 SA 387 F22 CL2 SS Tp 347

MOTIVA JACOBS/Chevron Refinery Porth Arthur B.L. Type Heat Exchangers 3 103+5 110.800 176,1 450 SA 213 Tp. 347 2015 15.1225

Texas, USA 7.316 SA 336 F22 CL3 SS Tp 347




205.0

176.0


Materials: Carbon Steels,Micro-Alloyed (high strength) SteelLow Alloy Steels300 Series SteelsDuplex Stainless Steels

MaximumDimensions:

Reactor Length: 30.000 mmShell Diameter: 7.200 mmN. of tubes 29.400

30 large units built since 1989

Licensors: Shell, BASF, Scientific Design, Lurgi, Toyo, KBR


Ethylene Oxide (EO), SMDS, Vinyl Acetate, OxoSynthesis, Gas-to-Liquid (GTL)

Process:

Units:

TUBULAR REACTORS

REFERENCE LIST - TUBULAR REACTORS SHEET: 1 of 1


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3861 12 - 204 SA 516 70 SA 240 Tp 304L -

QUANTUM CHEMICAL Fluor Daniel Vinyl Acetate La Porte Reactors 13 VR 5500/5501 2 25.4+3.2wo 150.000 10,5 - 204 SA 249 Tp 316L - 1989 89.1841

Texas, U.S. (Tubular) 10.897 SA 516 70 SA 240 Tp 316L -

5360 64 - 288 SA 302 C - -

P.D. GLYCOL Scientech Assoc.Inc. Ethylene Oxide Beaumont EO Reactor R-1120 1 103 605.550 23,7 - 325 SA 266 4 - 1989 89.1846

Texas, U.S. (Tubular) 11.176 - - -

6731 51 - 275 - - -

SHELL JGC SMDS Bintulu HPS Reactor R 3021/22/23/41 4 78 890.000 54 - - 20 Mn Mo Ni 4 5 - 1989 89.1855

Malaysia (Tubular) 12.865 - - -

3887 9 - 185 SA 516 70 - -

ANDHRA PETROCHEM. Davy McKee Oxo Visag Reactor Converter 03/D163-01 1 20 92.000 7,8 - 250 SA 210 A1 - 1989 89.1870-02

India (Tubular) 11.989 SA 516 70 - -

4420 23 - - - - -

BASF Basf Ethylene Oxide Antwerp EO Reactors C-101 A/B/C 3 90 425.000 60 - 320 20 Mn Mo Ni 4 5 SA 240 Tp 304L 1990 90.1896

Belgium (Tubular) 21.209 - on head only -

4268 9,8 - 205 SA 240 Tp 316L - -

SAMSUNG-BP CHEMIC Samsung VAM Ulsan VA Reactor R-5101 1 22 149.000 9,8 - 220 SA 213 Tp 316L - 1995 95.1008

South Korea (Tubular) 9.170 SA 240 Tp 316L - -

1270 162 - 170 SA 516 70 - -

PAKARAB Kellogg Ammonia Multan Feed Effluent H.E. 121-C 1 94 82.500 162 - 190 SA 210 A1 - 1996 96.1034

Pakistan (Tubular) 12.726 SA 516 70 - -

2236 48 - 315 SA 387 5 2 - -

PHILLIPS PETROLEUM Bechtel Methyl Mercaptan Borger Mesh Reactor 95-MM1 1 51 72.000 41 - 315 SA 213 T9 - 1996 96.1041

Texas, U.S. (Tubular) 6.096 SA 516 70 S.S. Tp 304L w.o. -

5563 65,5 - 290 SA 516 70 DOWN CONE: Tp 304L -

NPC TECNIMONT Ethilene Oxide Marun EO reactor 2 144 810.000 21 - 310 SA 210 A1 - 2001 01.1125

Iran (Tubular) 12.294 SA 516 70 - -

5563 65,5 - 290 SA 516 70 DOWN CONE: Tp 304L -

JAM TECNIMONT Ethilene Oxide Bandar Assaluyeh EO reactor 2 144 810.000 21 - 310 SA 210 A1 - 2002 02.1133

Iran (Tubular) 12.294 SA 516 70 - -

7032 70 - 290 Tubes 19 Mn 5 304 L on bottom head -

QATAR SHELL GTL SHELL GTL Ras Laffan HPS Reactors 6 193+5 1.125.000 70 - 290 Tubesh 20 Mn Mo Ni 45 - 2005 05.1171

Qatar (Tubular) 12.979 Shell 20 Mn Mo Ni 45 - -

7032 70 - 290 Tubes 19 Mn 5 304 L on bottom head -

QATAR SHELL GTL SHELL GTL Ras Laffan HPS Reactors 6 193+5 1.125.000 70 - 290 Tubesh 20 Mn Mo Ni 45 - 2006 06.1180

Qatar (Tubular) 12.979 Shell 20 Mn Mo Ni 45 - -





Licensors: Stamicarbon, Snamprogetti, Toyo Engineering

Units: > 50 units built


Equipment type:

Urea StripperCarbamate Condensers ScrubbersUrea Reactors

Materials: High Strength Carbon Steel316 L Urea Grade Stainless Steel25-22-2 High Alloy SteelsSafurexDuplex Steel

UREA EQUIPMENT

REFERENCE LIST - UREA EXCHANGERS SHEET: 1 of 4


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1499 6 - 180 K.C.S. - -

NAT.FERT.CORP. Snamprogetti Urea Mirpur Mathelo First Carbamate Condenser 1 91 58.500 166 - 210 X2 Cr Ni Mo 25 22 2 - 1975 75.1355-01

Pakistan - 12.396 K.C.S. S.S. Tp 316L mod. Lin -

1499 6 - 180 K.C.S. - -

NAT.FERT.CORP. Snamprogetti Urea Mirpur Mathelo 2nd Carbamate Condenser 1 91 58.500 166 - 210 X2 Cr Ni Mo 25 22 2 - 1975 75.1355-02

Pakistan - 12.396 K.C.S. S.S. Tp 316L mod. Lin -

1397 5 - 180 K.C.S. - -

*** Snamprogetti Urea Novomoskowsk First Carbamate Condenser 1 84 47.500 165 - 210 X2 Cr Ni Mo 18 12 DIN mod. 1975 75.1359-01

U.S.S.R. - 12.700 K.C.S. S.S. Tp 316L mod. Lin -

1397 5 - 180 K.C.S. - -

*** Snamprogetti Urea Novomoskowsk 2nd Carbamate Condenser 1 84 47.500 165 - 210 X2 Cr Ni Mo 18 12 DIN mod. 1975 75.1359-02


1677 29 - 225 K.C.S. - -

SEMADCO Foster Wheeler Urea Thalka Urea Stripper 2 - 67.500 159 - 225 X2 Cr Ni Mo 25 22 2 - 1975 75.1364-01

Egypt - 6.020 K.C.S. S.S. Tp 316L mod.w.o. -

1448 8 - 164 K.C.S. - -

SEMADCO Foster Wheeler Urea Thalka Urea Condenser 2 - 60.000 159 - 183 X2 Cr Ni Mo 18 12 DIN mod. 1975 75.1364-02

Egypt - 12.040 K.C.S. S.S. Tp 316L mod.w.o. -

635 12 - 183 K.C.S. - -

SEMADCO Foster Wheeler Urea Thalka Urea Scrubber 2 84 16.500 159 - 183 X2 Cr Ni Mo 18 12 DIN mod. 1975 75.1364-03

Egypt - - K.C.S. S.S. Tp 316L mod.w.o. -

1397 5 - 180 K.C.S. - -

*** Snamprogetti Urea Togliattigrad First Carbamate Condenser 1 84 47.500 165 - 210 X2 Cr Ni Mo 18 12 DIN mod. 1975 75.1367-01


1397 5 - 180 K.C.S. - -

*** Snamprogetti Urea Togliattigrad 2nd Carbamate Condenser 1 84 47.500 165 - 200 X2 Cr Ni Mo 18 12 DIN mod. 1975 75.1367-02


1169 9 - 200 C.S. - -

GUANOMEX Snamprogetti Urea Minatitlan First Carbamate Condenser 1 - 46.000 165 - 200 SA 213 Tp 316LUrea - 1977 77.1440

Mexico - 12.446 K.C.S. - -

2210 25 - 225 K.C.S. - -

S.P.L.A.J. Uhde Urea Marsa El Brega Stripper E 201 1 - 135.000 163 - 225 X2 Cr Ni Mo 25 22 2 - 1981 81.1659

Libya - 7.010 SA508CL3/K.C.S. S.S. Tp 316L w.o. -

2058 6 - 164 C.S. - -

S.P.L.A.J. Uhde Urea Marsa El Brega Carbamate Condenser E 202 1 - 125.000 162 - 220 X2 Cr Ni Mo 18 12 - 1981 81.1660

Libya - 12.142 SA508CL3/K.C.S. S.S. Tp 316L w.o. -

2134 33,1 - 225 C.S. X Cr Ni Mo -

UNOCAL 76 Stamicarbon Urea Kenai Stripper 1 - 145.000 177,9 - 225 X2 Cr Ni Mo 25 22 2 S.S. Tp25 22 2 1985 85.1759-01

Alaska, U.S. - 7.112 - - -

2032 10,8 - 188 C.S. X Cr Ni Mo -

UNOCAL 76 Stamicarbon Urea Kenai Carbamate Condenser 1 - 120.000 177,9 - 188 X2 Cr Ni Mo 25 22 2 S.S. Tp25 22 2 1985 85.1759-02

Alaska, U.S. - 12.192 - - -

915 18,23 - 188 C.S. X Cr Ni Mo -

UNOCAL 76 Stamicarbon Urea Kenai Scrubber 1 - 46.000 173,4 - 188 X2 Cr Ni Mo 25 22 2 S.S. Tp25 22 2 1985 85.1759-03

Alaska, U.S. - 2.794 - - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2617 25 - 214 SA 516 70 - -

P.T. PUPUK SRIWIDJAJA Rekayasa/Toyo Urea Palembang Urea Stripper 1 - 192.000 180 - 190 DP12 - 1990 90.1900

Indonesia - 5.995 SA 266 2 Lining DP12 -

2159 8 - 175 C.S. X2 Cr Ni Mo -

CANADIAN FERT. Stamicarbon Urea Medicine Hat Carbamate Condenser 1 - 136.000 160 - 183 X2 Cr Ni Mo 25 22 2 33 25 22 2 1993 93.1953

Canada - 11.303 - w.o./Lining -

2385\1625 5,4 - 180 SA 516 60 - -

CNTIC Snamprogetti Urea Jiujiang Carbamate Condenser E-105 1 - 66.200 162 - 200 X2 Cr Ni Mo 25 22 2 - 1993 93.1957

China, People's Rep. of - 12.726 SA 266 2 S.S. Tp 316L w.o./Lin -

2385\1625 5,4 - 180 SA 516 60 - -

CNTIC Snamprogetti Urea Hohoot Carbamate Condenser E-105 1 - 66.200 162 - 200 X2 Cr Ni Mo 25 22 2 - 1993 93.1958

China, People's Rep. of - 12.726 SA 266 2 S.S. Tp 316L w.o./Lin -

1065\2820 12,5 - 220 SA 516 70 - -

QAFCO Uhde/Belleli Urea Umm Sa'id Scrubber 22-E003 1 - 84.000 160 - 200 SA 213 Tp 316LUrea - 1994 94.1976

Qatar - 2.590 SA 516 70 S.S. Tp 316L Urea w.o. -

2337 31 FV 230 SA 516 70 - -

QAFCO Uhde/Belleli Urea Umm Sa'id Heat Exchanger 22-E001 1 - 186.000 160 - 220 X2 Cr Ni Mo 25 22 2 - 1994 94.1976


2236 31 FV 165 SA 516 70 - -

QAFCO Uhde/Belleli Urea Umm Sa'id Carbamate Condenser 22-E002 1 - 161.000 160 - 220 SA 213 Tp 316LUrea - 1994 94.1976


1651 25 - 225 SA 516 70 - -

P.I.C. Stamicarbon Urea Shuaiba Urea Stripper E-4202 A/B 2 - 70.000 160 - 225 X2 Cr Ni Mo 25 22 2 - 1995 95.1010

Kuwait - 5.182 SA 266 2 S.S. Tp25 22 2 w.o./Lin -

2312 31 FV 225 20 Mn 5 V - -

ABU QIR FERT. & CHEM. Uhde Urea Alexandria Stripper 322 E 001 1 - 150.000 160 - 225 X2 Cr Ni Mo N 25 22 2 X2 Cr Ni Mo 17 13 2 1996 96.1033-01

Egypt - 5.995 20 Mn 5 V - -

2320 31 FV 225 P355 NH - -

EFC Uhde Urea Suez H.P. Heat Exchanger Stripper 1 35 156.400 160 - 225 X2 Cr Ni Mo N 25 22 2 - 2004 04.1149-01

Egypt - 7.082 20 Mn 5 V - -

1050/2700 13,5 - 175 P355 NH - -

EFC Uhde Urea Suez H.P. Scrubber 1 20/78 42.300 160 - 200 X2 Cr Ni Mo 18 14 3 (BC01)- 2004 04.1149-02

Egypt - 2.852 20 Mn Mo Ni 4.5 - -

2150 8 FV 165 P355 NH - -

EFC Uhde Urea Suez H.P. Carbamate Condenser 1 20 137.800 160 - 200 X2 Cr Ni Mo 18 14 3 (BC01)- 2004 04.1149-03

Egypt - 12.292 20 Mn 5 V - -

2320 31 FV 225 P355 NH - -

EFC Uhde Urea Alexandria H.P. Heat Exchanger Stripper 1 35 156.400 160 - 225 X2 Cr Ni Mo N 25 22 2 - 2004 04.1150-01

Egypt - 7.082 20 Mn 5 V - -

1050/2700 13,5 - 175 P355 NH - -

EFC Uhde Urea Alexandria H.P. Scrubber 1 20/78 42.300 160 - 200 X2 Cr Ni Mo 18 14 3 (BC01)- 2004 04.1150-02

Egypt - 2.852 20 Mn Mo Ni 4.5 - -

2150 8 FV 165 P355 NH - -

EFC Uhde Urea Alexandria H.P. Carbamate Condenser 1 20 137.800 160 - 200 X2 Cr Ni Mo 18 14 3 (BC01)- 2004 04.1150-03

Egypt - 12.292 20 Mn 5 V - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2320 31 FV 225 P355 NH - -

EFC UHde Urea Helwan H.P. Heat Exchanger Stripper 1 35 156.400 160 - 225 X2 Cr Ni Mo N 25 22 2 - 2004 04.1161-01

Egypt - 7.082 20 Mn 5 V - -

1050/2700 13,5 - 175 P355 NH - -

EFC UHde Urea Helwan H.P. Scrubber 1 20/78 42.300 160 - 200 X2 Cr Ni Mo 18 14 3 (BC01)- 2004 04.1161-02

Egypt - 2.852 20 Mn Mo Ni 4.5 - -

2150 8 FV 165 P355 NH - -

EFC UHde Urea Helwan H.P. Carbamate Condenser 1 20 137.800 160 - 200 X2 Cr Ni Mo 18 14 3 (BC01)- 2004 04.1161-03

Egypt - 12.292 20 Mn 5 V - -

2429 160 - 225 Tubes 25-22-2-BC05 - -

UHDE UHDE Urea Plant Mopco H.P. Heat Exchanger Stripper 1 190+7 149.000 31 - 225 Channel 20 Mn 5V 18-14-3 BC01 2005 05.1174-01

Egypt - 5.994 Shell P355 NH Lining Channel -

2149 160 - 200 Tubes 18-14-3-BC01 - -

UHDE UHDE Urea Plant Mopco H.P. Heat Exchanger Condenser 1 12 138.000 8 - 165 Channel 20 Mn 5V 18-14-3 BC01 2005 05.1174-02


2692 160 - 200 Tubes 18-14-3-BC01 - -

UHDE UHDE Urea Plant Mopco H.P. Heat Exchanger Scrubber 1 69+7 46.000 13,5 - 175 Channel 20 Mn 5V 18-14-3 BC01 2005 05.1174-03


2410 29 - 225 SA 516 M Gr 70 - -

QAFCO QAFCO Urea Mesaieed HP Stripper 1 85 125.000 156 - 225 Safurex - 2010 10.1195

Qatar - 6.700 SA 508 Gr 3 GL 2 Safurex -

2270 160 - - 20 Mn Mo Ni 4 5 - -

CHEMOPROJEKT Chemoprojekt/Stac Urea Cherepovesky HP Heat Exchanger 1 110 95.000 25 - 225 Safurex - 2010 10.1199-01

Russia - 6.000 20 Mn Mo Ni 4 5 Safurex -

3200 160 - - 20 Mn Mo Ni 4 5 Safurex -

CHEMOPROJEKT Chemoprojekt/Stac Urea Cherepovesky Pool Reactor 1 106 10.500 - - 200 Safurex Safurex 2010 10.1199-03

Russia - 29.132 20 Mn Mo Ni 4 5 Safurex -

2400 160 - 225 SA5086 Gr 3 CL2 - -

ZIA FERTILIZER Stamicarbon Urea Bangladesh HP Heat Exchangers stripper 1 125 118.000 29 - 215 Safurex Safurex 2011 11.1201-01

India - 6.000 SA 508 Gr 3 GL 2 - -

2050 160 - 215 SA 266 Gr 3 - -

ZIA FERTILIZER Stamicarbon Urea Bangladesh HP Carbamate Condenser 1 130 112.000 8 - 194 Safurex Safurex 2011 11.1201-02

India - 11.200 SA266 Gr.3 - -

2515 24 - 240 SA 516 GR.70 - -

IFCO UHDE Urea Iowa HP Stripper 1 25 138.000 168 - 225 Safurex Safurex 2013 13.1213.01

USA - 6.809 SA 508 GR.3 CL.2 Safurex -

3600 167 - 200 SA 533 GR.B CL.2 Safurex -

IFCO UHDE Urea Iowa Pool Reactor 1 125 437.000 9 - 180 Safurex Safurex 2013 13.1213.02

USA - 13.100 SA 516 GR.70 Safurex -

1540 31,6 - 230 SA 516 GR.70 - -

YARA Stamicarbon Urea Yara Belle Plaine H.P. Stripper 1 130+5 67.000 166,6 - 230 SA 789 UNS S 32906 Safurex 2013 13.1217.01

USA - 6.660 SA 765 Gr IV Lining Channel -

2340 8 - 165 SA 516 GR.70 - -

YARA Stamicarbon Urea Yara Belle Plaine H.P. Carbamate Condenser 1 150+5 165.000 164,5 - 220 SA 789 UNS S 32906 Safurex 2013 13.1217.02

USA - 12.280 SA 765 Gr IV Lining Channel -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3200 181,3 - 428 SA 516 GR 70 Safurex -

QAFCO QAFCO Urea Doha HP Scrubber 1 101+5 85.000 2374 - 428 SA 789 UNS S 32906 Safurex 2015 15.1233

Qatar - 2.000 SA 182 Gr F310 Safurex -

2230 165 - 225 SA 765 Gr 4 Safurex -

KIMA FERTILIZER STAMICARBON/TECNIMONTUrea Egypt H.P. Heat Exchanger Stripper 1 30 142.000 24 - 230 Safurex Safurex 2015 15.1235.01

Egypt - 6.000 SA 516 Gr 70 Safurex -

3400 162 - 225 SA 533 GR.B CL.2 Safurex -

KIMA FERTILIZER STAMICARBON/TECNIMONTUrea Egypt Pool Reactor 1 120 342.000 7 - 180 Safurex Safurex 2015 15.1235.02

Egypt - 23.200 SA 204 Gr B - -





REFERENCE LIST - UREA VESSELS & REACTORS SHEET: 1 of 1


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2800 - - - 17 Mn Mo V 6 4 SA 240 Tp 316L -

S.P.L.A.J. NAPETCO Uhde Urea Marsa El Brega Urea Reactor R-201 1 97+7.5 300.000 161 - 220 - Mod. Urea 1981 81.1658

Libya - 33.250 - - -

3090 - - - SA 737 C S.S. Tp 316L -

QAFCO Uhde/Belleli Urea Umm Said Reactor 22-R001 1 148+6 440.000 160 - 183 - (mod. urea) 1994 94.1976

Qatar - 30.910 - - -

2950 - - - 20 Mn Mo Ni 4 5 X2 Cr Ni Mo 17 13 2 -

ABU QIR FERT. & CHEM. Uhde Urea Alexandria Urea Reactor 322 R 001 1 100 240.000 160 - 200 - Lining 1996 96.1033-02

Egypt - 25.000 - - -

3600 - - - 20 MnMoNi 4 5 Lining:X2CrNiMo17132 -

KAWASAKI KELLOGG/Stamicarbon Urea Plant Hainan Urea Reactor 1 120+10 281.500 160 - 197 - - 2001 01.1118


3810 - - - 20 MnMoNi 4 5 Lining: Safurex -

SAFCO IV Uhde Urea Al Jubail Urea Reactor 1 132 331.000 164 - 205 - - 2003 03.1144



SUEZ Uhde Urea Alexandria Urea Reactor R 001 1 101+10 258.100 160 - 200 VD-TUV 440/1 - 2004 04.1149-04

Egypt - 25.000 - - -


ALEXFERT Uhde Urea Alexandria Urea Reactor R 001 1 101+10 258.100 160 - 200 VD-TUV 440/1 - 2004 04.1150-04

Egypt - 25.000 - - -

2946 - - - 20 Mn Mo Ni 4 5 16-14-3 BC01 -

UHDE UHDE Urea Plant Mopco H.P. Urea Reactor 1 110 258.000 160 - 200 - - 2005 05.1174-04

Egypt - 25.501 - - -

3810 160 - - 20 MnMoNi 4 5 Lining: Safurex -

RUWAIS FERT IND UHDE Urea Fertil Abu Dhabi Urea Reactor 1 125+5 329.000 - - 220 - W.O. Safurex 2010 10.1197


2650 - - - 20 MnMoNi 4 5 Lining: Safurex -

CHEMOPROJECT Chemoprojekt/Stac Urea Cherepovetsky HP Scrubber 1 64,5 23.000 159 - 200 - W.O. Safurex 2010 10.1199-02

Russia - - - - -


Thickness



Materials: High Strength Carbon Steel 0.5Mo Low Alloy Steels1.25Cr-0.5Mo Steels2.25Cr-1Mo 2.25Cr-1Mo-0.25V ModifiedStainless Steel

Equipment type :

Ammonia Converter Ammonia Converter Baskets Waste Heat Boilers Gas-Gas Exchanger

Units:

KBR, Snamprogetti, Topsoe, Ammonia Casale, Uhde

Licensors:

> 40 units built


AMMONIA EQUIPMENT

REFERENCE LIST - AMMONIA HEAT EXCHANGERS SHEET: 1 of 8


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118 49 - 274 C.S. - -

SHAHPUR CHEM. M.W.Kellogg Ammonia Bandar-Shahpur Secondary W.H.B. 1 - 17.500 34 - 594 SA 213 T11 - 1974 74.1274

Iran - 2.744 1¼ Cr ½ Mo - -

1143 119 - 330 C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan Primary Shift Eff. Exch. 1 - 22.100 33 - 355 SA 209 T1 - 1974 74.1288-01

Pakistan - 3.810 ½ Mo - -

940 9 - 0 K.C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan First Stage Chiller 1 - 15.300 162 - 0 SA 179 - 1974 74.1288-03

Pakistan - 5.995 K.C.S. - -

966 9 - -15 K.C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan 2nd Stage Chiller 1 - 18.600 162 - 0 SA 179 - 1974 74.1288-04


1143 9 - -40 K.C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan Third Stage Chiller 1 - 21.800 162 - -28 SA 179 - 1974 74.1288-05


966 162 - -15 K.C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan Separator Eff./ 1 - 52.400 162 - -28 SA 179 - 1974 74.1288-06

Pakistan Separator Feed 13.285 K.C.S. - -

1372 18 - 60 K.C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan Synthesis Gas Compressor 1 - 32.800 162 - 87 SA 179 - 1974 74.1288-07

Pakistan Aftercooler 4.496 K.C.S. - -

1347 119 - 330 C.S. - -

PAKARAB M.W.Kellogg Ammonia Multan Secondary W.H.B. 1 - 36.300 39 - 593 SA 213 T11 - 1974 74.1295

Pakistan - 3.988 1¼ Cr ½ Mo - -

1347 119 - 330 C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Secondary W.H.B. 1 - 33.500 34 - 600 SA 213 T22 - 1974 74.1309-01

Brazil - 3.506 2¼ Cr 1 Mo - -

1169 119 - 320 C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Primary Shift Eff. W.H.B. 1 - 27.000 33 - 455 SA 209 T1 - 1974 74.1309-02

Brazil - 5.487 ½ Mo - -

1143 126 - 330 C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Methanator Eff. BFW Heater 1 - 29.200 30 - 455 SA 209 T1 - 1974 74.1309-03

Brazil - 6.096 ½ Mo - -

915 9 - 35 K.C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Feed & Recycle Gas First 1 - 13.000 159 - 60 SA 179 - 1974 74.1309-04

Brazil Stage Chiller 4.877 K.C.S. - -

915 9 - -28 K.C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Feed & Recycle Gas Second 1 - 16.000 159 - 0 SA 179 - 1974 74.1309-05


1169 9 - -45 K.C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Feed & Recycle Gas Third 1 - 22.500 159 - -28 SA 179 - 1974 74.1309-06


1321 18 - 65 K.C.S. - -

PETROBRAS M.W.Kellogg Ammonia Copeb Synthesis Gas Compressor 1 - 28.000 160 - 85 SA 179 - 1974 74.1309-07

Brazil Aftercooler 3.277 K.C.S. - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1601 122 - 370 C.S. - -

*** M.W.Kellogg Ammonia Pancevo Primary W.H.B. 1 - 75.800 35 - 330 SA 213 T11 - 1975 75.1334

Yugoslavia - 7.316 ½ Mo - -

1245 122 - 330 C.S. - -

*** M.W.Kellogg Ammonia Pancevo Secondary W.H.B. 1 - 33.000 35 - 595 SA 213 T11 - 1975 75.1335

Yugoslavia - 3.963 1¼ Cr ½ Mo - -

1118 33 - 468 C.S. - -

*** M.W.Kellogg Ammonia Pancevo Primary Shift Eff. W.H.B. 1 - 33.000 122 - 330 SA 209 T1 - 1975 75.1336

Yugoslavia - 5.512 ½ Mo - -

915 219 - -28 K.C.S. - -

N.E.T. M.W.Kellogg Ammonia Marino Point Feed & Recycle Gas 1 - 44.300 219 - -28 SA 179 - 1975 75.1363-01

Ireland Recycle Gas Exchanger 12.192 K.C.S. - -

1372 230 - 190 K.C.S. - -

N.E.T. M.W.Kellogg Ammonia Marino Point Ammonia Converter 1 - 104.500 230 - 175 SA 179 - 1975 75.1363-02

Ireland Feed/Eff. Exch. 12.192 K.C.S. - -

1220 130 - 310 K.C.S. - -

N.E.T. M.W.Kellogg Ammonia Marino Point NH3 Converter Feed Effluent Exch. 1 - 82.000 230 - 345 SA 209 T1 - 1975 75.1363-03

Ireland S.F.W. Exch. 14.020 ½ Mo - -

1169 6 - 70 K.C.S. - -

N.E.T. M.W.Kellogg Ammonia Marino Point Feed & Recycle Gas Cooler 2 - 31.700 219 - 85 SA 179 - 1975 75.1363-04

Ireland - 7.925 K.C.S. - -

1143 22 - 450 ½ Mo - -

SIR Struthers Wells Ammonia Catanzaro Waste Heat Boiler 1 - 30.000 120 - 343 SA 209 T1 - 1976 76.1408

Italy - 5.766 ½ Mo - -

1499 35 - 343 C.S. - -

INA M.W.Kellogg Ammonia Kutina Primary W.H.B. 2 - 67.000 150 - 344 SA 213 T11 - 1978 78.1497-01

Yugoslavia - 8.459 C.S. - -

1651 150 - 344 C.S. - -

INA M.W.Kellogg Ammonia Kutina Secondary W.H.B. 1 - 55.000 35 - 593 SA 213 T11 - 1978 78.1497-02

Yugoslavia - 4.877 1¼ Cr ½ Mo - -

1042 118 - 330 C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail Primary Shift Eff. W.H.B. 1 - 21.000 34 - 445 SA 209 T1 - 1980 80.1582-01

Saudi Arabia, Kingdom of - 4.496 ½ Mo - -

1093 30 - 330 ½ Mo - -

SAMAD M.W.Kellogg Ammonia Al Jubail Methanator Feed Heater 1 - 21.300 33 - 404 SA 209 T1 - 1980 80.1582-02


813 120 - 330 C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail Methanator Eff. Heater 1 - 22.100 31 - 455 SA 209 T1 - 1980 80.1582-04


991 9 - 13 K.C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail Feed & Recycle Gas 1 - 12.500 159 - 65 SA 179 - 1980 80.1582-05

Saudi Arabia, Kingdom of 1st Stage Chiller 3.506 K.C.S. - -

991 7 - -7 K.C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail Feed & Recycle Gas 1 - 17.000 159 - 1 SA 179 - 1980 80.1582-06

Saudi Arabia, Kingdom of 2nd Stage Chiller 5.995 K.C.S. - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1347 7 FV -33 K.C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail Feed & Recycle Gas 1 - 28.400 159 - -29 SA 179 - 1980 80.1582-07

Saudi Arabia, Kingdom of 3rd Stage Chiller 5.000 K.C.S. - -

1067 159 - -10 K.C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail NH3 Converter Feed Effluent Exch. 1 - 74.700 159 - -29 SA 179 - 1980 80.1582-08

Saudi Arabia, Kingdom of Recycle Exch. 16.510 K.C.S. - -

1194 154 - 180 C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail NH3 Converter Feed Effluent Exch. 1 - 77.200 159 - 155 SA 179 - 1980 80.1582-09

Saudi Arabia, Kingdom of - 14.500 C.S. - -

1042 120 - 300 C.S. - -

SAMAD M.W.Kellogg Ammonia Al Jubail Ammonia Conv./BFW Exch. 1 - 40.600 153 - 300 SA 209 T1 - 1980 80.1582-11


915 250 - 260 13 Cr Mo 4 4 - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio Hot Ammonia Exch. 1 - 46.000 250 - 300 13 Cr Mo 4 4 DIN17175 - 1980 80.1589-01

Portugal - 13.005 13 Cr Mo 4 4 DIN17175 - -

839 94 - 310 12 Mn 5 - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio BFW Preheater 1 - 14.000 250 - 350 10 Cr Mo 9 10 - 1980 80.1589-02

Portugal - 1.600 10 Cr Mo 9 10 Inconel w.o.on T.S. -

1067 7 - 50 C.S. - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio Water Cooler 1 - 34.100 250 - 100 SA 179 - 1980 80.1589-03

Portugal - 10.160 C.S. - -

661 250 - 75 19 Mn 5 - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio Cold Ammonia Exch. 1 - 8.600 250 - 75 SA 179 - 1980 80.1589-04

Portugal - 4.623 19 Mn 5 DIN17155 - -

813 20 - -30 K.C.S. - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio Ammonia Chiller 1 55 19.200 250 - -10 SA 179 - 1980 80.1589-05

Portugal - 6.630 K.C.S. - -

1016 58 - 425 ½ Mo - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio Circulation Water Exch. 1 - 13.400 64 - 285 SA 209 T1 - 1980 80.1590-01

Portugal - 3.000 ½ Mo - -

1397 56 - 425 ½ Mo - -

QUIMICAL QUIM. Lurgi Ammonia Lavradio Circulation Water Exch. 2 - 27.100 64 - 285 SA 209 T1 - 1980 80.1590-02

Portugal - 4.014 ½ Mo - -

1321 209 - 360 12 Cr Mo 9 10 - -

BASF Braun Ammonia Ludwigshafen Synthesis Warmeaustauscher "1" 1 - 90.200 216 - 340 10 Cr Mo 9 10 - 1980 80.1597-01

Germany Rod Baffles Type 9.017 12 Cr Mo 9 10 - -

1321 209 - 232 20 Mn Mo Ni 5 5 - -

BASF Braun Ammonia Ludwigshafen Synthesis Warmeaustauscher "2" 1 - 87.200 216 - 232 15 Mo 3 - 1980 80.1597-02

Germany - 9.017 15 Mo 3 - -

915 202 - 60 WStE36 - -

BASF Braun Ammonia Ludwigshafen Kreislauf-Kaltaustauscher 1 - 44.100 206 - 65 St35.8 - 1980 80.1597-03

Germany - 7.595 20 Mn 5 - -

1016 53 - 300 WStE36 Inconel 600 -

PETROCHEM. IND. CO. Uhde Ammonia Rangoon Waste Heat Boiler AA-08-E001 1 - 33.500 466 - 400 10 Cr Mo 9 10 weld overlay 1982 82.1682

Burma (Myanmar) - 6.604 10 Cr Mo 9 10 on tubesheet -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1067 49 - 264 C.S. - -

GULF PETROCH.IND. CO. Snamprogetti/Uhde Ammonia Sitra Island Waste Heat Boiler E-0801 1 - 53.800 333 - 400 SA 213 T22 - 1983 83.1705

Bahrain - 5.207 2¼ Cr 1 Mo - -

1093 118 - 325 15 Ni Cu Mo Nb 5 Inconel 600 -

NAT.FERT.CORP. Uhde Ammonia Nangal Waste Heat Boiler E-1801 1 - 33.800 246 - 480 10 Cr Mo 9 10 weld overlay 1983 83.1709

India - 3.556 12 Cr Mo 9 10 on tubesheet -

1067 228 - 290 ½ Mo - -

NAT.CHEM.FERT.CO. Toyo Ammonia Al Jubail NH3 Converter Feed Effluent Exch. 1 - 78.500 233 - 260 SA 209 T1 - 1985 85.1755-01


1575 8 - 65 C.S. - -

NAT.CHEM.FERT.CO. Toyo Ammonia Al Jubail NH3 Converter Effluent Cooler 1 - 41.000 227 - 87 SA 179 - 1985 85.1755-02


2591 11,1 FV -43 SA 516 70 - -

KEMIRA M.W.Kellogg Ammonia Hull Unitized Chiller 120-C 1 - 90.000 151,9 - 118 SA 334 6/SA 179 - 1986 86.1774-01

U.K. - 20.778 SA 350 LF2 - -

1016 152,8 - 321 1¼ Cr ½ Mo - -

KEMIRA M.W.Kellogg Ammonia Hull Converter Feed Exch. 121 C 1 - 47.000 157,1 - 280 SA 209 T1 - 1986 86.1774-02

U.K. - 11.989 - - -

1524 10,3 - 55 C.S. - -

KEMIRA M.W.Kellogg Ammonia Hull Converter Feed Cooler 120 C 1 - 54.300 151,9 - 133 SA 179 - 1986 86.1774-03

U.K. - 7.316 - - -

1220 125 - 350 15 Ni Cu Mo Nb 5 Inconel 600 -

ENFERSA Uhde Ammonia Cartagena Waste Heat Boiler 08-E001 1 - 55.000 258 - 475 10 Cr Mo 9 10 weld overlay 1987 87.1779

Spain - 10.210 12 Cr Mo 9 10 on tubesheet -

1499 35 - 343 - - -

INA PETROKEMIA M.W.Kellogg Ammonia Kutina Primary W.H.B. 101-CB 1 - 34.700 150 - 344 SA 209 T1 - 1987 87.1785

Yugoslavia - 8.459 C.S. - -

813 346 - 240 SA 336 F11A - -

EKO CHEMICAL CO. Haldor Topsoe Ammonia Tessaloniki F/P Exchanger E 750 1 - 45.000 346 - 270 SA 213 T12 - 1987 87.1797-01

Greece - 10.084 SA 336 F12 - -

1245 34,4 - 243 SA 515 60 - -

EKO CHEMICAL CO. Haldor Topsoe Ammonia Tessaloniki Waste Heat Boiler E 751 A 1 - 32.400 346,2 - 365 SA 213 T22 - 1987 87.1797-02

Greece - 6.198 SA 336 F22 - -

661 50 - 250 SA 516 60 - -

EKO CHEMICAL CO. Haldor Topsoe Ammonia Tessaloniki BFW Preheater E 751 A 1 - 10.700 346,2 - 280 SA 213 T12 - 1987 87.1797-03

Greece - 1.677 SA 336 F12 - -

813 122,5 - 330 SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Neminomisk Lateral Amm.Conver.Eff./BFW Exch. 1 - 40.300 304 - 350 SA 209 T1 - 1988 88.1800-01

U.S.S.R. 1123-C1 12.015 SA 182 F1/SA 266 4 - -

813 122,5 - 330 SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Niznij Novgorod Lateral Amm.Conver.Eff./BFW Exch. 1 - 40.300 304 - 350 SA 209 T1 - 1988 88.1800-01

U.S.S.R. 1123-C1 12.015 SA 182 F1/SA 266 4 - -

813 122,5 - 330 SA 516 70 - -


U.S.S.R. 1123-C1 12.015 SA 182 F1/SA 266 4 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

813 122,5 - 330 SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Severodvinsk Lateral Amm.Conver.Eff./BFW Exch. 1 - 40.300 304 - 350 SA 209 T1 - 1988 88.1800-01

U.S.S.R. 1123-C1 12.015 SA 182 F1/SA 266 4 - -

813 122,5 - 330 SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Neminomisk Lateral Amm.Conver.Eff./BFW Exch. 1 - 40.000 304 - 350 SA 213 T22 - 1988 88.1800-02

U.S.S.R. 1123-C2 12.015 SA 387 22 2 - -

813 122,5 - 330 SA 516 70 - -


U.S.S.R. 1123-C2 12.015 SA 387 22 2 - -

813 122,5 - 330 SA 516 70 - -


U.S.S.R. 1123-C2 12.015 SA 387 22 2 - -

813 122,5 - 330 SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Severodvinsk Lateral Amm.Conver.Eff./BFW Exch. 1 - 40.000 304 - 350 SA 213 T22 - 1988 88.1800-02

U.S.S.R. 1123-C2 12.015 SA 387 22 2 - -

1016 31 - 240 WStE355 Inconel 600 -

AGROLINZ Uhde Ammonia Linz Waste Heat Boiler 1 73 29.000 210 - 400 10 Cr Mo 9 10 weld overlay 1989 89.1863

Austria - 11.507 12 Cr Mo 9 10 on tubesheet -

813 210 - 210 20 Mn Mo Ni 4 5 - -

AGROLINZ Uhde Ammonia Linz Gas/Gas Exchanger 1 - 32.000 210 - 240 15 Mo 3 - 1989 89.1864

Austria - 12.904 20 Mn Mo Ni 4 5 - -

1093 49 - 264 WStE355 Inconel 600 -

ASEAN BINTULU FERT. Uhde Ammonia Bintulu Waste Heat Boiler 1 84 53.000 333 - 400 SA 213 T22 weld overlay 1989 89.1865

Malaysia - 11.608 12 Cr Mo 9 10 on tubesheet -

1296 140 - 340 SA 302 C Inconel 600 -

SAFERCO Uhde Ammonia Belle Plaine Waste Heat Boiler 008 E 001 1 - 60.000 214 - 490 SA 213 T22 weld overlay 1990 90.1895

Canada - 8.230 SA 336 F22 on tubesheet -

1296 140 - 340 SA 302 C Inconel 600 -

SAFERCO Uhde Ammonia Belle Plaine Waste Heat Boiler 008 E 002 1 - 58.800 214 - 470 SA 213 T22 weld overlay 1990 90.1895

Canada - 8.535 SA 336 F22 on tubesheet -

1296 206 - 120 SA 516 70 - -

SAFERCO Uhde Ammonia Belle Plaine Gas Cooler 08 E 004 1 - 237.000 8 - 70 SA 210 A1 - 1990 90.1897

Canada - 18.593 SA 285 C - -

1347 214 - 350 SA 387 11 2 - -

SAFERCO Uhde Ammonia Belle Plaine Gas/Gas Exchanger 08 E 003 1 - 153.500 214 - 366 SA 213 T11 - 1990 90.1897

Canada - 20.574 SA387-11CL2 - -

1321 39 - 61 SA 387 11 2 Refractory lined -

P.T. PUPUK SRIWIDJAJA Rekayasa/Kellogg Ammonia Palembang HP Steam Superheater 1-102 C 1 67 75.000 138 - 215 SA 213 Tp 347H - 1990 90.1901

Indonesia - 10.491 SA516-70 - -

1601 39 - 62 SA 387 11 2 Refractory lined -

P.T. PUPUK SRIWIDJAJA Rekayasa/Kellogg Ammonia Palembang Secondary Reformer W.H.B. 1-101-C 1 77 106.700 141 - 237 SA 213 T11 - 1990 90.1901

Indonesia - 8.509 SA516-70 - -

1347 16 - 65 SA 516 70 - -

P.T. PUPUK SRIWIDJAJA Rekayasa/Kellogg Ammonia Palembang Ammonia Unitized Chiller 1-120-C 1 138 184.000 185 - -33 SA 334 6/SA 179 - 1990 90.1901

Indonesia - 18.288 SA 350 LF2 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1093 184 - 375 SA 387 11 2 - -

P.T. PUPUK SRIWIDJAJA Rekayasa/Kellogg Ammonia Palembang Ammonia Converter Effl. BFH 1 - 33.500 159 - 343 SA 213 T11 - 1990 90.1901

Indonesia Preheater 1-123-C2 3.660 SA516-70 - -

1321 184 - 482 SA 336 F11 S.S. Tp 347 -

P.T. PUPUK SRIWIDJAJA Rekayasa/Kellogg Ammonia Palembang Ammonia Converter Effl. Steam Gen. 1 - 60.000 159 - 244 SA 213 T11 weld overlay 1990 90.1901

Indonesia 1-123-C1 4.725 SA 516 70 on tubesheet -

1601 184 - 300 SA 387 11 2 - -

P.T. PUPUK SRIWIDJAJA Rekayasa/Kellogg Ammonia Palembang Ammonia Converter Feed Effl. Exch. 1 - 182.000 184 - 5 SA 213 T11 - 1990 90.1904

Indonesia 1-121-C 19.508 SA387-11CL2 - -

940 35 - 250 SA 302 C Inconel 600 -

SASOL Uhde Ammonia Sasolburg Waste Heat Boiler Item 08 e 001 1 79 33.400 180 - 470 SA 213 T22 weld overlay 1991 91.1908

South Africa, Rep. of - 5.563 SA 336 F22 on tubesheet -

1448 139 - 337 20 Mn Mo Ni 4 5 Inconel 600 -

CNTIC Uhde Ammonia Puyang Waste Heat Boiler 1 - 63.000 119 - 450 10 Cr Mo 9 10 weld overlay 1991 91.1925

China, People's Rep. of - 14.885 12 Cr Mo 9 10 on tubesheet -

1550 115 - 321 20 Mn Mo Ni 4 5 - -

DALIAN CHEM.IND.CO. Uhde/Linde Ammonia Dalian Waste Heat Boiler E 0701 1 - 55.000 167 - 400 10 Cr Mo 9 10 - 1992 92.1945

China, People's Rep. of with integrated BFW-Preheating 20.016 12 Cr Mo 9 10 - -

1321 138 - 340 SA 302 C - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id Waste Heat Boiler I 08-E001 1 - 60.000 210 - 490 SA 213 T22 - 1994 94.1976

Qatar - 3.000 SA 336 F22 - -

1321 138 - 340 SA 302 C - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id Waste Heat Boiler II 08-E002 1 - 58.800 210 - 470 SA 213 T22 - 1994 94.1976

Qatar - 4.190 SA 336 F22 - -

1728 137 - 337 SA 302 B - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id BFW Heater 04-E001 1 - 69.000 40 - 480 SA 213 T11 - 1994 94.1976

Qatar - 4.623 SA 387 11 2 - -

1347 39 - 260 SA 240 Tp 321 - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id BFW Preheater 04-E002 1 - 31.500 192 - 260 SA 213 Tp 321 - 1994 94.1976

Qatar - 6.730 SA 516 70 - -

1042 210 - 65 SA 516 70 - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id Cold Exchanger 08-E005 1 - 49.000 210 - 75 SA 210 A1 - 1994 94.1976

Qatar - 6.858 SA 516 70 - -

1296 210 - 120 SA 516 70 - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id Gas Cooler 08-E004 1 - 107.000 8 - 80 SA 210 A1 - 1994 94.1976

Qatar - 18.160 SA 516 70 - -

1347 210 - 350 SA 387 11 2 - -

QAFCO Uhde/Belleli Ammonia Umm Sa'id Gas/Gas Exchanger 08-E003 1 - 148.000 210 - 366 SA 213 T11 - 1994 94.1976

Qatar - 20.498 SA387-11CL2 - -

1194 160 - 348 13 Cr Mo 4 4 DIN17175 - -

GUJARAT FERT. CO. Linde Ammonia Vadodara BFW Preheater E-502 1 - 42.500 160 - 350 13 Cr Mo 4 4 DIN17175 - 1995 95.1014-01

India - 5.284 13 Cr Mo 4 4 DIN17175 Inconel 600 -

1194 160 - 220 13 Cr Mo 4 4 DIN17175 - -

GUJARAT FERT. CO. Linde Ammonia Vadodara Hot Exchanger E-0503 1 - 81.050 160 - 250 13 Cr Mo 4 4 DIN17175 - 1995 95.1014-02

India Rod Baffles Type 19.000 13 Cr Mo 4 4 DIN17175 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1473\1400 137 - 336 20 Mn Mo Ni 4 5 - -

ABU QIR FERT. & CHEM. Uhde Ammonia Alexandria Waste Heat Boiler 308 E 001 1 - 61.000 207 - 400 10 Cr Mo 9 10 - 1996 96.1032-01

Egypt - 6.096 12 Cr Mo 9 10 - -

1270 162 - 170 SA 516 70 - -

PAKARAB Kellogg Ammonia Multan Feed Effluent H.E. 121-C 1 94 82.500 162 - 190 SA 210 A1 - 1996 96.1034

Pakistan (Tubular) 12.726 SA 516 70 - -

1423 119 - 345 SA 302 C - -

I F I Kellogg Ammonia Cobh, Co Cork Secondary W.H.B. 102-C 1 71 39.900 34 - 595 SA 199 T11 - 1997 97.1074

Ireland - 3.660 SA 387 11 1 - -

1448 142 - 344 SA 302 C - -

PETROKEMIJA Kellogg Ammonia Kutina Secondary W.H.B. 11 E 101 1 86 50.500 33,4 - 593 SA 199 T11 - 1997 97.1075

Croatia - 4.877 SA 387 11 2 - -

1448 142 - 344 SA 302 C - -

PETROKEMIJA Kellogg Ammonia Kutina Secondary W.H.B. 102-C 1 86 56.200 33,4 - 593/400 SA 199 T11 - 1997 97.1075

Croatia - 4.877 SA 387 11 2 - -

1143 162 - 382/482 SA 336 F22 3 S.S. Tp 308L -

KAWASAKI KELLOGG B&R Ammonia Hainan Ammonia Converter Effl. Steam Generator 1 94+5wo 62.100 141+FV - 343 SA 213 Tp 321 - 2001 01.1120-01

China, People's Rep. of - 7.000 SA 516 70 - -

1397 162 - 382/482 SA 387 11 2 - -

KAWASAKI KELLOGG B&R Ammonia Hainan Ammonia Converter Effl. Steam Generator 1 100 76.500 141+FV - 343 SA 213 T11 - 2001 01.1120-02

China, People's Rep. of - 5.995 SA 516-70 - -

1410 42 - 463 SA 387 11 2 - -

KAWASAKI KELLOGG B&R Ammonia Hainan HTS Effluent/BFW Steam Generator 1 28 37.000 141+FV - 343 SA 213 Tp 321 - 2001 01.1120-03


1410 42 - 350 SA 387 11 2 S.S. Tp 304L -

KAWASAKI KELLOGG B&R Ammonia Hainan HTS Effluent/BFW Preheater 1 23+3wo 34.900 141+FV - 343 SA 213 Tp 304L/SA 179 - 2001 01.1120-04


1550 37 - 480 SA 387 11 2 Inconel 600 -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh HTS Effluent Steam Generator 1 34 37.200 137 - 345 SA 213 T11 - 2002 02.1131-01

Iran - 5.000 SA 336 F11 3 - -

1550 37 - 340 SA 516 70 S.S. Tp 308 -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh HTS Effluent Steam Generator 1 28+3 34.800 137 - 345 SA 179/SA 213 Tp 304L S.S. Tp 304L 2002 02.1131-02

Iran - 5.000 SA 266 4 - -

1450 36 - 270 SA 516 70 S.S. Tp 308 -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh LTS Effluent/BFW Exchanger 2 23+3 31.800 140 - 270 SA 213 Tp 304 S.S. Tp 304L 2002 02.1131-03

Iran - 5.995 SA 266 4 - -

1350 190 - Hot 320 SA 387 11/516 70 - -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Converter Feed Effl. Exch. 1 98/105 106.900 190 - Cold 200 SA 213 T11 - 2002 02.1131-04

Iran - 19.990 SA 336 F11/266 3 - -

1200 190 - 500 SA 336 F22 S.S. Tp 308L -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Converter Effl. Steam Gen. 1 147+4.5wo 75.300 155 - 345 SA 213 Tp 321 S.S. Tp 308L 2002 02.1131-05

Iran - 5.995 SA 336 F22 - -

1250 190 - 375 SA 387 11 2 S.S. Tp 309/LOW C.S. -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Converter Effl. Steam Gen. 2 86 57.600 155 - 345 SA 213 T11 - 2002 02.1131-06

Iran - 5.000 SA 336 F11 3 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

5000 190 - -25/65 SA 516 70 - -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Unitized Chiller 1 33 310.000 190 - -25/65 SA 334 6/179 - 2002 02.1131-07

Iran - 19.990 SA 765 II - -

1423 29 - 455 SA 387 11 2 - -

PIDEC Ammonia Casale Ammonia Razi Methanator Eff. BFW Heater 2 17\26 43.800 136 - 335 SA 199 T11 - 2003 03.1141-01

Iran Rod Baffles Type 6.096 SA266 Gr.4 - -

1260 175 - 450 SA 387 22 2 - -

PIDEC Ammonia Casale Ammonia Razi Ammonia Conv./BFW Heater 1 95 69.000 136 - 335 SA 199 T22 - 2003 03.1141-02

Iran Rod Baffles Type 6.096 SA266 Gr.4 - -

1397 175 - 240 SA 387 11 2 - -

PIDEC Ammonia Casale Ammonia Razi Ammonia Converter Feed Effl. Exch. 1 93 132.000 175 - 335 SA 199 T11 - 2003 03.1141-03

Iran - 16.053 SA 387 11 2 - -

1550 37 - 480 SA 387 11 2 Inconel 600 -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh HTS Effluent Steam Generator 1 34 37.200 137 - 345 SA 213 T11 - 2004 04.1154-01

Iran - 5.000 SA 336 F11 3 - -

1550 37 - 340 SA 516 70 S.S. Tp 308 -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh HTS Effluent Steam Generator 1 28+3 34.800 137 - 345 SA 179/SA 213 Tp 304L S.S. Tp 304L 2004 04.1154-02

Iran - 5.000 SA 266 4 - -

1450 36 - 270 SA 516 70 S.S. Tp 308 -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh LTS Effluent/BFW Exchanger 2 23+3 31.800 140 - 270 SA 213 Tp 304 S.S. Tp 304L 2004 04.1154-03

Iran - 5.995 SA 266 4 - -

1350 190 - Hot 320 SA 387 11/516 70 - -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Converter Feed Effl. Exch. 1 98/105 106.900 190 - Cold 200 SA 213 T11 - 2004 04.1154-04

Iran - 19.990 SA 336 F11/266 3 - -

1200 190 - 500 SA 336 F22 S.S. Tp 308L -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Converter Effl. Steam Gen. 1 147+4.5wo 75.300 155 - 345 SA 213 Tp 321 S.S. Tp 308L 2004 04.1154-05

Iran - 5.995 SA 336 F22 - -

1250 190 - 375 SA 387 11 2 S.S. Tp 309/LOW C.S. -

IPS TOYO Kellogg Ammonia Bandar Assaluyeh Ammonia Converter Effl. Steam Gen. 2 86 57.600 155 - 345 SA 213 T11 - 2004 04.1154-06

Iran - 5.000 SA 336 F11 3 - -

5000 190 - -25/65 SA 516 70 - -

IPS Kellogg Ammonia Bandar Assaluyeh Ammonia Unitized Chiller 1 33 310.000 190 - -25/65 SA 334 6/179 - 2004 04.1154-07

Iran - 19.990 SA 765 II - -





REFERENCE LIST - AMMONIA PRESSURE VESSELS & CONVERTERS SHEET: 1 of 4


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3,190\1,120 - - 204 AMMO 58/65 - -

N.A. M.W. Kellogg Ammonia Pancevo Ammonia Converter 105-D 1 113\43 253.400 154 - 538 - - 1974 74.1265

Yugoslavia (Vertical) 22.700 SA 240 Tp 321 - -

5,000\1,650 - - - 15 Mo 3 - -

MONTEDISON Tecnimont Ammonia Ferrara Secondary Reformer R-201 1 70\40 120.000 38 - 250 - - 1974 74.1266

Italy - 10,200/10,550 - - -

1980 - - - K.C.S. - -

SHAHPUR CHEM. CO. M.W. Kellogg Ammonia Bandar-Shahpur Ammonia Separator 10-106 F 1 110 43.800 165 - -29 - - 1974 74.1273

Iran - 4.900 - - -

3,200\1,170 - - 322 AMMO 58/65 - -

N.E.T. M.W. Kellogg Ammonia Marino Point Ammonia Converter 105-D 1 168\63 383.000 239 - 538 - - 1975 75.1314

Ireland (Vertical) 22.000 SA 240 Tp 316 - -

4,270\1,220 - - 205 C.S. - -

N.E.T. M.W. Kellogg Ammonia Marino Point Secondary Reformer 103-D 1 53\36 90.000 35 - 554 - - 1975 75.1358

Ireland - 10.000 - - -

2530 - - 210 AMMO 58/65 - -

SEMADCO Foster Wheeler Ammonia Thalka Ammonia Converter R-107 1 150 230.000 270 - 530 - - 1975 75.1368

Egypt (Vertical) 20.000 - - -

4,050\1,550 - - - ½ Mo - -

N.O.C. Snamprogetti Ammonia Marsa El Brega Secondary Reformer 01-R-203 1 55\62 90.000 38 - 250 - - 1979 79.1525

Libya - 9.500 - - -

4700 - - - C.S. - -

N.O.C. Snamprogetti Ammonia Marsa El Brega L.T.C.O. Converter 01-R-205 1 70 92.000 33 - 300 - - 1979 79.1526

Libya - 5.350 - - -

2500 - - - ½ Mo - -

PAKARAB Snamprogetti Ammonia Goth Machi Sulphur Absorber R201 A/B 2 48 37.500 44 - 450 - - 1979 79.1529-01

Pakistan - 6.900 - - -

4,620\1,650 - - - ½ Mo - -

PAKARAB Snamprogetti Ammonia Goth Machi Secondary Reformer R 203 1 62\51 92.000 38 - 250 - - 1979 79.1529-02

Pakistan - 9.800 - - -

4300 - - - 1¼ Cr ½ Mo - -

PAKARAB Snamprogetti Ammonia Goth Machi High Temp. COx Converter R-204 1 57 71.000 34 - 465 - - 1979 79.1529-03

Pakistan - 5.700 - - -

4300 - - - ½ Mo - -

PAKARAB Snamprogetti Ammonia Goth Machi Low Temp. Co. Converter R-205 1 52 70.500 34 - 300 - - 1979 79.1529-04

Pakistan - 7.300 - - -

3500 - - - 1¼ Cr ½ Mo - -

PAKARAB Snamprogetti Ammonia Goth Machi Methanator R-311 1 46 38.300 30 - 465 - - 1979 79.1529-05

Pakistan - 4.700 - - -

1350 - - - 19 Mn 5 - -

QUIMIGAL QUIMICA Lurgi Ammonia Lavradio Ammonia Separator F-551 1 98 26.700 245 - -10 - - 1980 80.1588

Portugal - 4.550 - - -

2980 - - - C.S. - -

QUIMIGAL QUIMICA Lurgi Ammonia Lavradio Saturator 5301-E 1 59 139.000 57 - 250 - - 1980 80.1599-01

Portugal - 23.600 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

3,275\2,500 - - - C.S. - -

QUIMIGAL QUIMICA Lurgi Ammonia Lavradio Cooler 5302-E 1 62\48 143.000 55 - 250 - - 1980 80.1599-02

Portugal - 26.550 - - -

2500 - - - SA 302 B - -

SHERRITT GORDON MINES M.W. Kellogg Ammonia Fort Saskatchewan Ammonia Converter 105-D 1 110 342.000 152 - 343 SA 240 Tp 304 - 1981 81.1641

Canada (Horizontal) 28.650 - - -

2500 - - - TERNI CMT - -

U.C.A.M. M.W. Kellogg Cont. BV Ammonia Geleen Ammonia Converter R-3301 1 158 411.500 235 - 318 12 Cr Mo 9 10 - 1982 82.1681

The Netherlands (Horizontal) 25.020 SA 240 Tp 304 - -

2270 - - - SA 240 Tp 304 - -

SHERRITT GORDON MINES M.W. Kellogg Ammonia Fort Saskatchewan Spare Basket for Ammonia Converter 1 32 90.000 2 - 538 - - 1984 84.1740

Canada - 28.000 - - -

2400 - - - SA 302 B - -

KEMIRA M.W. Kellogg Ammonia Hull Ammonia Converter 105-D 1 110 196.000 155 - 339 - - 1986 86.1773-01

U.K. (Horizontal) 22.000 - - -

1710 - - - BS 1501-224/490A-LT50 - -

KEMIRA M.W. Kellogg Ammonia Hull Ammonia Separator 106-F 1 70 18.000 152 - 20 - - 1986 86.1773-02

U.K. - 2.550 - - -

2650 - - - 20 Mn Mo Ni 4 5 - -

ENFERSA Uhde Ammonia Cartagena Ammonia Converter 08-R001 1 147 245.000 258 - 300 - - 1987 87.1778

Spain (Vertical) 17.500 - - -

1455 - - 300 SA 336 F11 A - -

EKO CHEMICALS CO. Haldor Topsoe Ammonia Tessaloniki Ammonia Converter R751 1 175 111.000 346 - 425 SA 336 F22 - 1987 87.1796

Greece (Vertical) 11.950 - - -

2160 34 - - SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Neminomisk Molecular Sieve Drier 1109-DA/DB 2 82 42.000 111 - 330 - - 1988 88.1800

U.S.S.R. - 5.030 - - -

2160 34 - - SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Novomoskowsk Molecular Sieve Drier 1109-DA/DB 2 82 42.000 111 - 330 - - 1988 88.1800

U.S.S.R. - 5.030 - - -

2160 34 - - SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Severodoneisk Molecular Sieve Drier 1109-DA/DB 2 82 42.000 111 - 330 - - 1988 88.1800

U.S.S.R. - 5.030 - - -

2160 34 - - SA 516 70 - -

TECHMASHIMPORT Toyo Ammonia Novgorod Molecular Sieve Drier 1109-DA/DB 2 82 42.000 111 - 330 - - 1988 88.1800

U.S.S.R. - 5.030 - - -

2500 - - - 20 Mn Mo Ni 4 5 - -

NAPETCO Uhde Ammonia Marsa El Brega Ammonia Converter 07-R001 1 196 193.000 333 - 300 - - 1989 89.1828

Libya (Vertical) 12.700 - - -

2200 - - - 20 Mn Mo Ni 4 5 - -

AGROLINZ Uhde Ammonia Linz Ammonia Converter 1 105 180.000 210 - 300 - - 1989 89.1862

Austria (Vertical) 19.750 - - -

1880 - - - SA 240 Tp 304 - -

SINOPEC Haldor Topsoe Ammonia Sinopec Ammonia Converter Basket S-200 1 16 10.500 - - - - - 1990 90.1881

China, People's Rep. of (Horizontal) 16.000 - - -


Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2650 - - - SA 302 C - -

SASOL Uhde Ammonia Sasolburg Ammonia Converter 08 R 001 1 139 245.000 180 - 300 - - 1991 91.1909

South Africa, Rep. of (Vertical) 18.350 - - -

2800 - - - SA 302 B - -

PETROKEMIJA M.W. Kellogg Ammonia Gresik Ammonia Converter 105-D 1 151 470.000 185 - 282 - - 1991 91.1913

Indonesia (Horizontal) 27.000 - - -

4600 - - - SA 387 11 2 - -

QAFCO Uhde/Belleli Ammonia Umm Said H.T. Converter 04-R001 1 88 91.000 40,5 - 480 - - 1994 94.1976

Qatar - 2.950 - - -

2700 - - - SA 508 3 - -

QAFCO Uhde/Belleli Ammonia Umm Said Ammonia Converter II 08-R002 1 166 220.000 210 - 300 - - 1994 94.1976

Qatar - 12.300 - - -

3000 - - - SA 508 3 - -

QAFCO Uhde/Belleli Ammonia Umm Said Ammonia Converter I 08-R001 1 184 260.000 210 - 300 - - 1994 94.1976

Qatar - 11.350 - - -

3300 - - - SA 516 60 - -

QAFCO Uhde/Belleli Ammonia Umm Said Desulph. Reactor 01-R001 1 96 113.000 54 - 400 - - 1994 94.1976

Qatar - 11.250 - - -

1880 - - - SA 516 70 - -

QAFCO Uhde/Belleli Ammonia Umm Said Separator 08-F002 1 134 62.500 210 - 50 - - 1994 94.1976

Qatar - 6.200 - - -

4600 - - - SA 516 70 - -

QAFCO Uhde/Belleli Ammonia Umm Said L.T. Converter 04-R002 1 78 84.000 39 - 260 - - 1994 94.1976

Qatar - 4.200 - - -

2580 - - - 12 Cr Mo 9 10 - -

GUJARAT FERT. CO. Linde Ammonia Vadodara Ammonia Converter R-0501 1 109 232.000 160 - 300 - - 1995 95.1005

India - 24.300 - - -

2800 - - - 20 Mn Mo Ni 4 5 - -

ABU QIR FERT. & CHEM. Uhde Ammonia Alexandria Ammonia Converter 308 R 001 1 127 238.000 207 - 300 - - 1996 96.1032-02

Egypt - 16.900 - - -

2694 - - - W.No. 1.4301 - -

ABU QIR FERT. & CHEM. Uhde Ammonia Alexandria Ammonia Converter Basket 308 R 001-Z50 1 - 66.300 3,7 - 500 - - 1996 96.1032-03

Egypt - 15.520 - - -

1805 - - -33 TStE355 - -

ABU QIR FERT. & CHEM. Uhde Ammonia Alexandria Separator 308 F 001 1 102 45.000 207 - 50 - - 1996 96.1032-04

Egypt - 6.000 - - -

3000 - - - 20 MnMoNi 4 5 (vessel) - -

KAWASAKI KELLOGG B&R Ammonia Plant Hainan Ammonia converter with basket 1 103 400.000 162 - 285 S.S. Tp 304/321 (basket) - 2001 01.1117


2997 - - - SA 542 D 4A - -

IPM/CNCL ITC KBR Ammonia Yunnan Ammonia Converter (Shell) 1 104 290.000 163 - 285 - - 2005 05.1170-01


2692 3,2 - 325 SA 240 Tp 304 - -

IPM/CNCL ITC KBR Ammonia Yunnan Ammonia Converter (Basket) 1 35 107.000 1,75 - 535 SA 213 Tp 321 - 2005 05.1170-02



Thickness





DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

2700 - - - SA 387 GR.22 CL.2 - -

BCIC KBR Ammonia Fenchuganj Ammonia Converter (Shell) 1 142 300.100 165 - 280 - - 2012 12.1212.01

Bangladesh - 23.405 - - -

2450 3,6 - 315 SA 240 Tp 304 - -

BCIC KBR Ammonia Fenchuganj Ammonia Converter (Basket) 1 20 83.500 1,65 - 525 SA 213 Tp 321 - 2012 12.1212.02

Bangladesh - 22.015 - - -

3010 230,5 - 300 20 MnMoNi 45 EN 10028/2- -

THYSSEN KRUPP/DAELIM UHDE Ammonia Ma aden Ammonia Converter I 1 143 222.000 207,5 - 281,4 - - 2013 13.1216.01


2865 230,5 - 300 20 MnMoNi 45 EN 10028/2- -

THYSSEN KRUPP/DAELIM UHDE Ammonia Ma aden Ammonia Converter II 1 136 202.000 203,4 - 392 - - 2013 13.1216.02


3210 127 - 300 20 MnMoNi 45 EN 10028/2- -

THYSSEN KRUPP/DAELIM UHDE Ammonia Ma aden Ammonia OT Converter 1 81 202.000 110,8 - 147 - - 2013 13.1216.03


3250 170 - 285 SA 387 GR.22 CL.2 - -

YARA KBR Ammonia Peony Ammonia Converter (Shell) 1 163 553.000 153 - 225 - - 2015 15.1227.01

USA - 32.950 - - -

2950 3,9 - 315 SA 240 Tp 321 - -

YARA KBR Ammonia Peony Ammonia Converter (Basket) 1 25 140.000 2,2 - 490 - - 2015 15.1227.02

USA - 31.600 - - -


Thickness



Units: 22 large units built since 1989

•N°°°°2 Water Cooled•N°°°°1 Gas Cooled

Process: Methanol


MaximumDimensions

Materials:

Licensors:

Reactor Length: 10.500 mm (tube length)Shell Diameter: 5.470 mmN. of tubes: 6.400

Carbon SteelLow Alloy Steels300 SeriesDuplex Stainless Steel

Lurgi, Toyo, Davy Process Technology

METHANOL REACTORS

REFERENCE LIST - METHANOL EXCHANGERS & REACTORS SHEET: 1 of 3


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1118 22 - 400 ½ Mo - -

CELANESE Braun Methanol Edmonton BFW Heaters 2 56 33.400 128 - 300 SA 209 T1 - 1980 80.1591-01

Canada - 9.144 1¼ Cr ½ Mo - -

1118 22 - 250 C.S. S.S. Tp 304 -

CELANESE Braun Methanol Edmonton BFW Heaters 2 56 32.400 128 - 300 SA 213 Tp 304 - 1980 80.1591-02

Canada - 8.916 C.S. S.S. Tp 308L w.o. on TS -

1169 6 - 65 C.S. - -

CELANESE Braun Methanol Edmonton Make Up Gas 1 - 25.300 48 - 180 SA 213 Tp 304 - 1980 80.1591-03

Canada 1st Stage Intercooler 7.316 C.S. S.S. Tp 304 -

889 6 - 65 C.S. - -

CELANESE Braun Methanol Edmonton Make Up Gas 1 - 15.500 62 - 115 SA 213 Tp 304 - 1980 80.1591-04

Canada 2nd Stage Intercooler 8.535 C.S. S.S. Tp 309 w.o. -

1093 41 - 300 S.S. Tp 304 - -

CELANESE Braun Methanol Edmonton Loop Saturator Water Heaters 2 - 52.100 93 - 327 SA 213 Tp 304 - 1980 80.1591-05

Canada - 18.000 1¼ Cr ½ Mo S.S. Tp 308L w.o. on TS -

1651 6 - 65 C.S. - -

CELANESE Braun Methanol Edmonton Water Cooled Crude 1 - 85.600 93 - 100 SA 213 Tp 304 - 1980 80.1591-06

Canada Methanol Condenser 15.240 C.S. S.S. Tp 309 w.o. -

1728 93 - 146 C.S. - -

CELANESE Braun Methanol Edmonton Cold Shell Loop Exch. 1 - 105.300 93 - 170 SA 213 Tp 304 - 1980 80.1591-07

Canada Rod Baffles Type 8.535 C.S. S.S. Tp 309 w.o. -

635 93 - 270 C.S. - -

CELANESE Braun Methanol Edmonton Warm Shell Loop Exch. 2 - 19.500 93 - 300 SA 213 Tp 304 - 1980 80.1591-08

Canada Rod Baffles Type 14.326 C.S. S.S. Tp 309 w.o. -

635 93 - 270 ½ Mo - -

CELANESE Braun Methanol Edmonton Warm Shell Loop Exch. 2 - 20.200 93 - 300 SA 209 T1 - 1980 80.1591-09

Canada Rod Baffles Type 14.326 1¼ Cr ½ Mo - -

737 70 - -80 3½ Ni - -

QUIMICAL QUIM. Lurgi Methanol Lavradio Methanol/Methanol H.E. 5 - 11.300 73 - -80 SA 334 3 - 1980 80.1598

Portugal - 5.995 3½ Ni - -

1194 22 - 400 ½ Mo - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail BFW Heater 140 HE 10/12 2 - 37.000 130 - 300 SA 209 T1 - 1981 81.1673-01


1194 22 - 250 C.S. S.S. Tp 304L -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail BFW Heater 140 HE 11/13 2 - 36.300 130 - 300 SA 213 Tp 304 - 1981 81.1673-02

Saudi Arabia, Kingdom of - 9.144 C.S. S.S. Tp 308L w.o. -

1194 8 - 100 C.S. - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Make Up Gas 1 - 15.900 75 - 150 SA 213 Tp 304 - 1981 81.1673-03

Saudi Arabia, Kingdom of 1st Stage Interc. 140 HE 16 3.912 C.S. S.S. Tp 308L w.o. -

940 8 - 100 C.S. - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Make Up Gas 1 - 11.600 75 - 150 SA 213 Tp 304 - 1981 81.1673-04

Saudi Arabia, Kingdom of 2nd Stage Interc. 140 HE 17 3.912 C.S. S.S. Tp 308L w.o. -

991 113 - 120 C.S. - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Cold Shell Loop Exch.140 HE 21 1 - 25.800 113 - 327 SA 213 Tp 304 - 1981 81.1673-05








DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1220 113 - 200 C.S. - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Warm Shell Loop Exch.140 HE 22 1 - 82.300 113 - 225 SA 213 Tp 304 S.S. Tp 308L w.o. 1981 81.1673-06

Saudi Arabia, Kingdom of - 18.160 C.S. (Outlet Channel) -

1220 113 - 270 1¼ Cr ½ Mo - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Warm Shell Loop Exch.140 HE 23 1 - 85.100 113 - 327 SA 209 T1 - 1981 81.1673-07

Saudi Arabia, Kingdom of - 18.160 1¼ Cr ½ Mo/C.S. - -

991 113 FV 300 ½ Mn - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Loop Start-up Heater 140 HE 25 1 - 20.600 125 - 327 SA 209 T1 - 1981 81.1673-08


1143 41 - 300 S.S. Tp 304 - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Loop Saturator Wat.Heat.140 HE 26 1 - 45.000 113 - 327 SA 213 Tp 304 - 1981 81.1673-09

Saudi Arabia, Kingdom of - 11.710 1¼ Cr ½ Mo S.S. Tp 308L w.o. on TS -

1143 41 - 300 S.S. Tp 304 - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Loop Saturator Wat.Heat.140 HE 27 1 - 45.000 113 - 327 SA 213 Tp 304 - 1981 81.1673-10

Saudi Arabia, Kingdom of - 11.710 1¼ Cr ½ Mo S.S. Tp 308L w.o. on TS -

1245 8 - 100 C.S. - -

NAT. METHANOL CO. C.F. Braun Methanol Al Jubail Crude Methanol Condens.140 HE 28 1 - 42.400 113 - 140 SA 213 Tp 304 - 1981 81.1673-11


4700 - - - SA 302 B - -

S.P.L.A.J. NAPETCO Uhde Methanol Marsa El Brega Methanol Converter 74 R-01 1 95 178.000 70 - 360 - - 1981 81.1675

Libya - 6.260 - - -

3099 88 - 330 SA 516 70 - -

T.&T. METHANOL CO. Toyo Methanol Point Lisas MRF Reactor M-DC-402 1 66 103.000 39 - 251 SA 209 T1A - 1989 89.1834

Trinidad and Tobago (Tubular) 8.306 SA 302 B - -

4318 51 - 265 BS 1501-621B - -

STATOIL Fluor Daniel Methanol Tjeldbergodden Methanol Synt.Reactors 30V1304 A/B 2 72 243.000 94 - 280 SA 789 S31500 S.S. Tp 347 w.o. 1994 94.1987

Norway (Tubular) 7.240 BS 1503-621B on tubesheet -

2515 94 - 250 WStE355 DIN17102 1.4828 SEW 470 -

STATOIL Fluor Daniel Methanol Tjeldbergodden Interchanger 30 H 1303 1 - 191.000 94 - 280 1.4541 DIN17440 1.4550 DIN17440 1994 94.1987

Norway - 13.208 WStE355 DIN17102 1.4541 DIN17440 -

2196 - - - 15 Mo 3 DIN17155 - -

STATOIL Fluor Methanol Tjeldbergodden Steam Drum 52 V 1303 1 52 45.900 51 - 266 - - 1994 94.1987

Norway - 11.300 - - -

3988 50 - 265 20 Mn Mo Ni 4 5 - -

K.M.I. Lurgi Methanol Kaltim Methanol Reactor R201 A/B 2 43\65 167.200 89 - 275 X2 Cr Ni Mo Si 19 5 1.4550 DIN17440 1995 95.1011

Indonesia (Tubular) 7.240 20 Mn Mo Ni 4 5 - -

4496 50 - 265 SA 533 B 1 - -

PIDM Lurgi Methanol Khang Island Methanol Reactor R4001 A/B 2 68\92 248.000 89 - 275 SA 789 S31500 S.S. Tp 347 w.o. 1996 96.1028-01

Iran (Tubular) 7.240 SA 508 3 on tubesheet -

1474 6,9 - 170 SA 516 70 - -

AMPCO Raytheon Methanol Bioko Methanol Water Cooler E-404 4 12 63.500 120 - 230 SA 213 Tp 304 - 1998 98.1079

Equatorial Guinea - 6.096 SA 516 70 S.S. Tp 304 -

4522 - - - SA 387 11 2 - -

AMPCO RAYTHEON Methanol Bioko Methanol Converter 1 183\94 437.253 120,7 - 343 - - 1998 98.1080

Equatorial Guinea - 15.470 - - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

4496 55 - 280 SA 387 22 2 - -

ATLAS LURGI Methanol Couva Water cooled methanol reactor 2 80 315.000 88 - 280 SA 789 S31500 - 2001 01.1122-01

Trinidad (Tubular) 8.000 SA 387 22 2 - -

5461 88 - 300 SA 387 22 2 - -

ATLAS LURGI Methanol Couva Gas cooled methanol reactor 1 155 468.000 88 - 270 SA 213 Tp 321 - 2001 01.1122-02

Trinidad (Tubular) 10.491 SA 387 22 2 - -

5461 88 - 300 SA 387 22 2 - -

ZAGROS PETR. COMIANT LURGI Methanol Bandar Assaluyeh Gas cooled methanol reactor 1 155 468.000 88 - 270 SA 213 Tp 321 - 2002 02.1134

Iran (Tubular) 10.491 SA 387 22 2 - -

4496 55 - 280 SA 387 22 2 - -

ZAGROS PETR. COMIANT LURGI Methanol Bandar Assaluyeh Water cooled methanol reactor 2 80 315.000 88 - 280 SA 769 S31500 - 2002 02.1135

Iran (Tubular) 8.000 SA 387 22 2 - -

4500 55 - 280 SA 387 22 2 - -

ZAGROS PETR. COMIANT LURGI Methanol Bandar Assaluyeh Water cooled methanol reactor 2 80 330.000 88 - 280 SA 789 S31500 - 2004 04.1160-01

Iran (Tubular) 8.000 SA 387 22 2 - -

5470 88 - 300 SA 387 22 2 - -

ZAGROS PETR. COMIANT LURGI Methanol Bandar Assaluyeh Gas cooled methanol reactor 1 155 463.000 88 - 270 SA 213 Tp 321 - 2004 04.1160-03

Iran (Tubular) 10.500 SA 387 22 2 - -

5100 50 - 265 SA 387 11 2 - -

*** LURGI Methanol Hainan Water cooled methanol reactor 1 84 475.000 110 - 289 SA 789 S31500 - 2004 04.1162

China, People's Rep. of (Tubular) 10.000 SA 336 11 3 - -

4050 95 - 300 SA 387 11 2 - -

CWEME LURGI Methanol Datang Gas cooled methanol reactor 1 125 410.000 95 - 270 SA 213 Tp 321 - 2006 06.1179

China, People's Rep. of (Tubular) 97.000 SA 240 Tp 321 - -





Period: From 1970 to 2006

(Italian/European/USA Plants)

• Steam Generators (completion)• Heat Exchangers• Pressure Vessels & Pumps Casing• Main containment & Air Locks• Primary Piping (Prototype)• R&D with Prototypes USA APS Steam Generator Superphenix NA-Air Exchanger

Superphenix NA Internal Containment Italian Plant - Main Steel Containment

NUCLEAR EQUIPMENT

REFERENCE LIST - POWER & NUCLEAR EQUIPMENT SHEET: 1 of 8


DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1220 16 - 420 ½ Mo - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater AP5 4 - 34.000 335 - 224 16 Mo 5 UNI5462 - 1970 70.411A/70.412A

Italy - 10.110 Fe510-1KW UNI7660 - -

1220 30 - 505 1 Cr ½ Mo - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater AP6 4 - 33.600 335 - 255 16 Mo 5 UNI5462 - 1970 70.411B/70.412B

Italy - 8.738 Fe510-1KW UNI7660 - -

1220 51 - 375 C.S. - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater AP7 4 - 41.500 335 - 286 16 Mo 5 UNI5462 - 1970 70.411C/70.412C

Italy - 10.313 Fe510-1KW UNI7660 - -

1220 97 - 460 ½ Mo - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater AP8 4 - 53.000 335 - 329 Boron Steel - 1970 70.411D/70.412D

Italy - 10.592 Fe510-1KW UNI7660 - -

1220 16 - 420 ½ Mo - -

ENEL Belleli Power plant 320 MWS.Filippo del Mela BFW Heater AP5 4 - 34.000 335 - 224 16 Mo 5 UNI5462 - 1970 70.413A/71.1041A

Italy - 10.110 Fe510-1KW UNI7660 - -

1220 30 - 505 1 Cr ½ Mo - -

ENEL Belleli Power plant 320 MWS.Filippo del Mela BFW Heater AP6 4 - 33.600 335 - 255 16 Mo 5 UNI5462 - 1970 70.413B/71.1041B

Italy - 8.738 Fe510-1KW UNI7660 - -

1220 51 - 375 C.S. - -

ENEL Belleli Power plant 320 MWS.Filippo del Mela BFW Heater AP7 4 - 41.500 335 - 286 16 Mo 5 UNI5462 - 1970 70.413C/71.1041C

Italy - 10.313 Fe510-1KW UNI7660 - -

1220 97 - 460 ½ Mo - -

ENEL Belleli Power plant 320 MWS.Filippo del Mela BFW Heater AP8 4 - 53.000 335 - 329 Boron Steel - 1970 70.413D/71.1041D

Italy - 10.592 Fe510-1KW UNI7660 - -

1220 16 - 420 ½ Mo - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP5 4 - 34.000 335 - 224 16 Mo 5 UNI5462 - 1971 71.1039A/1040A

Italy - 10.110 Fe510-1KW UNI7660 - -

1220 30 - 505 1 Cr ½ Mo - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP6 4 - 33.600 335 - 255 16 Mo 5 UNI5462 - 1971 71.1039B/1040B

Italy - 8.738 Fe510-1KW UNI7660 - -

1220 51 - 375 C.S. - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP7 4 - 41.500 335 - 286 16 Mo 5 UNI5462 - 1971 71.1039C/1040C

Italy - 10.313 Fe510-1KW UNI7660 - -

1220 97 - 460 ½ Mo - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP8 4 - 53.000 335 - 329 Boron Steel - 1971 71.1039D/1040D

Italy - 10.592 Fe510-1KW UNI7660 - -

1630 - - - MARREL AM 60 S.S. Tp 316L -

MONTEDISON Breda Power Plant Brindisi Steam Drum 1 82 45.000 156 - 345 - - 1971 71.1093

Italy - 10.500 - - -

1540 - - - MARREL AM 60 S.S. Tp 316L -

TERMOSUD Breda Power Plant Tirso Steam Drums 2 80 45.000 140 - 338 - - 1971 71.1108

Italy - 10.500 - - -

1225 - - - MARREL AM 56 - -

STANIC Breda Power Plant Livorno Drums 2 82 41.000 97 - 333 - - 1973 73.1184

Italy - 6.080 - - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1296 54 - 375 C.S. - -

ENEL Belleli Power plant 320 MWPriolo Gargallo BFW Heater AP6 4 - 37.800 294 - 298 16 Mo 5 UNI5462 - 1974 74.1298-02-05

Italy - 12.015 Fe510-1KW UNI7660 - -

1296 95 - 455 ½ Mo - -

ENEL Belleli Power plant 320 MWPriolo Gargallo BFW Heater AP7 4 - 42.000 294 - 326 16 Mo 5 UNI5462 - 1974 74.1298-03-06

Italy - 11.000 Fe510-1KW UNI7660 - -

1601 25 - 252 C.S. - -

WEIR Weir Power plant Vales Point BFW Heater HP 2 - 36.000 246 - 252 16 Mo 5 UNI5462 - 1975 75.1345

Australia - 9.703 Fe510-1KW UNI7660 - -

1067 296 - 200 C Mn Mo Ni - -

*** Alsthom Power plant Belfort HP Hot Gas/Gas Exchanger 1 - 41.000 296 - 230 SA 209 T1 - 1975 75.1347-01

France - 8.154 C Mn Mo Ni - -

1067 160 - 343 C Mn Mo Ni - -

*** Alsthom Power plant Belfort HP BFW Preheater 1 - 27.500 35 - 450 SA 209 T1 - 1975 75.1347-02

France - 3.150 C Mn Mo Ni - -

1804 23 - 405 C.S. - 75.1360-01-04

ENEL Belleli Power plant 660 MWTorrevaldaliga Nord BFW Heater AP4 8 - 74.200 380 - 239 Boron Steel - 1975 75.1348-01-04

Italy - 12.800 Fe510-1KW UNI7660 - -

1855 58 - 290 C.S. - 75.1360-02-05


Italy - 12.065 Fe510-1KW UNI7660 - -

1855 95 - 350 C.S. - 75.1360-03-06


Italy - 10.516 Fe510-1KW UNI7660 - -

991 20 - 450 15 Mo 3 - -

*** Cass Power plant Frimmersdorf HP BFW Heater 1 - 23.000 350 - 265 15 Mo 3 - 1978 78.1467-01

Germany - 9.017 15 Mo 3 - -

1042 50 - 366 15 Mo 3 - -

*** Cass Power plant Frimmersdorf HP BFW Heater 1 - 28.000 350 - 265 15 Mo 3 - 1978 78.1467-02

Germany - 10.491 15 Mo 3 - -

- - - 650 S.S. Tp 316LN - -

SOCALTRA LEVIVIER Novatome Nuclear Power plant Creys Malville Sodium-Air Heat Exchanger 4 - - - - 540 - - 1979 79.1512

France [ASME Code Case N-47] - - - -

966 40 - 371 ½ Mo - -

EDF Lummus Power plant Montereau HP BFW Heater 2 - 23.000 170 - 254 SA 179 - 1979 79.1517

France - 8.433 Fe510-1KW UNI7660 - -

1347 23 - 465 ½ Mo - -

AMN Belleli Power plant Cassano d'Adda BFW Heater AP5 2 - 69.000 295 - 241 SA 179 - 1979 79.1558-01

Italy - 14.000 Mn C.S. - -

1321 50 - 375 ½ Mo - -


Italy - 14.000 Mn C.S. - -

1372 95 - 455 ½ Mo - -


Italy - 14.000 Mn C.S. - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

800 - - - 15MDV 4.05 - -

PUBLIC POWER CORP. Stein Industrie Power Plant Aghios Dimitrios Separators 2 80\65 49.300 212 - 370 AMMO 52 - 1980 80.1605

Greece - 29.550 - - -

800 - - - 15MDV 4.05 - -

E.D.F. Stein Industrie Power Plant Cordemais Separator 1 80\72 41.700 214 - 424 AMMO 52 - 1980 80.1606

France - 22.850 - - -

1550 31 - 450 L.A.S.\C.S. - -

EDF Delas Weir Power plant Gardanne BFW Heater HP5 2 - 52.000 330 - 210 SA 179 - 1981 81.1653-01

France - 8.840 C.S. - -

1550 48 - 320 C.S. - -

EDF Delas Weir Power plant Gardanne BFW Heater HP6 2 - 64.000 330 - 243 SA 179 - 1981 81.1653-02

France - 8.586 C.S. - -

1220 27 - 295 C.S. - -

ENEL Belleli Power plant 320 MWTorrevaldaliga Sud BFW Heater AP6 2 - 64.600 299 - 371 16 Mo 5 UNI5462 - 1981 81.1665

Italy - 10.008 High tens. st. - -

- - - - - - -

NIRA CNEN 3\5.8\19.4MW Test CircuitPEC-Brasimone Sodium-Air Heat Exchanger 3 - - - - - - - 1982 82.1679

Italy [ASME Code Case N-47] - - - -

1245 16 - 412 C.S. - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater AP5 4 - 35.100 331 - 224 16 Mo 5 UNI5462 - 1983 83.1714-01-05

Italy - 10.897 Fe510-1KW UNI7660 - -

1245 30 - 505 1 Cr ½ Mo\C.S. - -


Italy - 8.916 Fe510-1KW UNI7660 - -

1245 51 - 375 C.S. - -


Italy - 10.364 Fe510-1KW UNI7660 - -

1245 96 - 460 C.S. - -


Italy - 8.610 Fe510-1KW UNI7660 - -

1499 4 FV 152 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater BP1 2 - 31.900 40 - 152 C 18 UNI5462 - 1983 83.1715

Italy - 12.269 Fe460-1KW UNI5869 - -

1347 4 FV 215 Fe410-1KW UNI5869 - -


Italy - 8.280 Fe460-1KW UNI5869 - -

1347 4 FV 270 Fe410-1KW UNI5869 - -


Italy - 7.265 Fe460-1KW UNI5869 - -

- - - - - - -

NIRA CNEN 3\5.8\19.4MW Test CircuitPEC-Brasimone Sodium-Air Heat Exchanger 3 - - - - - - - 1983 83.1717

Italy [ASME Code Case N-47] - - - -

1093 27 - 480 ½ Mo\C.S. - -

ENEL Belleli Power plant 320 MWTorrevaldaliga Sud BFW Heater AP5 1 - 25.000 326 - 250 16 Mo 5 UNI5462 - 1983 83.1720-01

Italy - 7.670 Fe510-1KW UNI7660 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1347 27 - 515 1 Cr ½ Mo\C.S. - -

ENEL Belleli Power plant 320 MWTorrevaldaliga Sud BFW Heater AP6 1 - 32.000 291 - 250 16 Mo 5 UNI5462 - 1983 83.1720-02

Italy - 7.214 Fe510-1KW UNI7660 - -

1245 16 - 412 C.S. - -

ENEL Belleli Power plant 320 MWPiombino BFW Heater AP5 1 - 35.100 331 - 204/224 16 Mo 5 UNI5462 - 1984 84.1738

Italy - 10.897 Fe510-1KW UNI7660 - -

1372 16 - 410 ½ Mo\C.S. - -

ENEL Belleli Power plant 320 MWVado Ligure BFW Heater AP5 8 - 30.600 335 - 204/224 16 Mo 5 UNI5462 - 1984 84.1741

Italy - 7.697 Fe510-1KW UNI7660 - -

1499 4 FV 152 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWBrindisi Sud LP BFW Heater BA 001 A/B 4 - 32.800 40 - 152 C 18 UNI5462 - 1984 84.1744

Italy - 13.285 Fe410-1KW UNI5869 - -

1474 4 FV 170 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWBrindisi Sud LP BFW Heater BA 002 A/B 4 - 24.900 40 - 152 C 18 UNI5462 - 1984 84.1744

Italy - 11.938 Fe410-1KW UNI5869 - -

1702 23 - 450 ½ Mo - -

ENEL Belleli Power plant 660 MWBrindisi Sud BFW Heater AP4 4 - 75.800 380 - 245 Boron Steel - 1984 84.1745-01-04

Italy - 11.684 Fe510-1KW UNI7660 - -

1626 58 - 335 C.S. - -


Italy - 10.364 Fe510-1KW UNI7660 - -

1651 95 - 400 C.S. - -


Italy - 8.890 Fe510-1KW UNI7660 - -

1270 16 - 412/204 C.S. - 86.1767-05

ENEL Belleli Power plant 320 MWFiume Santo BFW Heater AP5 4 - 35.300 331 - 224 16 Mo 5 UNI5462 - 1986 86.1767-01

Italy - 10.922 Fe510-1KW UNI7660 - -

1245 30 - 505/235 14 Cr Mo 3 - 86.1767-06


Italy - 8.916 Fe510-1KW UNI7660 - -

1245 51 - 375/266 C.S. - 86.1767-07


Italy - 10.364 Fe510-1KW UNI7660 - -

1245 96 - 460/309 C.S. - 86.1767-08


Italy - 8.610 Fe510-1KW UNI7660 - -

1575 4 FV 152 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 320 MWFiume Santo BFW Heater BP1 2 - 38.500 40 - 152 C 18 UNI5462 - 1986 86.1768

Italy - 12.700 Fe460-1KW UNI5869 - -

1245 4 FV 215 Fe410-1KW UNI5869 - -


Italy - 9.398 Fe460-1KW UNI5869 - -

1499 4 FV 270 Fe410-1KW UNI5869 - -


Italy - 7.925 Fe460-1KW UNI5869 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1651 10 - 380/180 C.S. - -

CNTIC G.I.E./Delas Weir Power plant Da Gang HP BFW Heater B-007 2 - 42.800 265 - 200 - - 1986 86.1772-01


1677 21 - 480/220 C.S.\1Cr ½ Mo - -

CNTIC G.I.E./Delas Weir Power plant Da Gang HP BFW Heater B-008 2 - 49.100 265 - 240 SA 179 - 1986 86.1772-02


1728 44 - 360/260 C.S. - -



1778 93 - 460/310 C.S.\1Cr ½ Mo - -



1270 16 - 412 C.S. - -

ENEL Belleli Power plant 320 MWS.Filippo del Mela BFW Heater AP5 2 - 35.500 331 - 204/224 16 Mo 5 UNI5462 - 1987 87.1783

Italy - 10.922 Fe510-1KW UNI7660 - -

1372 29,4 - 505 SA 387 11 2 - -

ENEL Belleli Power plant 320 MWVado Ligure BFW Heaters AP6 A/B 4 - 35.500 328,5 - 255 16 Mo 5 UNI5462 - 1987 87.1788

Italy - 6.325 19 Mn 5 DIN17155 - -

1499 4 FV 152 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWGioia Tauro LP BFW Heaters BA 001 A/B 4 - 32.800 40 - 152 C 18 UNI5462 - 1988 88.1820

Italy - 13.285 Fe410-1KW UNI5869 - -

1474 4 FV 170 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWGioia Tauro LP BFW Heaters BA 002 A/B 4 - 24.900 40 - 152 C 18 UNI5462 - 1988 88.1820

Italy - 11.938 Fe410-1KW UNI5869 - -

1702 23 - 450 ½ Mo - -

ENEL Belleli Power plant 660 MWGioia Tauro BFW Heaters AP4 4 - 75.800 380 - 245 Boron Steel - 1988 88.1820

Italy - 11.684 Fe510-1KW UNI7660 - -

1626 58 - 335 ½ Mo - -


Italy - 10.364 Fe510-1KW UNI7660 - -

1651 95 - 400 ½ Mo - -


Italy - 8.890 Fe510-1KW UNI7660 - -

1702 23 - 450 ½ Mo - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP4 4 - 75.800 380 - 245 Boron Steel - 1988 88.1820-04A

Italy - 11.684 Fe510-1KW UNI7660 - -

1626 58 - 335 ½ Mo - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP5 4 - 81.400 380 - 295 Boron Steel - 1988 88.1820-04B

Italy - 10.364 Fe510-1KW UNI7660 - -

1651 95 - 400 ½ Mo - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heater AP6 4 - 93.800 380 - 326 Boron Steel - 1988 88.1820-04C

Italy - 8.890 Fe510-1KW UNI7660 - -

1499 50 - 425 BS 1501-161/430 - -

C.E.G.B. Weir Westgarth Power plant West Thurrock HP BFW Heaters 12 - 40.000 86 - 287 BS 3606-440/ESI 23.4 - 1989 89.1860

U.K. - 9.805 BS 1501-161/430 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1499 4 FV 152 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWMontalto di Castro LP BFW Heaters BA 001 A/B 8 - 32.800 40 - 152 C 18 UNI5462 - 1990 90.1879

Italy - 13.285 Fe410-1KW UNI5869 - -

1474 4 FV 170 Fe410-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWMontalto di Castro LP BFW Heaters BA 002 A/B 8 - 24.900 40 - 152 C 18 UNI5462 - 1990 90.1879

Italy - 11.938 Fe410-1KW UNI5869 - -

1702 23 - 450 ½ Mo - -

ENEL Belleli Power plant 660 MWMontalto di Castro BFW Heaters AP4 8 - 75.800 380 - 245 Boron Steel - 1990 90.1879

Italy - 11.684 Fe510-1KW UNI7660 - -

1626 58 - 335 ½ Mo - -


Italy - 10.364 Fe510-1KW UNI7660 - -

1651 95 - 400 ½ Mo - -


Italy - 8.890 Fe510-1KW UNI7660 - -

2007 26,3 FV 343 BS 1501-161/430B - -

CEGB Weir Westgarth Power plant Drax HP BFW Heater (no.7) 3 - 90.000 220 FV 254 ESI STD 23.4 Gr 440 - 1990 90.1888

U.K. - 10.033 BS 1503-221/430 - -

2083 3 FV 144 WStE355 - -

E.E.A. Belleli Power plant 330 MWCairo West BFW Heater LP1/LP2 Duplex 2 - 41.400 30 - 144 1.4541 DIN17440 - 1990 90.1899-01

Egypt - 9.983 WStE355 DIN17102 - -

1143 5 FV 277 WStE355 - -

E.E.A. Belleli Power plant 330 MWCairo West BFW Heater LP3 2 - 12.050 30 - 159 1.4541 DIN17440 - 1990 90.1899-03

Egypt - 9.094 WStE355 DIN17102 - -

1220 7 FV 299 WStE355 - -

E.E.A. Belleli Power plant 330 MWCairo West BFW Heater LP4 2 - 17.500 30 - 171 1.4541 DIN17440 - 1990 90.1899-04

Egypt - 9.398 WStE355 DIN17102 - -

1601 30 - 494/236 13 Cr Mo 4 4/WStE355 - -

E.E.A. Belleli Power plant 330 MWCairo West BFW Heater HP A6 2 - 37.600 300 - 256 15 Mo 3 DIN17175 - 1990 90.1899-06

Egypt - 8.484 15 Ni Cu Mo Nb 5 - -

1626 56,9 - 373/272 13 Cr Mo 4 4/WStE355 - -

E.E.A. Belleli Power plant 330 MWCairo West BFW Heater HP A7 2 - 48.200 300 - 292 15 Mo 3 DIN17175 - 1990 90.1899-07

Egypt - 9.195 15 Ni Cu Mo Nb 5 - -

1347 50 FV 375 Fe510-1KW UNI5869 - -

ENEL Belleli Power plant 320 MWVado Ligure BFW Heaters AP7 A/B 4 - 43.200 329 - 286 16 Mo 5 UNI5462 - 1991 91.1906

Italy - 16.155 Fe510-1KW UNI7660 - -

1905 23 - 450 Fe510-1KW UNI5869 - -

ENEL Belleli Power plant 660 MWTorrevaldaliga Nord BFW Heaters AP4 A/B 2 - 76.300 380 - 245 16 Mo 5 UNI5462 - 1991 91.1912

Italy - 11.710 SA182F1 - -

1270 16 - 412 Fe510-1KW UNI5869 - -

ENEL Belleli Power plant 320 MWTermini Imerese BFW Heaters AP5 A/B 2 - 31.900 331 - 224 16 Mo 5 UNI5462 - 1991 91.1923

Italy - 10.922 Fe510-1KW UNI7660 - -

1804 23 - 405 ½ Mo - -

ENEL Belleli Power plant 660 MWTorrevaldaliga Nord BFW Heaters AP4 A/B 2 - 70.300 380 - 239 16 Mo 5 UNI5462 - 1991 91.1929

Italy - 12.800 Fe510-1KW UNI7660 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1372 3,5 FV 148 SA 516 70 - -

E.E.A. Ansaldo/GIE Power plant 300 MWAssiut BFW Heater LP1 1 - 26.100 39 - 120 SA 556 B2 - 1992 92.1937

Egypt - 11.176 SA 516 70 - -

1397 3,5 FV 267 SA 516 70 - -


Egypt - 9.068 SA 516 70 - -

1397 3,5 FV 220 SA 516 70 - -


Egypt - 5.944 SA 516 70 - -

1347 6 - 316 SA 516 70 - -


Egypt - 6.706 SA 516 70 - -

1575 22 - 460/260 SA 516 70 - -

E.E.A. Ansaldo/GIE Power plant 300 MWAssiut BFW Heater HP6 1 - 42.400 272 - 270 16 Mo 5 UNI5462 - 1992 92.1937

Egypt - 5.588 SA 266 2 - -

1575 47,5 - 365/260 SA 516 70 - -

E.E.A. Ansaldo/GIE Power plant 300 MWAssiut BFW Heater HP7 1 - 66.200 272 - 270 16 Mo 5 UNI5462 - 1992 92.1937

Egypt - 10.720 SA 266 2 - -

889 3 FV 150 WStE355 - -

E.E.A. Belleli Power plant 33 MW Al-Arish BFW Heater LP1 2 - 6.850 20 - 150 1.4541 DIN17457 - 1993 93.1959-02

Egypt - 4.877 WStE355 DIN17102 - -

839 3 FV 150 WStE355 - -

E.E.A. Belleli Power plant 33 MW Al-Arish BFW Heater LP2 2 - 5.600 20 - 150 1.4541 DIN17457 - 1993 93.1959-03

Egypt - 4.496 WStE355 DIN17102 - -

1016 20 FV 350/220 13 Cr Mo 4 4 DIN17175 - -

E.E.A. Belleli Power plant 33 MW Al-Arish BFW Heater HP1 2 - 10.600 160 - 250 15 Mo 3 DIN17175 - 1993 93.1959-04

Egypt - 4.190 15 Ni Cu Mo Nb 5 - -

991 40 - 440/275 13 Cr Mo 4 4 DIN17175 - -

E.E.A. Belleli Power plant 33 MW Al-Arish BFW Heater HP2 2 - 10.900 160 - 275 15 Mo 3 DIN17175 - 1993 93.1959-05

Egypt - 3.100 15 Ni Cu Mo Nb 5 - -

1524 25 - 480/250 SA 204 B\SA 516 70 - -

HUB POWER COMPANY LTD. Belleli Power plant 320 MWHub-River BFW Heater HP6 4 - 34.000 246 - 270 SA 556 2 - 1993 93.1966-01

Pakistan 1-2-3-4 LAD 10A-C001 9.195 SA 299 - -

1524 54 - 385 SA 204 B - -

HUB POWER COMPANY LTD. Belleli Power plant 320 MWHub-River BFW Heater HP7 4 - 43.500 246 - 270 SA 556 C2 - 1993 93.1966-02

Pakistan 1-2-3-4 LAD 20A-C001 9.500 SA 299 - -

2007 10,5 - 55 SA 515 70 - -

P.L.N. Belleli Power plant 600 MWSuralaya Aux. Cooling Water Exchanger 6 - 27.000 3 - 55 SB 338 2 - 1994 94.1975

Indonesia - 13.716 SA 515 70 rubber lined -

1169 40 FV 510 SA 387 11 2 - -

ENEL Belleli Power plant 320 MWBrindisi Sud BFW Heaters AP6 A/B 4 - 31.400 299 - 255 16 Mo 5 UNI5462mod - 1994 94.1978

Italy - 6.400 SA516-70 - -

1220 94 FV 450 SA 387 11 2 - -

ENEL Belleli Power plant 320 MWBrindisi Sud BFW Heaters AP8 A/B 2 - 41.500 299 - 306 16 Mo 5 UNI5462mod - 1994 94.1978

Italy - 8.052 SA516-70 - -







DESIGN CONDITIONS


[mm] [Kg.] [Bar] [°C]

1296 13 - 410 SA 516 70 - -

ENEL Belleli Power plant 320 MWTorrevaldaliga Sud BFW Heaters AP5 A/B 2 - 31.500 295 - 215 16 Mo 5 UNI5462mod - 1994 94.1985

Italy - 10.540 Fe510-1KW UNI7660 - -

1270 3,9 FV 270 SA 515 60 - -

ENEL Belleli Power plant 320 MWFusina BFW Heaters BP3 Gr.3-4 2 - 17.200 39 - 172 SA 249 Tp 304L - 1994 94.1998

Italy - 10.059 SA 516 70 - -

1448 50 FV 405 SA 204 B - -

ENEL Belleli Power plant 175 MWMonfalcone BFW Heater AP1 1 - 27.700 215,7 - 285 16 Mo 5 UNI5462mod - 1994 94.1999

Italy - 10.110 Fe510-1KW UNI7660 - -

1321 16,7 - 445 SA 204 B - -

ASM BS/AGSM VR Belleli Power plant Ponti sul Mincio BFW Heater AP4 1 - 24.300 232,4 - 230 15 Mo 3 UNI5462 - 1996 96.1042

Italy - 14.580 SA 266 2 - -

5893 - - - SA 533 B 1 - -

ARIZONA PUBLIC SERVICE Ansaldo Camozzi Nuclear Power plant Palo Verde Steam Generator (Final Assembly) 4 148 730.000 - - - - - 2003 03.1143

USA - - - - -

5893 - - - SA 533 B 1 - -

ANSALDO CAMOZZI Ansaldo Camozzi Nuclear Power plant Palo Verde Steam Generator (Final Assembly) 2 148 730.000 - - - - - 2006 06.1178

USA - - - - -

42672 493 - 399 SA387Gr11CL2 Inconel 625 -

GENERAL ELECTRIC/DUKE GENERAL ELECTRIC Coal Gasification Indiana Radiant Syngas Cooler 2 83 678.500 - - - SB407 UNS8800 (Incoloy 800 H)- 2007 07.1187

USA - 4.474 - - -

2930 32 - 240 13 Cr Mo 45 - -

EDF ALSTOM Nuclear Power plant Flamanville H.P. Heat Exchangers 4 40 178.000 140 - 260 X2 Cr Ti 18 - 2007 07.1189

France - 14.311 18 Mn Mo Ni 55 SS 308 L -





Documents

BELLELI COMPANY [modalit · PDF file3810 - - - BS 1503-622 Enhanced S.S. Tp 347 w.o. - ESSO Davy McKee Residfiner Fawley Residfiner Lead Reactor R-101 1 235+4.5 630.000 216 - 448 -