vacuum distillation unit (u-74) - Ecommerce News

VACUUM DISTILLATION UNIT (U-74)

DEEP CONVERSION PROJECT PUERTO LA

CRUZ REFINERY

EARLY START UP

ENERO 2019

I-CP-P-GE-PR-19-0193

CP-GI-PR-11-0067 REV. 1 06 / AÑO 2

VACUUM DISTILLATION UNIT (U-74)

CONTENT

OBJECTIVE

SCOPE OF WORK

PROCESS BASIS

PRELIMINAR VOLUMETRIC BALANCE

AVAILABILITY OF UTILITIES IN RPLC.

REQUIRED INTERCONNECTIONS FOR PROCESS & OFFSITES

REQUIRED INTERCONNECTIONS FOR OFFSITES

COST ESTIMATION


CP-GI-PR-11-0067 REV. 1 06 / AÑO 3

OBJECTIVE

To present the interconnections proposed for Process /

utilities / offsites and associated items required to Start

up VDU unit prior to HDHPLUS® construction (early

start up)

Atmosferic residues from DA-1 & 2 (Mesa 30 and Merey

16 respectively) will be processed in VDU in order to

obtain, as final products: reconstituted crude oil

(RECON~16°API), Fuel oil and asphalt in order to

maximize the RPLC profits.

OBJETIVO


CP-GI-PR-11-0067 REV. 1 06 / AÑO 4

SCOPE OF WORK

To develop engineering, procurement and construction necessary to

construct, precommission and start-up the total facilities required for

the early start-up of VDU. Such facilities includes, but not limited to:

1) Interconnections (between RPLC existing facilities – VDU) for all

necessary utilities / process / offsites required for VDU operation.

2) Revamp of tanks (where required) for handling new products.

3) Heat exchangers train for cooling down the products.

4) All instrumentation & associated accessories.

5) New Truck loading system for asfalt handling.

6) Evaluation of existing pumps and New pumps for asphalt handling.

7) Additional facilities for oily water / fresh water system to supply VDU

requirements.


CP-GI-PR-11-0067 REV. 1 06 / AÑO 5

VDU Design Capacity = 2 identical trains with 65620 BSPD each.

TURNDOWN = 50% (32810 BSPD)

Early operation Capacity = 2 trains operating at 38918.3 BSPD c/u.

FEEDSTOCK:

DA-1 at 80000 BSPD = AR 22112.6 BPD from Mesa 30

DA-2 at 70000 BSPD = AR 55724 BPD from Merey 16

BASIS OF PROCESS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 6

DA-2

DA-1 VDU

IHVGO

MEREY 16

MESA 30

LVGO

HVGO

VDU

II

LVGO

HVGO

VR to

HDHPLUS

VR VR to

HDHPLUS

LVGO

VR

VR to

Storage

LVGO to

SHP

2840.6 BPD

12028.5 BPD

24067.8 BPD

5681.2 BPD

24057 BPD

48135.6 BPD

77836.6 BPD

2840.6 BPD

12028.5 BPD

24067.8 BPD

38918.3 BPD

38918.3 BPD

22112.6 BPD

55724 BPD

80000 BPD

70000 BPD

PRELIMINAR VOLUMETRIC BALANCE

RECON TO

SELL

FUEL OIL

ASFALTO


CP-GI-PR-11-0067 REV. 1 06 / AÑO 7

PRELIMINAR VDU PRODUCTS PROPERTIES

PROPERTIES UNIT LVGO HVGO VR

Temperature °F 110 157,6 397,7

Pressure psig 210 60 60

Total Mass Rate LB/HR 36920,80 165383,83 368643,41

Total Molar Rate LB-MOL/HR 155,06 460,74 560,20

Liquid Std Rate (vol) FT3/HR 664,54 2813,96 5630,43

Liquid Std Rate (vol) BPSD 2840,62 12028,49 24067,76

Liquid Act. Density LB/FT3 54,60 56,83 59,37

Liquid Viscosity CP 3,29 12,17 103,34

Stream Phase Liquid Liquid Liquid

TBP at 760 MM HG (LV) °F

IBP 412,20 585,66 908,26

5% 470,09 640,63 947,46

10% 497,92 672,60 973,69

30% 554,11 749,50 1062,88

50% 590,93 809,48 1141,63

70% 626,72 863,56 1314,63

90% 676,76 918,87 1627,19

95% 700,00 938,00 1752,65

EBP 743,37 964,45 1866,54

Total Crit. Pressure (Kay's Rule) psia 278,93 213,14 157,39

Total Molecular Weight 238,11 358,96 658,05

Total Enthalpy MM BTU/HR 1,04 7,54 58,15

Liquid Std Rate (vol) gal/min 82,85 350,83 701,98

Total Std. API 27,34 18,65 3,29

Liquid Std. Sp. Gr. 0,89 0,94 1,05


CP-GI-PR-11-0067 REV. 1 06 / AÑO 8

AVAILABILITY OF UTILITES FROM RPLC

UtilityRequirement (1)

Normal~MaxDesign Normal Operation

Current Production /

Consumption RPLC Availability

Current Production /

Consumption

RPLC + VDU

Availability Post VDU CONCLUSIONS

Sanitary water 20 gpm = 4,5 m3/h 109,04 m3/h (2) 93,60 m3/h (2) 46,13 m3/h (2) (10) + 62,91 m3/h 50,63 m3/h + 58,41 m3/h It does NOT require additional facility

Storm water 4760 gpm = 1081 m3/hRPLC philosophy for handling storm

water from plants to be confirmed

Oily Water 10 gpm = 2,27 m3/h 385 m3/h 385 m3/h ~ 500m3/h 385 m3/h ~ 500m3/h - 115 m3/h - 502,27 m3/h - 117,27 m3/hNo Availability -

additional facilities shall be required

Instrument Air

Plant Air

Total

33 MSCFH

5 MSCFH

33 MSCFH ~ 38 MSCFH

483,3 MSCFH (3) 435 MSCFH (3) -308,6 MSCFH (3) + 126,4 MSCFH (3) - 346,6 MSCFH + 88,4 MSCFH RPLC Recovery Plan for Utilities Shall

be implemented

Steam

HP (0 ~ -108) Klb/h

MP (+6 ~ -32) Kllb/h

MLP (+16 ~ +67) Klb/h

430 Klb/h (3) 379 Klb/h (3) -300 Klb/h (3) + 79 Klb/h (3) - 408 Klb/h - 29 Klb/hRPLC Recovery Plan for Utilities Shall

be implemented

Total Water (7) (431 ~ 1224) gpm 6000 gpm (3) 6000 gpm (3) - 5200 gpm (3) + 800 gpm (3) - 6424 gpm - 424 gpmNo Availability -

additional facilities shall be required

(*) Boiler Feed Water (3 ~ 364) gpm 1000 gpm (3) 1000 gpm (3) -750 gpm (3) + 250 gpm (3) - 1084 gpm - 84 gpm

Currently No availability -

RPLC Recovery Plant for Utilities Shall

be implemented ( Capacity will

increase)

Fuel Gas & Natural Gas 0,002 ~ 7,1 MMSCFD 80 MMFCSD (3) (4) 70 MMFCSD (3) - 48 MMFCSD (3) + 32 MMFCSD (3) + 55,1 MMFCSD + 24,9 MMSCFD It does NOT require additional facility

Condensate 6,2 Klb/h = 12,4 gpm 200 gpm (5) 90 gpm (5) 90 gpm (5) + 110 gpm + 122,4 gpm + 122,4 gpm It does NOT require additional facility

Nitrogen 3,2 ~ 5500 SCFH (6) 57250 SCFH 54190 SCFH - 12273 SCFH (8) + 44997 SCFH - 17773 SCFH + 39477 SCFH It does NOT require additional facility

RPLC VDU - Requirement

1) RPLC Recovery Plan (by others) shall be implemented in order to have

availability of utilities for VDU early start-up

2) For Oily water and fresh water systems – additional facilities are required and

to be included under VDU early start up scope of work.


CP-GI-PR-11-0067 REV. 1 06 / AÑO 9

• INTERCONNECTIONS REQUIRED FOR

PROCESS AND OFFSITES AREAS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 10

Feed – Atmospheric Residue System

ATMOSPHERIC RESIDUE


CP-GI-PR-11-0067 REV. 1 06 / AÑO 11

Current Design (Deep Conversion Project Scenario) :

The System receives and stores Long Residue from DA-1, DA-2 y DA-3 Units. DA-1/DA-2

Long Residue is stored in the existing tank TK-130x2 and fed to VDU-1 and VDU-2. DA-3 Long

Residue is stored in existing tank TK-130x3 and fed to VDU-2.

Conceptual Scheme (simplified) for Long Residue System (Deep Conversion Project Scenario)

ATMOSPHERIC RESIDUE


CP-GI-PR-11-0067 REV. 1 06 / AÑO 12

Proposal of Interconnections for Early start up: Feed VDU from an Offsite Tank Conceptual Scheme for this option (Tank TK-250x5):

ATMOSPHERIC RESIDUE


CP-GI-PR-11-0067 REV. 1 06 / AÑO 13

Routes of pipes in Plot Plan

ATMOSPHERIC RESIDUE


CP-GI-PR-11-0067 REV. 1 06 / AÑO 14

Remarks:

-Hydraulic evaluations must be performed in order to sizing the line.

-Availability of space for new pipe routing must be evaluated.

-New interconnection line must be designed taking into account the future

facilities/connections required for Deep Conversion Project.

-Although tanks TK-250x1/2/4/5 are currently connected to residual suction header is

required to evaluate the piping arrangement for this operation in order to isolate of

other systems. These pumps are already proposed to pump fuel oil produced during

this early stage therefore, interconnections must be designed allowing these two

operations (feed VDU and send fuel oil to jetties).

ATMOSPHERIC RESIDUE


CP-GI-PR-11-0067 REV. 1 06 / AÑO 15

Reconstituted Crude Oil

(RECON ~ 16 °API)

RECONSTITUTED CRUDE OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 16

Proposal: To Use tanks TK-250x3 and 250x6

Conceptual Scheme for this option:



CP-GI-PR-11-0067 REV. 1 06 / AÑO 17

Route in Plot Plan



CP-GI-PR-11-0067 REV. 1 06 / AÑO 18

Remarks:

- Hydraulic evaluations are required.

- Availability of space for routing of pipes must be confirmed.

- Cooling system is considered same as for Fuel Oil (E-9801).

- Proposed pumps for this option are OSAMCO pumps (existing). Minors

maintenance & repairing works shall be included as part of this Scope Of Work.



CP-GI-PR-11-0067 REV. 1 06 / AÑO 19

Fuel Oil

FUEL OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 20

Fuel Oil

Current Design:

Bunker Fuel and Fuel Oil System consist of four (4) existing storage tanks TK-250x3/4/5/6

and one (1) product tank TK-260x5 located at Guaraguao Marine Terminal.

This blend is produced by mixing of the following components:

• Long Residue from DA-1/2 (TK-130X2) (NNF).

• Long Residue form DA-3 (TK-130X3) (NNF).

• Short Residue from VDU-2 and from tanks TK-250x1 and TK-150x18.

• FCC Catalytic Oils (Mixture of Slurry, LCO, HCO) (TK-56x10).

• HHGO from HDH Unit.

• LVGO from VDU-1/2.

• SR Diesel from DA-1/2 and tank TK-150X1.

• ML Diesel from tanks TK-80X3/6/7.

• Heavy Slop Oil from tanks TK-25x2/3/5.

• AGO from tanks TK-56x4/5.

• Neutralized ASO from Alkylation Unit (T-6 Tower).

• HVGO from tanks TK-150x2 and TK-150x18.

• DA-3 SR Diesel from TK-20x8/9.

• Recovered Heavy HC from MRU (E-5808A/B).

Once all components are mixed, the product is fed to a new Bunker Fuel Cooler E-9801

A/F due to temperature limitations for Bunker Fuel truck loading operation and tanks.

FUEL OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 21

Conceptual (simplified) scheme for current design

FUEL OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 22

Proposal of interconnection for early start up of VDU: Fuel Oil can be stored in existing

atmospheric residual tanks TK-250x1/2/4.

Conceptual Scheme:

FUEL OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 23

Route of pipes in Plot Plan

FUEL OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 24

Remarks:

-Interconnections for FCC Catalytic Oil, ASO and spent caustic shall be included in this scope

-Facilities for cooling (heat exchangers system) should be same as for RECON, Asphalt case

(E-9801, included in HPC scope of work).

FUEL OIL


CP-GI-PR-11-0067 REV. 1 06 / AÑO 25

Asphalt

Asphalt Production


CP-GI-PR-11-0067 REV. 1 06 / AÑO 26

TK-

120x1

Jetty # 6

Asphalt from CRP

P-1/2/3

Current Operation of RPLC

Asphalt from CRP is discharged from marine tanker to tank TK-120x1 and dispatched

by trucks with existing P-1/2/3 pumps.

In jetty # 6 is available a hose for connection to marine tanker.

Asphalt Production

Asphalt to

local market


CP-GI-PR-11-0067 REV. 1 06 / AÑO 27

Deep Conversion Project Design:

Asphalt Production

This is part of HPC scope of work


CP-GI-PR-11-0067 REV. 1 06 / AÑO 28

Asphalt:

Asphalt will be produced by mixing of Short Residue and HVGO. This Asphalt

production will be stored in existing tank TK-120x1 located in El Chaure area.

Interconnections required:

Will be required an interconnection from VDU B.L to TK-120x1 header.

Conceptual Scheme

Asphalt Production


CP-GI-PR-11-0067 REV. 1 06 / AÑO 29

Route of piping in plot plan This is part of HPC scope

Asphalt Production


CP-GI-PR-11-0067 REV. 1 06 / AÑO 30

New facilities / Utilities required for this option:

- To revamp an existing tank for asphalt storage.

- The cooling system for asphalt should be the same cooling system for fuel oil

considered in the HPC scope.

- Additional consumption of steam for tracing or electrical tracing for lines and

asphalt tank will be required.

- Two (2) new pumps to send Asphalt to trucks.

- New truck loading facilities in RPLC side.

Asphalt Production


CP-GI-PR-11-0067 REV. 1 06 / AÑO 31

Send asphalt to jetty providing a new pump

VDU

Train 1

T

T

Asphalt

VDU

Train 2 TK-???

T

E-9801 New pump and New truck

Loading facilities

To be provided in this

early stage

Asphalt truck

Will be loaded in

RPLC

To El Chaure Area

Asphalt truck

Located in the El Chaure to

Local Market

Existing tank

in RPLC

Asphalt Production


TK-

150x2

(HPC Scope)

To

CP-GI-PR-11-0067 REV. 1 06 / AÑO 32

Slops

SLOPS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 33

SLOP

In the future (Deep Conversion Project scenario), slop coming from VDU will be stored in new tanks

25x1/2/3/4/5. However, these tanks are not available for early star up of VDU.

Heavy slop produced in VDU is feed AR Tank TK-250x5 for reprocessing.

Conceptual Scheme:

SLOPS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 34

Route of pipes in Plot Plan:

SLOPS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 35

For Light Slop this must be sent to existing slop tank TK-10x4

Conceptual Scheme:

SLOPS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 36

For Light Slop this must be sent to existing slop tank TK-10x4

Route of pipes in Plot Plan:

SLOPS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 37

Light Flushing

LIGHT FLUSHING


CP-GI-PR-11-0067 REV. 1 06 / AÑO 38

Current Design for Deep Conversion Project

SR Diesel from DA-1/DA-2 and LVGO from VDU-1/VDU-2 are stored in the existing tanks TK-130x4 and TK-150x1

and is supplied to intermittent users via Light Flushing Oil Pumps, G-9837 A/B and Light Flushing Oil Header as

Light Flushing Oil. One pump is kept running with an automatic pump spillback flow controller so the Light Flushing

Oil can be supplied upon consumer’s request at any time. An emergency power failure, a back up is provided to the

new Light Flushing Oil Pump, G-9837A/B.

Conceptual Scheme:

LIGHT FLUSHING

CP-GI-PR-11-0067 REV. 1 06 / AÑO 39

Interconnections Required: From G-2802 A/B Discharge line.

One option is interconnect the discharge of pump G-2802 A/B (HDT Feed pump from TK-130x4) with VDU

flushing header however is required take into account that upset with U-45 feeding must be avoided.

Conceptual Scheme:

LIGHT FLUSHING


CP-GI-PR-11-0067 REV. 1 06 / AÑO 40

Route of pipes in plot plan:

LIGHT FLUSHING


CP-GI-PR-11-0067 REV. 1 06 / AÑO 41

Remarks:

-Site survey is required

-Availability of space for pipe routes must be confirmed.

-Flow required for VDU flushing in this early start up must be confirmed

-Hydraulic evaluation is required in order to confirm if G-2802 A/B have enough

capacity for send flushing required for VDU in early start up.

LIGHT FLUSHING


CP-GI-PR-11-0067 REV. 1 06 / AÑO 42

Relief loads

RELIEF LOADS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 43

Proposal for Existing Flare Interconnection.

Once the total load received by the Heads of U-71, including the load of VDU and the E.W-01.1, the total

amount of relief is 1,425,753 lb / hr. details the design loads for each unit.

RELIEF LOAD SUMMARY OF SINGLE GENERAL FAILURE

Unit No.

Imported

Power

Failure

Self-

generated

Power Failure

Cooling

Water

Failure

Steam

Failure (1)

Fire

(in Each

Area)

lb/hr lb/hr lb/hr lb/hr lb/hr

U-03 569.620 30.206

DA-1 388.000

U-19 291.586 202.962

U-20 287.602 97.085 97.085 554.868

U-45 696.565 847.643

U-71 1.463

U-72 3.944

EW-01.1 169116(2)

U-74 (3) 150.000

TOTAL 1.425.753 957.620 97.085 97.085

GROUND

FLARE

DESIGN

LOAD

1,562,446 lb/hr

Notes:

(1) Steam failure case is same as Cooling Water case because Cooling Water

Circulation Pump (G-6501B) driven by steam turbine will stop.

(2) D-2811/12 with 67.343 lb/hr and D-2813 with 101.773 lb/hr

(3) Both trains

RELIEF LOADS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 44

Proposal: Interconnection to the Head of 24 "of diameter of Low Pressure: The proposal considers the relief

of the entire design load of VDU (150 klb / hr) towards the available connection facilities located in Av. H and

located in the areas of the battery limit of Unit 20 (CCR Platforming).

Routing:

RELIEF LOADS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 45

Tanks

TANKS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 46

Preliminar options for existing tanks to be considered for early start up of Vacuum Distillation Unit

VDU (U-74).

Belong is shown a summary of the tanks that should be used in the early start up of U-74 Vacuum Distillation

Unit.

Note: Evaluation of existing tanks to be used as asphalt tanks (2) is pending

TANKS


Steam /

(Quality)

Current Early S. Up Early S. Up Current Early S. Up

250X3 Crude Oil Syn. Crude Y (SM) Y 200 397


250X5 Residual Asmospherical Residue NO Y 200 200

250X1 Residual Fuel Oil NO Y 200 200



150X2 Residual Asphalt Y (SM) Y 200 200


TAGService

Current

Operative

? (Y/N)

Design Temperature

CP-GI-PR-11-0067 REV. 1 06 / AÑO 47

Summary of Lines Required

Interconnections and Utilities required

for VDU Early Star-up


CP-GI-PR-11-0067 REV. 1 06 / AÑO 48

Summary of Lines for Process & Offsites interconnections:

(1): Hydraulic evaluations are required in order to determine final size of lines

(2): Measured on plot plan considering the longest possible route

(3): Asphalt line is based on HPC case.

(m) (ft)

1 Atmospheric Residue (Feed) 16 3CB1S01 ST1.5 561,00 1.840,55 62,58

2 Synthetic Crude Oil 10 3CB1S01 STM2.0 555,00 1.820,87 40,48

3 Fuel Oil 10 3SH1S89 STM2.5 966,00 3.169,29 40,48

4 Asphalt 10 3CB1S01 STM2.0 3.244,00 10.643,04 40,48

5 Slop 10 3SH1S89 STM2.5 0,00 0,00 40,48

6 Light Flushing Oil 4 1CB1S01 640,00 2.099,74 10,79

7 Reliefs 42 1CB1S01 612,00 2.007,87 221,61

Weight

(lbs/ft)Item Service Size (inches)

(1) ClassLenght

(2)




CP-GI-PR-11-0067 REV. 1 06 / AÑO 49

• INTERCONNECTIONS REQUIRED FOR

UTILITIES


CP-GI-PR-11-0067 REV. 1 06 / AÑO 50

Summary of Lines for utilites interconnections:

(1): Hydraulic evaluations are required in

order to determine final size of lines

(2): Measured on plot plan considering the

longest possible route



Ite

m Services

Diameter

(inch) Class

Lenght

(m) (ft)

1 Fuel Gas 6" 1CB1S01 295 968

2 Natural Gas 2" 1CB1S01 295 968

3 HP Steam 8" 6CB1S02 281 922

4 MP Steam 10" 3CB1S02 281 922

5 MLP Steam 30" 1CB1S02 281 922

6 Instrument Air 3" 1CG1T01 264 866

7 Plant Air 3" 1CB1S01 264 866

8 Nitrogen 3" 1CB1S01 83 272

9 Boiler Feed Water 6" 6CB1S02 281 922

10 Drinking Water 2" 1CG1T01 193 633

11 Service Water 2" 1CS1S95 193 633

12 Condensate 4" 1CB1S02 281 922

13 Deaerated Water 2" 1CB1S02 281 922

14 Oily Water 3" 1CB2S01 142 466

15 Oily Storm Water 16" 1CB2S01 142 466

16 Sour Water 6" 3CH2S82L 300 984

17 Sanitary Water 3" 1CS2S95 357 1171


CP-GI-PR-11-0067 REV. 1 06 / AÑO 51

• UTILITIES DEEP CONVERTION PROJECT

• EXISTING UTILITIES PLOT PLAN

• HP STEAM

• MP STEAM

• MLP STEAM

• CONDENSATE

• INSTRUMENT AIR

• PLANT AIR

• NITROGEN

• FUEL GAS

• NATURAL GAS

• BOILER FEED WATER (BFW)

• SERVICE WATER

• DRINK WATER

• SANITARY WATER

• STORM/FIRE

• SOUR & OILY WATER

• BATTERY LIMIT

CONTENT


CP-GI-PR-11-0067 REV. 1 06 / AÑO 52

EXISTING UTILITIES PLOT PLANT

UTILITIES

AREA

NITROGEN

SYSTEM U-

94 BL VDU / COOLING TOWER

CP-GI-PR-11-0067 REV. 1 06 / AÑO 53

HP STEAM


CP-GI-PR-11-0067 REV. 1 06 / AÑO 54

MP STEAM (Option 1)


CP-GI-PR-11-0067 REV. 1 06 / AÑO 55

MP STEAM (Option 2)


CP-GI-PR-11-0067 REV. 1 06 / AÑO 56

MLP STEAM


CP-GI-PR-11-0067 REV. 1 06 / AÑO 57

INSTRUMENT AIR

INSTRUMENT AIR


CP-GI-PR-11-0067 REV. 1 06 / AÑO 58

PLANT

AIR

PLANT AIR


CP-GI-PR-11-0067 REV. 1 06 / AÑO 59

NITROGEN

NITROGEN


CP-GI-PR-11-0067 REV. 1 06 / AÑO 60

FUEL GAS

FUEL GAS

FUEL GAS SYSTEM

(U-72)


CP-GI-PR-11-0067 REV. 1 06 / AÑO 61

NATURAL GAS

NATURAL GAS


CP-GI-PR-11-0067 REV. 1 06 / AÑO 62

BFW

BOILER FEED WATER


CP-GI-PR-11-0067 REV. 1 06 / AÑO 63

(U-62)

CONDENSATE

RECOVERY

UNIT

CONDENSAT

E

CONDENSATE


CP-GI-PR-11-0067 REV. 1 06 / AÑO 64

SERVICE WATER



CP-GI-PR-11-0067 REV. 1 06 / AÑO 65

DRINKING WATER


CP-GI-PR-11-0067 REV. 1 06 / AÑO 66

SANITARY WATER


CP-GI-PR-11-0067 REV. 1 06 / AÑO 67

STORM/FIRE

I-C-P-GE-PR-19-0193

CP-GI-PR-11-0067 REV. 1 06 / AÑO 68

SOUR & OILY WATER

SOUR WATER

OILY WATER

TREATMENT

PACKAGE # 1

TREATMENT

PACKAGE # 2

STEP PLANT

I-C-P-GE-PR-19-0193

CP-GI-PR-11-0067 REV. 1 06 / AÑO 69

TREATED OILY AND SOUR WATER QUALITY

THE QUALITY OF TREATED WATER FROM TREATMENT

PACKAGE # 1 AND # 2 TO STEP PLANT ARE THE FOLLOWING:

I-C-P-GE-PR-19-0193

CP-GI-PR-11-0067 REV. 1 06 / AÑO 70

BATTERY LIMIT


CP-GI-PR-11-0067 REV. 1 06 / AÑO 71

BATTERY LIMIT

Interconnections between B.L VDU & B.L Valcor


CP-GI-PR-11-0067 REV. 1 06 / AÑO 72

SOW SUMMARY

To Develop EPC (Engineering, Procurement and Construction)

Basic Engineering and Detailed Engineering for VDU Interconections based

on Conceptual Engineering proposed by PDVSA.

Procurement and Construction of all equipment and facilities required.

CP-GI-PR-11-0067 REV. 1 06 / AÑO 73

SOW SUMMARY

Items to be procured:

- New heat exchanger system E-9801

- New pump and new truck loading facilities for asphalt dipatch in RPLC

(Guaraguao) area.

- New Pump to send Asphalt to Jetties

- New Treatment Package for Oily Water

- New Treatment Package for Sour Water

- New Chlorine Package for Cooling Tower U-91C

CP-GI-PR-11-0067 REV. 1 06 / AÑO 74

UNIDAD DE DESTILACIÓN AL VACIO (U-74)


CP-GI-PR-11-0067 REV. 1 06 / AÑO 75

(m) (ft)

1 Atmospheric Residue (Feed) 16 3CB1S01 ST1.5 561,00 1.840,55 62,58

2 Synthetic Crude Oil 10 3CB1S01 STM2.0 555,00 1.820,87 40,48

3 Fuel Oil 10 3SH1S89 STM2.5 966,00 3.169,29 40,48

4 Asphalt 10 3CB1S01 STM2.0 3.244,00 10.643,04 40,48

5 Slop 10 3SH1S89 STM2.5 0,00 0,00 40,48

6 Light Flushing Oil 4 1CB1S01 640,00 2.099,74 10,79

7 Reliefs 42 1CB1S01 612,00 2.007,87 221,61

Weight

(lbs/ft)Item Service Size (inches)

(1) ClassLenght

(2)

Process Lines Utilities Lines

Steam /

(Quality)

Current Early S. Up Early S. Up Current Early S. Up



250X5 Residual Asmospherical Residue NO Y 200 200




150X2 Residual Asphalt Y (SM) Y 200 200


TAGService

Current

Operative

? (Y/N)

Design Temperature

Tanks

• 24 Interconnections are required.

• 7 for process lines including reliefs

• 17 for utilities lines

• 8 tanks are required for VDU early start up

Interconnections / Tanks required

Items to be procured:

• New heat exchanger system E-9801

• New pump and new truck loading facilities for

asphalt dipatch in RPLC (Guaraguao) area.

• New Pump to send Asphalt to Jetties

• New Treatment Package for Oily Water

• New Treatment Package for Sour Water

• New Chlorine Package for Cooling Tower U-91C

Documents

vacuum distillation unit (u-74) - Ecommerce News