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8/14/2019 Giammatteo Online NMR EAS 2007
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More From the Barrel
On-Line NMR Increases Diesel Production
and Quality (Part I)
Paul J. Giammatteo
Process NMR Associates, LLCNMR Process Systems, LLC
87A Sand Pit Road
Danbury, CT 06810
203-744-5905
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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On-line, high resolution nuclear magnetic resonance spectroscopy
(NMR) made its introduction into refinery processes twelve yearsago with installation of two units into Texacos Los Angeles arearefinery. From then to now, integration of the proper NMR hardwarewith the properly designed applications have proven economicallyand operationally beneficial. Whether the on-line NMR application
serves as a preferred multi-parameter analyzer, or, integrated intoadvanced process control and optimization, the accuracy, reliability,and performance of on-line NMR delivers true value throughout therefining process.
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Refinery Applications
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Advantages and Disadvantages of NMR Applied to Process
Advantages:Non-Optical Spectroscopy
No Spectral Temperature Dependence
Minimal Sampling Requirements
Spectral Response to Sample Chemistry is Linear
Chemical Regions of NMR Spectra are Orthogonal
Entire Volume is Sampled by the RF Experiment
Water is in Distinct Region and can be digitally removed
Detailed Hydrocarbon information is readily observed.
Fundamental Chemical Information Can be Derived Directly from Spectrum.
Colored/Black Samples Readily Observed
Disadvantages:
Solids Cannot be Observed
Individual Molecular Component Sensitivity Not Observed Directly in the Spectrum.
Low Sensitivity to Impurities Quantitative > 1000 ppm.
Sensitive to Ferro-magnetics.
Sample Viscosity Causes Resolution ChangesNon-Hydrogen Containing Species are Not Observed
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
NMR - What a differenceone letter can make!!
.2
.4
.6
.8
1
10000 9000 8000 7000 6000 5000 4000
NIRTypical Variability Observed in
Gasoline Blending
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8 7 6 5 4 3 2 1 0 -10
.5
1
1.5
2
2.5
3 CH
RR
HH
R
H
R
H
R
H
H
R
CH2
CH3
CH3
CH3CH-C= and
57 M Hz
Aromatic Olefinic Water OxygenateMethyl
AromaticAliphatic
Hydrocarbon Picture
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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ASTM ASTM Engineering
Method Used Reproducibility UnitsGasoline Blending RON D 2699 0.4 Octane
Gasoline Blending MON D 2700 0.4 Octane
Gasoline Blending T10 D 86 9.50 Degrees F
Gasoline Blending T50 D 86 13.00 Degrees F
Gasoline Blending T90 D 86 13.50 Degrees F
Gasoline Blending EBP D 86 13.50 Degrees FGasoline Blending Aromatics detailed GC 1.1 Volume %
Gasoline Blending Benzene D 3606 0.5 Volume %
Gasoline Blending RVP - information only
Diesel Blending API D 4052 1 Degree
Diesel Blending IBP D 86 14 Degrees FDiesel Blending T10 D 86 14 Degrees F
Diesel Blending T50 D 86 14 Degrees F
Diesel Blending T90 D 86 14 Degrees F
Diesel Blending EBP D 86 14 Degrees F
Diesel Blending Viscosity D 445 - informational data only
Diesel Blending Cloud Point D 5773 7 Degrees CDiesel Blending Cetane Index D 976 - D 4737 2 Index Number
Diesel Blending Pour Point D 97 6 Deg C
Parameter Description
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Aramco
BASF
Petrochina
High Resolution Process NMR Installations
ORL
PNA
Aramco
BASF
Petrochina
High Resolution Process NMR Installations
ORL
PNA
Aramco
BASF
Petrochina
High Resolution Process NMR Installations
ORL
PNA
High Resolution Process NMR Installations
PNA
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AtmosphericTower
VacuumTower
Coker
FCCU*
Hydrocracker
Desalter
HTU
HTU
HTU
HTU
ReformerAromatics
Extraction
GasPlant
Polymerization
Alkylation
LPG
Gasoline
Aromatics
Kerosene
Distillates
Lubricant Oils
Asphalt
Coke
VGO
Gas
Lt Naphtha
Hv Naphtha
Kerosene
AGO
Crude
Residue
Olefins
i-C4
Reformate
FCC Gasoline
Naphtha
Motor Alkylate
Gasoline StreamsKerosene/AvJet
Distillate Streams
*or Resid Cracker
HeavyOil
Upgrading
Unit
Current Commercial
NMR Units
Blend
Head
AtmosphericTower
VacuumTower
Coker
FCCU*
Hydrocracker
Desalter
HTU
HTU
HTU
HTU
ReformerAromatics
Extraction
GasPlant
Polymerization
Alkylation
LPG
Gasoline
Aromatics
Kerosene
Distillates
Lubricant Oils
Asphalt
Coke
VGO
Gas
Lt Naphtha
Hv Naphtha
Kerosene
AGO
Crude
Residue
Olefins
i-C4
Reformate
FCC Gasoline
Naphtha
Motor Alkylate
Gasoline StreamsKerosene/AvJet
Distillate Streams
*or Resid Cracker
HeavyOil
Upgrading
Unit
Current Commercial
NMR Units
Blend
Head
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Effective feedstock management can save up to70 cents/barrel for refineries.
.modern analytical tools contribute significantlyto this .
Hydrocarbon Processing,
September 1998
In 1998 crude was less than $30/barrel.
What about $100+?
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
NMR NeSSI: Never expect Small Sample Input!
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Crude Unit Overview
Distillation (D86, Sim Dis, TBP)
Flash Point
Cloud Point
Pour Point
Freeze Point
Chemistry (Fa, Fn, Fp,Naphthalene)
PONA/PIONA
API Gravity/Density
Octane/Cetane
APC and OptimizationNaphtha
Kero
Diesel
AGO
Crude
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
0
5
10
15
20
10 8 6 4 2 0
NMR Spectra ShowingSpectral Variability of 6 Crudes
ppm
CH
CH2
CH3CH3
CH3
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Actual Crude TBP Curves
0
10
20
30
40
50
60
70
80
90
100
30 130 230 330
Temperature (C)
C
um
ulative
W
eightLoss
(W
t%
)
KuwaitMarib Light
Nemba
GOS Mix
DulangBacho
Actual Crude TBP Curves
0
10
20
30
40
50
60
70
80
90
100
30 130 230 330
Temperature (C)
C
um
ulative
W
eightLoss
(W
t%
)
KuwaitMarib Light
Nemba
GOS Mix
DulangBacho
NMR Predicted TBP Curves for Crudes
0
10
20
30
40
50
60
70
80
90
100
30 130 230 330
Temperature (C)
C
um
ulativ
e
W
eightLoss(W
t%
)
NMR Predicted TBP Curves for Crudes
0
10
20
30
40
50
60
70
80
90
100
30 130 230 330
Temperature (C)
C
um
ulativ
e
W
eightLoss(W
t%
)
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Marib Light Crude TBP Curves
(Actual and NMR Predicted)
0
10
20
30
40
50
60
70
80
90
100
30 130 230 330
Temperature (C)
Cum
ulative
W
eightLoss
(W
t%
)
Actual
Predicted
Marib Light Crude TBP Curves
(Actual and NMR Predicted)
0
10
20
30
40
50
60
70
80
90
100
30 130 230 330
Temperature (C)
Cum
ulative
W
eightLoss
(W
t%
)
Actual
Predicted
Dulang Crude TBP Curves
(Actual and NMR Predicted)
0
10
20
30
40
50
60
70
80
90
100
30 80 130 180 230 280 330 380
Temperature (C)
Cum
ulative
W
eightLoss
(W
t%
)
Actual
Predicted
Dulang Crude TBP Curves
(Actual and NMR Predicted)
0
10
20
30
40
50
60
70
80
90
100
30 80 130 180 230 280 330 380
Temperature (C)
Cum
ulative
W
eightLoss
(W
t%
)
Actual
Predicted
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Crude Feed API D 4052 1 DegreeCrude Feed Sulfur D 2622 - D 4294 - Weight % information only
Crude Feed TBP wt% 38 C D 2892 2.2 Weight %
Crude Feed TBP wt% 105 C D 2892 2.2 Weight %
Crude Feed TBP wt% 165 C D 2892 2.2 Weight %
Crude Feed TBP wt% 365 C D 2892 2.2 Weight %
Crude Feed TBP wt% 565 C D 2892 2.2 Weight %
FCC Feed API D 4052 1 Degree
FCC Feed Viscosity D 2161 - information only
FCC Feed IBP D 2887 42 Degrees F
FCC Feed T10 D 2887 12 Degrees F
FCC Feed T50 D 2887 12 Degrees F
FCC Feed T90 D 2887 12 Degrees F
FCC Feed EBP D 2887 25 Degrees FFCC Feed Sulfur D 2622 - D 4294 - Weight % information only
FCC Feed Carbon Aromaticity D 5292 2 mole %
FCC Feed Carbon Naphthenicity - mole % internal proprietary
FCC Feed Carbon Parafinicity - mole % internal proprietary
CDU AGO API D 4052 1 Degree
CDU AGO T10 D 2887 12 Degrees FCDU AGO T50 D 2887 12 Degrees F
CDU AGO T90 D 2887 12 Degrees F
CDU AGO Sulfur D 2622 - D 4294 - Weight % information only
Method Used
Reproduc
ibility UnitsParameter Description
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Real Time Crude Assays On-Line Analysis:
Light to Heavy Crude
Accurately measured both Actual Crudes andBlends
Database of more than 110 Crudes in the Model
Does not require exact Crude and/or Blend for an accurate
Measurement
Universal Model
Reproducibility
Yield Curve < 2 % Broad Range, API Gravity from >9 to 52 deg
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Lagomar/Basrah 71/29
GP(Lagotreco/DZO/Boscan) 95/4/1
GP(Lagotreco/DZO/Boscan/Slops) 90/4/1/5
GP(Lagotreco/DZO) 95/5GP(Lagotreco/Oriente/DZO/Slops) 68/23/4/5
GP(Lagotreco/Oriente/DZO) 92/3/5
GP(Lagotreco/Oriente/mesa/DZO) 74/14/7/5GP(Lagotreco/Oriente/mesa/DZO/slops) 51/11/28/5/5
GP(Lagotreco/LagotrcoMediano/Oriente/mesa/DZO/Slops) 37/2/24/28/4/5
GP(DZO/MESA/Lagotreco/LagotrcoMediano/Orientae/Slops) 5/27/42/6/12/3
Some Crude Slates and Compositions used in Isla.
GP = General Purpose Crude. Slops = refinery slop re-blends of unknowncomposition and quality.
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Crude API 8/25-9/6/01
25
2627
28
29
30
31
32
33
34
35
0:03:38
15:16:27
6:29:22
21:42:25
12:55:32
4:08:17
19:21:02
10:33:52
1:46:49
18:49:43
10:10:13
1:30:48
16:51:30
8:12:22
23:32:13
14:53:09
6:14:16
5:48:57
21:07:14
12:25:33
Crude Switch
Tank Switch
Feed change
causing CDU
upset.
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Kero Freeze 8/25-9/6/01
-56
-54
-52
-50
-48
-46
-44
-42
-40
0:0
9:21
14:4
7:44
5:2
6:11
20:0
4:47
10:4
3:26
1:2
1:49
16:0
0:06
6:3
8:27
21:1
6:55
12:5
2:00
3:5
3:51
18:3
9:41
9:2
5:36
0:1
1:36
14:5
7:45
5:4
2:54
20:2
9:08
19:3
1:01
10:1
4:35
0:5
8:13
15:5
9:14
Tower Upset
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Kero Flash 8/25-9/6/01
30
35
40
45
50
55
60
0:0
9:21
14:4
7:44
5:2
6:11
20:0
4:47
10:4
3:26
1:2
1:49
16:0
0:06
6:3
8:27
21:1
6:55
12:5
2:00
3:5
3:51
18:3
9:41
9:2
5:36
0:1
1:36
14:5
7:45
5:4
2:54
20:2
9:08
19:3
1:01
10:1
4:35
0:5
8:13
15:5
9:14
Tower Upset
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
8/14/2019 Giammatteo Online NMR EAS 2007
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Naphtha 8/25-9/6/01
90
110
130
150
170
190
0:15
:07
14:53
:30
5:31
:57
20:10
:32
10:49
:12
1:27
:34
16:05
:52
6:44
:13
21:22
:41
13:15
:08
4:34
:24
19:20
:13
10:06
:09
0:52
:12
15:37
:18
6:23
:28
21:09
:43
19:36
:48
10:20
:22
1:04
:00
15:47
:42
T10 T50 T90 EP
Tower Upset
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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ASTMASTM Engineering
Method UsedReproducibility Units
Naphtha (med & Hvy) API D 4052 1Degrees F
Naphtha (med & Hvy) IBP D 86 14 Degrees FNaphtha (med & Hvy) T10 D 86 14 Degrees FNaphtha (med & Hvy) T50 D 86 14 Degrees FNaphtha (med & Hvy) T90 D 86 14 Degrees FNaphtha (med & Hvy) EBP D 86 14 Degrees FNaphtha (med & Hvy) Viscosity D 445 - % informational data only
Naphtha (med & Hvy) Flash Point D 93 5 Degrees C
Kerosene API D 4052 1 DegreeKerosene IBP D 86 14 Degrees FKerosene T10 D 86 14 Degrees FKerosene T50 D 86 14 Degrees FKerosene T90 D 86 14
Degrees FKerosene EBP D 86 14 Degrees FKerosene Viscosity D 445 - % informational data only
Kerosene Flash Point D 56 5 Degrees CKerosene Freeze Point D 2836 3 Degrees CKerosene Cloud Point D 5773 7 Degrees CKerosene Cetane Index D 976 - D 4737 2 Index Number
Diesel API D 4052 1 DegreeDiesel IBP D 86 14 Degrees FDiesel T10 D 86 14 Degrees FDiesel T50 D 86 14 Degrees FDiesel T90 D 86 14
Degrees FDiesel EBP D 86 14 Degrees FDiesel Cloud Point D 5773 7 Degrees CDiesel Freeze Point D 2836 3 Degrees CDiesel Viscosity D 445 - % informational data only
Diesel Cetane Index D 976 - D 4737 2 Index NumberDiesel Flash Point D 93 5 Degrees C
Light Cycle Gas Oil API D 4052 1 Degrees CLight Cycle Gas Oil IBP D 86 14 Degrees CLight Cycle Gas Oil T10 D 86 14 Degrees CLight Cycle Gas Oil T50 D 86 14 Degrees C
Light Cycle Gas Oil T90 D 8614
Degrees CLight Cycle Gas Oil EBP D 86 14 Degrees CLight Cycle Gas Oil Cloud Point D 5773 7 Degrees CLight Cycle Gas Oil Freeze Point D 2836 3 Degrees CLight Cycle Gas Oil Viscosity D 445 - % informational data only
Light Cycle Gas Oil Cetane Index D 976 - D 4737 2 Index NumberLight Cycle Gas Oil Flash Point D 93 5 Degrees C
FCC Gasoline RON D 2699 1.7 Octane NumberFCC Gasoline MON D 2700 1.7 Octane NumberFCC Gasoline T10 D 86 14 Degrees FFCC Gasoline T50 D 86 14 Degrees F
FCC Gasoline T90 D 86 14 Degrees FFCC Gasoline Aromatics detailed GC 1.1 Volume %FCC Gasoline Benzene 0.5 Volume %
Parameter Description
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24 Hour NMR Data on 5 Crude Unit Rundown Streams
T10, T50, T90
300
350
400
450
500
550
600
650
700
750
800
A. Kero (CDU1), B. Kero (CDU2), C. Diesel (CDU2), D. AGO (CDU2),
E. Kero Product (Hydrotreater)
DegF
A.
D.
E.
C.
B.
There are a total of 3 models for all 5 streams: One each for T10, T50, and T90.
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
SHS
CU diesel
Coker diesel
Hydrocracker feed
DensityD-86 distillationFlash point
Cetane NumberCloud PointPour Point
Clean Fuels
Clean Fuels Project Bakersfield, CA
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Typical NMR Diesel Measurements
deg C7.63.8D86 T5
deg C52.5D86 T10
deg C5.42.7D86 T30deg C63D86 T50
deg C8.64.3D86 T70
deg C8.24.1D86 T90
deg C84D86 T95deg C7.43.7D86 FBP
deg C4.42.2Flash
g/mL0.00280.0014Density
%0.170.085Viscositydeg C31.5Cloud
UnitsLab MethodReproducibility
NMR ModelAccuracyParameter
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Advancements in Advanced ProcessAnalyzer Technology
Who, What, When, Where, Why and How?
Or, dj vu All Over Again!
(Part II)
Paul J. GiammatteoProcess NMR Associates, LLC
NMR Process Systems, LLC
87A Sand Pit Road
Danbury, CT 06810
203-744-5905
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Too many spectroscopic based on-line analyzer projects (FTIR, NIR,NMR, and Raman too) have failed to meet expectations and/orobjectives due to:
Overselling the measurements
Underestimating the sampling requirementsTrying to replace all traditional analyzers with one technique.Dj vu!!
3500 3000 2500 2000 1500 100010000 9000 8000 7000 6000 5000 4000
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Who? Whos selling it?
Who wants it?
Who needs it?
Who is responsible it? Who should be responsible?
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
What?
What is being sold/promised?
What is the value of the project?
What is the value of each measurement?
What will be done with the information?
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
When? When will the analyzer be delivered?
When is the project completed? When the site is prepared?
When the analyzer completes site acceptance?
When the analyzer is connected to the DCS? When the analyzer is retired from service?
When will I get the benefit?
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Where? Where is the money coming from?
Where is the manpower coming from? Where are we going to put it?
Where are the samples coming from?
Where is the information going?
Control room?
Engineers desk?
Management/accounting?
Nowhere?
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Why? Why are we doing this?
Replacement and/or update?
New measurement/control strategy?
Because!!!!!!
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.comNMR Process Systems, Inc www.nmr-automation.com
How? How will the project be:
Budgeted?
Implemented?
Supported?
Integrated?
How complicated is this?
How beneficial is it?
How will my performance review beaffected?
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Economic DriversUsually:1. Naphtha is worth more than jet.
2. Jet is worth more than diesel.3. Diesel is worth more than gas oil.
The problem is pulling product to some limitingproperty (end point, smoke point, cloud point &freeze point).
Maybe we need better tools in the control room.
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.comNMR Process Systems, Inc www.nmr-automation.com
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The Real WorldDiesel lost to gas oil
Loss of diesel product
Tough product properties (cloud)
Diesel worth more than gasoline
Poor feed to FCC Loss of diesel product
Not much gasoline
More coke make
New Clean Fuels Initiatives Is 10 ppm sulfur dieselworth an average daily loss of 400 500 barrels ofdiesel production?
Can 200 to 500+ BPD of diesel and gasoline be found?
Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.comNMR Process Systems, Inc www.nmr-automation.com
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Paul J. Giammatteo
Process NMR Associates, LLC www.process-nmr.comNMR Process Systems, Inc www.nmr-automation.com
SHS
CU diesel
Coker diesel
Hydrocracker feed
DensityD-86 distillationFlash point
Cetane NumberCloud PointPour Point
Clean FuelsSHS
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Typical NMR Diesel Measurements
deg C7.63.8D86 T5
deg C52.5D86 T10
deg C5.42.7D86 T30
deg C63D86 T50
deg C8.64.3D86 T70
deg C8.24.1D86 T90
deg C84D86 T95
deg C7.43.7D86 FBP
deg C4.42.2Flash
g/mL0.00280.0014Density%0.170.085Viscosity
deg C31.5Cloud
UnitsLab MethodReproducibility
NMR ModelAccuracyParameter
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Paul J. Giammatteo
Process NMR Associates, LLCwww.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com
Crude Unit Integrated Solution
Distillation (D86, Sim Dis, TBP)
Flash Point
Cloud Point
Pour Point
Freeze Point
Chemistry (Fa, Fn, Fp,Naphthalene)
PONA/PIONA
API Gravity/Density
Octane/Cetane
APC and Optimization
IR
NMR
Two
Parameters
Per
Stream
$$$$$$$$$$$
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NPS ISNPS ISNPS ISNPS IS
NMR Process Systems, LLC87A Sand Pit Road
Danbury, Connecticut 06810+203-744-5905 (ph)
+203-743-9297 (fax)www.nmr-automation.com
What the Meaning of IS Is!
NMR Process Systems, Inc.
NMR Process Systems, Inc. is a joint venture company between Process NMR Associates, LLC
(Danbury CT), and TTC Labs Inc. (Fond du Lac WI). NPS markets, installs and supports
process NMR and other technology solutions for control and optimization in the refining,
petrochemical, pharmaceutical and food industries.
NPS is now advancing new concepts in process analysis by offering integrated analyticalsolutions into its product slate. Integrated NMR, NIR and other analyzer solutions offer
strategic reliability, sampling, and control benefits to the end user.
Paul J. Giammatteo
Process NMR Associates, LLCwww.process-nmr.com
NMR Process Systems, Inc www.nmr-automation.com