Edwards cpac - 5-7-12

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Process NMR Associates Process NMR - Latest Technology Developments, Reaction Monitoring, Process Control Applications and At-Line Analysis Presented By John Edwards, Ph.D. Process NMR Associates, LLC Danbury, Connecticut May 7, 2012 CPAC Spring Meeting, Seattle, WA

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Transcript of Edwards cpac - 5-7-12

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Process NMR Associates

Process NMR - Latest Technology Developments,

Reaction Monitoring, Process Control Applications

and At-Line Analysis

Presented By

John Edwards, Ph.D.

Process NMR Associates, LLC

Danbury, Connecticut

May 7, 2012

CPAC Spring Meeting, Seattle, WA

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TTC Labs, Inc.

Process Engineering Excellence

Process NMR Associates

TopNIR Systems

250+ Analytical NMR Customers

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Process NMR Associates

High Resolution FT-NMR – Online / in Process

First Generation NMR – 1998 Elbit-ATI/Foxboro NMR Second Generation NMR – 2003

Qualion

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Lab version

On-Line version

New magnet design – 30mm bore size

• The amount of magnetic pieces that assemble the magnet reduced from 34 to 10. Reduction in

Mechanical Complexity

• Bore size of the magnet was increased to 30 mm - improve temperature susceptibility

• Improved temperature and shim stability.

New Digital Spectrometer Design - reduces footprint, improves signal processing capabilities

Probe - Improved Probe Q for Higher Sensitivity.

Software – Windows 7 – Improved Chemometric Capabilities

Third Generation NMR – Aspect Italia NMR System

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New magnet design solves the problem of:

Long term and short term Stability

Temperature sensitivity

State of the Art electronics:

Smaller foot-print

40 Shim coils on 2 single PCB

Integrated PCB for Shim & Heater Control

Digital RF & Acquisition –

improve SNR

New concept of Process Probe:

Entire sample pipe through

without contact with the system

Much better temperature

insulation

Higher Q (better sensitivity)

New Software:

Includes new algorithm for

standard and global Models

Fully automated process capacity

Extensive remote diagnostic capabilities

New Magnet System

Process NMR Associates

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NMR Sample System and Placement

Process NMR Associates

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Process NMR Associates

NMR Lock - External 7Li Lock @ 22.5 MHz Shim DACs Built into the Magnet Enclosure

Matrix Shimming Performed

by Optimizing FID RMS

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Process NMR Associates

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Process NMR Associates

p p m1234567

CH3

CH3

CH3

O

OH

A

B

C

D E F

G

H

A

F

B

CG

H

D E

PEG OH

PEG

p p m4 06 08 01 0 01 2 01 4 01 6 0

CH3

CH3

CH3

O

OH

A

B

C

D E F

G

H

I J

H

IJ

DE

F

A

B

G

C

PEG

CDCl3

FT-13C FT-1H

300 MHz

A

F

B

C

G

H

D E

PEG OH

PEG

58 MHz

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Process NMR Associates

ppm 1 2 3 4 5 6 7 8

300 MHz

CH3

CH2

CH

a-CH3

a-CH2

Aromatics Ethanol

Alkenes

60 MHz

Gasoline 1H NMR

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Process NMR Associates

Gasoline Parameters:

Octane Numbers

Distillation Properties (T10, T50, T90)

Benzene Content (wt%)

Total Aromatics (Wt%)

Total Olefins (Wt%)

Total Saturates (Wt%)

Oxygenates (Wt%)

Reid Vapor Pressure

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Process NMR Associates

Diesel Fuels

Biodiesels

Ethyl-benzene

Diethyl-benzene

Vinegar an Alcohol Fermentation

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Advantages and Disadvantages of NMR Applied to Process Control

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 Without Impact

Disadvantages:

Solids Cannot be Observed in a Liquid Stream

Individual Molecular Component Sensitivity Not Observed Directly in the Spectrum.

Low Sensitivity to Impurities – Quantitative > 500 ppm.

Sensitive to Ferromagnetics.

Sample Viscosity Causes Decrease in Resolution

Non-Hydrogen Containing Species are Not Observed (Exceptions Na, P, F, Al)

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Process NMR Associates

Application: Closed Loop Reformer Control - Installed 1998 Reformer Capacity: 34,000 Barrels per Day

Control Strategy: Control on MON and Benzene Content

NMR Analysis: 2 Minute Analysis

NMR PLS Outputs: RON, MON, Benzene (Wt%) Total Aromatics (Wt%)

RON Validation - April 2001 - April 2002

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1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39

NMR

CFR

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Application: Steam Cracking Optimization Installed 2000 Cracker Facility Capacity: 600,000 Tonnes per Year

Control Strategy: Feed Forward Detailed Hydrocarbon Analysis to SPYRO Optimization

NMR Analysis: 3-4 Minute Cycle (Single Stream)

NMR PLS Outputs: Naphtha – Detailed PIONA

C4-C10 normal-paraffin, iso-paraffin, aromatics, naphthenes

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Toluene

Actual Toluene (Wt%)

Pre

dic

ted T

olu

ene (

Wt%

) (

F9 C

1 )

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-.5

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Spectral Units ( )

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ta C

oe

ffic

ient (

F9 C

1 )

-1.5

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10 40 70 100 130

-1.5

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10 40 70 100 130

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Process NMR Associates

Cyclohexane

Beta Coefficients

Spectral Units ( ) Spectral Units ( )

Beta

Coeff

icie

nt (

F9 C

1 )

-2

-.5

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2.5

10 40 70 100 130

-2

-.5

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dic

ted

Cyclo

he

xa

ne

( F

9 C

1 )

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Cyclopentane

Date

Wt%

GC

NMR

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0

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iso-C5

iso-C6

iso-C7

iso-C8

iso-C9

96 Hours of NMR Process Output – iso-Paraffin Components

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0

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Benzene

Toluene

Ethyl-Benzene

Xylenes

96 Hours of NMR Process Output – Aromatic Components

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Process NMR Associates

Online NMR Applications Timeline

1993 - Development of Laboratory Based process NMR Methodologies

1995 - BTU Analysis of Refinery Fuel Gas

1995 - Sulfuric Acid Strength in Emulsion Zone of Stratco Acid Alkylation Unit

1999 - Diesel Blending System

1999 - Reformer Control System

2000 - Naphtha Cracker Feed Analyzer – Full GC PIONA

2000 - Crude Unit Analyzer

2000 - Crude Blending System

2001 - Gasoline Blending System,

2001 - Base Oil Manufacturing Analyzer

2002 - FCC Unit Analyzer

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20 40 60 80 100 120 140

VI 103

FACTOR1

F A C T O R 3

IL VI 115

VI 103

-3.0

-2.5

-2.0

-1.5

-1.0

-0.5

0.0

0.5

1.0

1.5

2.0

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3.0

-2.0 -1.5 -1.0 -0.5 0.0 0.5 1.0 1.5 2.0

Dewaxing Dearomatization

VI 100

AL

Base Oil Manufacturing – NMR Control

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0.00

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0:00:00 0:14:24 0:28:48 0:43:12

Acid CH3 Intensity

Anhydride CH3 Intensity

Process NMR - Latest Technology Developments, Reaction Monitoring, Process Control Applications and At-Line Analysis

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0.00

1.00

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0:00:00 0:02:53 0:05:46 0:08:38 0:11:31 0:14:24 0:17:17 0:20:10

Methyl Ester CH3

Acetic Anhydride CH3

Acetic Acid/Ester CH3

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0.00

2.00

4.00

6.00

8.00

10.00

12.00

0:00:00 0:02:53 0:05:46 0:08:38 0:11:31 0:14:24 0:17:17

Methyl Ester CH3

Acetic Anhydride CH3

Acetic Acid/Ester CH3

2 ppm 3 4 5 6

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Acknowledgements

Paul Giammatteo – PNA

Qualion NMR – Israel

Tal Cohen – ASPECT Italia and Modcon