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Application of NESSI to Modeling Application of NESSI to Modeling and Product /Process Developmentand Product /Process Development
Michelle J. CohnMichelle J. Cohn
uop uop LLCLLC
© 2004 UOP LLC. All Rights Reserved.
UOP LLC Who We AreUOP LLC Who We AreGlobal company with Global company with 11 manufacturing sites 11 manufacturing sites and offices in 25 countriesand offices in 25 countriesMore than 3,600 highly trained More than 3,600 highly trained employeesemployees90 years of innovative solutions 90 years of innovative solutions for the hydrocarbon processing for the hydrocarbon processing industryindustryUOP’s customers are located in UOP’s customers are located in more than 200 countries. more than 200 countries. World’s largest supplier of World’s largest supplier of molecular sieve adsorbentsmolecular sieve adsorbents
What We DoWhat We DoDevelop technology that Develop technology that provides solutions to problemsprovides solutions to problemsLicense, design, engineer,License, design, engineer,and service process technologyand service process technologyDevelop and manufacture Develop and manufacture catalysts, molecular sieves, catalysts, molecular sieves, adsorbents, and specialized adsorbents, and specialized equipmentequipmentTransfer technology to Transfer technology to customers who achieve high customers who achieve high yield of high quality productsyield of high quality products
UOP Research & Development UOP Research & Development ResourcesResources
More than 185 pilot plants (> 60 operating each day)More than 185 pilot plants (> 60 operating each day)
More than 20,000 pilot plantMore than 20,000 pilot plant--days per yeardays per year
Combinatorial chemistry capabilitiesCombinatorial chemistry capabilities
300 million data points generated per day300 million data points generated per day
350,000 laboratory analyses performed per year350,000 laboratory analyses performed per year
Modeling capabilities include: physical, computational Modeling capabilities include: physical, computational fluid dynamics, kinetic, and process simulation fluid dynamics, kinetic, and process simulation (dynamic and steady(dynamic and steady--state)state)
Average annual R&D spending: 8Average annual R&D spending: 8--10% of sales10% of sales
Process Analytical Technology (PAT)Process Analytical Technology (PAT)
PAT in Heterogeneous Catalysis Product and Process Controll
• Continuous composition diversity• Diversity in phase, microstructure, particle characteristics• Diversity in process conditions for all unit operations• Applied to synthesis, preparation, testing and characterization• Requires detailed material characterization
design, monitoring, control and modeling design, monitoring, control and modeling of materials and process conditionsof materials and process conditions
Desired Outcomes from PATDesired Outcomes from PAT
Increased manufacturing and production Increased manufacturing and production efficiencyefficiency
–– Increased product qualityIncreased product quality–– Reduced product variabilityReduced product variability
Increased innovationIncreased innovationReal time lot certification Real time lot certification
Enablers for PATEnablers for PAT
Reactor
Sensor∆T
Time
Online Online ProcessProcess
AnalyticsAnalytics
Data Analysis
ModelBuilding
SamplingFeedbackFeedbackControlControl
NIRNIRFTIRFTIRDLSDLSRAMANRAMAN
UltrasoundUltrasoundLAMIMSLAMIMSMicroMicro--calorimetrycalorimetryFTIRFTIR
NESSI
VTP
A
P.S.
NESSI
High High ThroughputThroughputCharacterization ToolsCharacterization Tools
HT RamanHT RamanActive Site, Active Site, Phase IDPhase ID
LAMIMSLAMIMSReactivityReactivity
IR ThermographyIR ThermographyTPD, AdsorptionTPD, Adsorption
HT Adsorption HT Adsorption Surface Area, PoreSurface Area, PoreSize DistributionSize DistributionFull spectrum of toolsFull spectrum of tools
UltraUltra--fast collection timesfast collection times100100’’s to 1000s to 1000’’s samples /days samples /day
GoalsGoals
Characterization is Key to SuccessCharacterization is Key to SuccessFrom Data From Data
Structure/Function Models Structure/Function Models = Knowledge= Knowledge
HT XRDHT XRDStructural,Structural,Phase IDPhase ID
HT SEMHT SEMMorphology, Particle SizeMorphology, Particle Size
HT XRFHT XRFElementElementAnalysisAnalysis
High Throughput ScreeningLAMIMS
Laser Activated Membrane IntroductionMass Spectrometry
Micro reactivity test Closed environment (realistic catalyst exposure)Very broad temperature application Full QMS product analysis Real world catalysts
The LAMIMS Screening System
System ComponentsLAMIMS reactant delivery systemA 25 watt CO2 barcode writing laserLAMIMS reactorQuadrupole mass spectrometer (QMS)
LAMIMS SystemLAMIMS SystemMeasure of metal sites
Laser heats samplesLaser heats samplesLarge array of samples Large array of samples in reactorin reactorMass spec monitors Mass spec monitors product streamproduct streamDehydrogenation test Dehydrogenation test for metal activityfor metal activityGoal: 1000 samples Goal: 1000 samples tested per day
CH3
Metal
CH3
H23+
MCH Toluene
To QMSPorous inlet
barrier
Reactant Gas Inlet
Gas out
Laser Beam
Fenix Laser Marker
tested per day
Sample Inlet
Catalyst Spot
To QMA
Silicone Rubber Membrane
Heat Cartridge Well
Tripod Base
ZnSe window
Al toothed flow distributor
Reactor
Data from Reactor System45 samples
Applying NeSSI TechnologyApplying NeSSI Technology
Honeywell sensorsParker Hannifin Intraflow substrate and componentsGO pressure regulatorsParker valves and actuatorsBrooks mass flow controllers
Used Ethernet and DeviceNet networks and commercially available Gen I LabView software on PC for configuration, control, data and diagnosticsProved the need for low power small size actuators and valvesExceptional diagnostic, control, and data collection capabilities Remote monitoring and control via standard internet tools Fast and easy configuration using LabView
Overview of SystemOverview of System
MFC
MFC
MFC
Cell
Laser
Vent
Nitrogen
Argon
Hydrogen
Neslab
Safety Enclosure
HT
-60
3
LAMIMS Flow System
MS
vent
vent
vent
cell
vent
Laser
MFC-20010( 0 -200 ccm)
0 - 250 PSI
0 - 250 PSI
NC
0 - 250 PSI
2005
KV-2006
PCV-
2007
PI-2008PSV-
2009 PCV-
20012
PI-2011 CK-
20013
KV
-201
4
NC
KV-4001
KV-4005
CK-4006
VP-4007
KV
-400
8
PSV-4011
HT-4014
LA-4015
CON-
5011
vent
MFC-10010 ( 0 -200
ccm)
0 - 250PSI
NC
0 - 250 PSI
NC
HV-1005 KV-1006PCV-1007
PI-1008PSV-
1009PI-1011
PCV-
1012
CK-1013KV-1014
CON- 6001
Set at 250 PSI
Set at 7 PSIG
Set at 250 PSI
Set at 250 PSI
CK-4017
AL-
5016
CK-4018
PI-4020
Vent
Vent
0 - 15 PSI
PI-7010
04
Safety enclosure
House Nitrogen gas
Argon gas
cylinder
House Hydrogen gasvent
MFC-30010 ( 0 -250 ccm)
0 - 250 PSI
0 - 250 PSI
HV-3005
HV-
KV-3006
PCV-
3007
PI-3008PSV-
3009PI-3011
PCV-
3012
CK-3013
NC
KV
-301
4
NC
PSV-4004
ISC-
4009
V-5002
TE
-5
00
4
CON-
5009
CON-
5010
refil vessell
0 - 600 PSI
0 - 600 PSI
HV-2001PI-2003
HV-3001PCV-
3002
PI-3003
0 - 600 PSI
HV-1001 PCV-
1002
PI-1003
0 - 600 PSI
To TSR
system
PUR-10
Set at 250 PSI0 - 600 PSI
PUR-2004
Neslab
Set at 250 PSI
PSV-2000
Optional
To TSR
system
Corridor area
Automated System ComponentsDescriptionDescription##
4 port two position valves4 port two position valves22
3 port two position valve3 port two position valve11
Pressure reducing Pressure reducing regulatorsregulators
3 3
Pressure IndicatorsPressure Indicators6 6
24VDC bellows sealed 24VDC bellows sealed valvesvalves
6 6
Back Pressure RegulatorsBack Pressure Regulators33
Device Net Flow controllersDevice Net Flow controllers33
LABVIEW SCREEN
LAMIMS Gas Handling SystemConstruction and Demonstration Accelerated with NeSSI
Mass Spectrometer installed Mass Spectrometer installed Laser installedLaser installedNESSI gas manifold installed NESSI gas manifold installed Lab View Automation software completedLab View Automation software completedSafety review completedSafety review completed
baselinebaseline+10%+10%Manifold costManifold cost4months4months2months2monthsPersonnel timePersonnel time6 months6 months4months4monthsElapsed timeElapsed timeTypicalTypicalW/W/NeSSINeSSIResourcesResources
Installation Went Very WellInstallation Went Very WellList of Minor IssuesList of Minor Issues
The check valves were ordered with a 1psi cracking The check valves were ordered with a 1psi cracking pressure.pressure. However, the check valves were delivered with a much However, the check valves were delivered with a much higher cracking pressure.higher cracking pressure. This was corrected the following day by This was corrected the following day by ordering new springs for the check valves.ordering new springs for the check valves.All the block valves and the mass flow controller for the nitrogAll the block valves and the mass flow controller for the nitrogen en line were specified to be normally opened.line were specified to be normally opened. They all were delivered They all were delivered normally closed.normally closed. A “simple” nitrogen line (needle valve and block A “simple” nitrogen line (needle valve and block valve) added to correct this safety issuevalve) added to correct this safety issueAll the connections to the All the connections to the NeslabNeslab fourfour--way valve (KVway valve (KV--4001) and to 4001) and to the vent fourthe vent four--way valve (KVway valve (KV--4005) were incorrectly installed.4005) were incorrectly installed. We We had to take apart most of the had to take apart most of the NeSSINeSSI system to correct this. system to correct this. Original design to put all electronics modules (Original design to put all electronics modules (labviewlabview field point field point modules, power supply, modules, power supply, etcetc.) inside an enclosure. .) inside an enclosure. The The NeSSINeSSIsystem arrived without such an enclosure, and all the electronicsystem arrived without such an enclosure, and all the electronics s parts were exposed to the outside, including the 110V cables.parts were exposed to the outside, including the 110V cables.The Brooks mass flow controllers failed to communicate The Brooks mass flow controllers failed to communicate ((DeviceNetDeviceNet communication) correctly with the automation communication) correctly with the automation software.software. Falaah resolved this issue with Brooks. Falaah resolved this issue with Brooks.
“Overall the “Overall the NeSSINeSSI system performs wellsystem performs well
Desired Outcomes from PAT and Desired Outcomes from PAT and NESSINESSI
Increased manufacturing and process Increased manufacturing and process efficiencyefficiency
–– Increased qualityIncreased quality–– Reduced variabilityReduced variability
Increased innovationIncreased innovationReal time certificationReal time certification
PAT SummaryPAT Summary
Technology and industry needs are Technology and industry needs are converging for PAT and NESSIconverging for PAT and NESSI
–– InIn--situ measurementssitu measurements–– Sensor integrationSensor integration–– Computational capacity and methodsComputational capacity and methods
Demonstrated success in refining and Demonstrated success in refining and petrochemicalspetrochemicalsOpportunities for crossOpportunities for cross--industry industry fertilizationfertilization
NESSINESSIPATPAT
AdvancedAdvancedCharacterizationCharacterization InformaticsInformatics
SummarySummary
Enabling Step Changes In Technology Enabling Step Changes In Technology
Innovation and growth driven by enabler toolboxInnovation and growth driven by enabler toolboxOpportunities PAT and NESSIOpportunities PAT and NESSI
–– Seek enhanced understanding of process variables and Seek enhanced understanding of process variables and relationship to performancerelationship to performance
Enabling technologies cut across industriesEnabling technologies cut across industries
AcknowledgmentsAcknowledgmentsEugene Smotkin, IIT, UPREugene Smotkin, IIT, UPR--RPRPRenxuan Liu, NuVant Systems Inc., currently GTIRenxuan Liu, NuVant Systems Inc., currently GTIYongtaeYongtae Kim, IITKim, IITDoug Galloway, UOP Doug Galloway, UOP Richard R. Willis, UOPRichard R. Willis, UOPFalaah Falih, UOP Falaah Falih, UOP Robert J. Allen, UOPRobert J. Allen, UOPMichael J. McCall, UOPMichael J. McCall, UOPJose A. Rodriguez, UPRJose A. Rodriguez, UPR--RPRPAmit Amit NayarNayar, IIT, IITJohn Mosher, HoneywellJohn Mosher, HoneywellRobert Nickels, HoneywellRobert Nickels, HoneywellSteve Doe, Parker HannifinSteve Doe, Parker Hannifin
A portion of this work was performed under the support of the U.S. Department of Commerce, National Institute of Standards and Technology, Advanced Technology Program, Cooperative Agreement 70NANB9H3035.”