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Speeding up the Deployment of Biofuels:  Rapid Catalyst and Process Optimization with CRI/Criterion’s High-Throughput Tools  Vikrant Urade, Alan Del Paggio, Laxmi Narasimhan CRI Catalyst
An Outline of the Presentation ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],09/22/11
High-Throughput Workflow 09/22/11 ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Catalyst Preparation   Parallel pelletizing, crushing and sieving tools
Success Story: EO Catalyst ,[object Object],[object Object],[object Object],[object Object],09/22/11
Improved Dehydrogenation Catalyst ,[object Object],[object Object],[object Object],[object Object],[object Object],09/22/11
Role of CRI in the Bio-Domain 09/22/11 Lignocellulosic Biomass “ Front End” Biochemical or Thermochemical Oxygenate-rich Liquid Hydrocarbon Liquid  (Gasoline/Jet/Diesel) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object], “ Back End” Catalytic  Upgrading
Biofuels Pathways and CRI’s Catalyst Portfolio 09/22/11
Introducing IH 2 ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],09/22/11 Biomass  Sizing , Drying & Feed Hydropyrolysis Hydroconversion Cellulosic Hydrocarbon Product Very Low O Pyrolysis Oil Light Gases IH 2  ISBL Bubbling  Fluidized Bed  Proprietary Catalyst Green H 2 500-600°C < 500 psig Fixed Bed  Hydrotreater  Proprietary Catalyst Green H 2 < 500 psig Green H 2
Conversion of mixed alcohols  to gasoline ,[object Object],09/22/11
Problem Statement  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],09/22/11
Screening Statement ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],09/22/11
Power of EE: Rapid Process Optimization 09/22/11 Total olefin yield Decrease @ high T Increase @ low T WHSV Temperature Region 2 Region 3 Region 1: Incomplete dehydration Region 2: Complete dehydration but little further reaction Region 3: Complete dehydration and further oligomerization, alkylation and isomerization to a mixture of gasoline and jet fuel WHSV Temperature Region 1 Use of EE tools is a must to bring down process optimization time!
Yield Patterns 09/22/11 Temperature Temperature WHSV Aromatics WHSV Propylene WHSV Gasoline yield Temperature Temperature H 2 :Liquid  Naphthenes
Flexibility in Product Slate 09/22/11 Increasing process severity Predominantly gasoline VGO+ Hydrocarbon layer Starting with the same mixed alcohols feed, products from gasoline to VGO boiling range can be made by changing process severity
Product Profile: SIMDIS 09/22/11 Liquid product of alcohol oligomerization is a smooth boiling mixture of gasoline, jet fuel and diesel
Conclusions ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],09/22/11
Questions 09/22/11

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CRI - TCBiomass2011

  • 1. Speeding up the Deployment of Biofuels: Rapid Catalyst and Process Optimization with CRI/Criterion’s High-Throughput Tools Vikrant Urade, Alan Del Paggio, Laxmi Narasimhan CRI Catalyst
  • 2.
  • 3.
  • 4.
  • 5.
  • 6.
  • 7. Biofuels Pathways and CRI’s Catalyst Portfolio 09/22/11
  • 8.
  • 9.
  • 10.
  • 11.
  • 12. Power of EE: Rapid Process Optimization 09/22/11 Total olefin yield Decrease @ high T Increase @ low T WHSV Temperature Region 2 Region 3 Region 1: Incomplete dehydration Region 2: Complete dehydration but little further reaction Region 3: Complete dehydration and further oligomerization, alkylation and isomerization to a mixture of gasoline and jet fuel WHSV Temperature Region 1 Use of EE tools is a must to bring down process optimization time!
  • 13. Yield Patterns 09/22/11 Temperature Temperature WHSV Aromatics WHSV Propylene WHSV Gasoline yield Temperature Temperature H 2 :Liquid Naphthenes
  • 14. Flexibility in Product Slate 09/22/11 Increasing process severity Predominantly gasoline VGO+ Hydrocarbon layer Starting with the same mixed alcohols feed, products from gasoline to VGO boiling range can be made by changing process severity
  • 15. Product Profile: SIMDIS 09/22/11 Liquid product of alcohol oligomerization is a smooth boiling mixture of gasoline, jet fuel and diesel
  • 16.