Microchannel Fischer-Tropsch for Biomass-to-Liquids Green Chemistry Conference June 25, 2008 Jeff S. McDaniel.

Slides:



Advertisements
Similar presentations
Copyright 2006 by E-MetaVenture, Inc. All Rights Reserved. Potential Impact of GTL Commercialization on the Fuels and Specialty Product Markets NPRA Annual.
Advertisements

Introduction to Fischer Tropsch Synthesis
Challenges in Sustainable Hydrogen Production David Wails Low Carbon Research Group Johnson Matthey Technology Centre.
Outline Introduction Design of catalytic membrane reactor Results
Bioprocess Technology
Methanol Project Design a plant to make methanol from synthesis gas to supply a future market in direct methanol fuel cells.
BioAsia Presents Coal to Diesel Conversion Local - Environmental - Profitable.
“Garbage to Gas” Team Bravo Mentor Eleftherios Avtzis David Garcia
Fischer Tropsch Diesel Production Through Black Liquor Gasification Chelsey MacNeill 2006 SAE WISE Intern.
SHALE GAS INNOVATION CONTEST May 7, Company Incorporated the State of Delaware in May 2011 Exclusive License Agreement signed with NETL US 8,241,600.
30 th ISTC Japan Workshop on Advanced Catalysis Technologies in Russia Fluidized bed catalytic pyrolysis and gasification of biomass for production of.
B9 Coal Deploying Fuel Cells to Generate Cheap, Clean Electricity from Fossil Fuels.
Lignocellulose-Based Ethanol and Chemicals Segment (Montreal, Canada) January 13 th, 2009 Ethanol Biofuel Opportunity Transforming biomass and residues.
©October, 2006 Masada OxyNol  MASADA OxyNol, L.L.C. FINALLY, A CLEAN SMART SOLUTION TURNING WASTE INTO ETHANOL Presentation for Alternative Energy Solutions.
Global drivers and process innovation for ‘unconventional’ conversions
Drive for Energy Independence Fuel Prices Rising / Volatile
World Waste to Energy City Summit – May 2015
Liquid-Phase Methanol Process (LPMeOH) Jill DeTroye, Brandon Hurn, Kyle Ludwig, and Isaac Zaydens.
Renewal Fuel from Biomass Waste UC Discovery/West Biofuels Research Project: “An Investigation of a Thermochemical Process for the Conversion of Biomass.
Striclty for educational purposes Final project in M.Sc. Course for teachers, in the framework of the Caesarea –Rothschild program of the Feinberg Grad.
Direct Oxidation of Methane to Methanol
Group 6: Jacob Hebert, Michael McCutchen, Eric Powell, Jacob Reinhart
Title: Coal Cowboy Duration: 00:12:51 Link: engr
Biomass Gasification: Emerging Technologies for Converting Biomass to Pipeline-Quality SNG presented to Wisconsin Public Utility Institute Natural Gas.
Constandinos Mitsingas.  Overall Process  Syngas Production  Fischer Tropsch Process  Fischer Tropsch Reactors  Chemical Reaction Catalysts  Products.
SynGas Gasifier ALTERNATIVE ENERGY Technology Presentation.
Dr. Mario Eden Department Chair Auburn University.
USF Clean Energy Research Center Clean Energy and Systems Biomass derived fuel and systems Hydrogen fuelled systems Solar energy Thin film solar cell R&D.
Hydrogen from Renewable Fuels by Autothermal Reforming: Alcohols, Carbohydrates, and Biodiesel Lanny D. Schmidt Department of Chemical Engineering and.
Licensing Cellulosic Biofuel Technology Today Coskata: Accelerating to Commercialization Wes Bolsen CMO & VP, Government Affairs Coskata, Inc.
Kirill LIATS General Director Metaprocess
WASTE TO FUEL Evaluation and Thermochemical Modeling of High Temperature Steam Gasification of Municipal Solid Waste (MSW) University of Florida Boiling.
Hubbert’s Peak and Beyond The Future of Liquid Fuels Richard J. McDonald, Ph.D. Presented to: Department of Engineering U.S. Naval Academy.
Economic Analysis Introduction Motivation Process Flow Diagram Design Basis/Block Flow Diagram Environmental Analysis We have taken advantage of the arbitrage.
Production of Gasoline Components from Synthesis Gas ChE 397 Senior Design Group Alpha Ayesha Rizvi Bernard Hsu Jeff Tyska Mohammad Shehadeh Yacoub Awwad.
Table of Content Introduction of heat exchanger. Design of Coolers.
Microwave Destruction of Waste Rocket Fuels Waste Rocket Fuel Treatment Vapor Phase Destruction Easily Incorporated to Existing Water Scrubbing Systems.
FIRST OPERATING EXPERIENCE ON A 120kW DUAL CIRCULATING FLUIDIZED BED (DCFB) SYSTEM FOR CHEMICAL LOOPING COMBUSTION 4th International Workshop on In-Situ.
Ansaldo Ricerche S.p.A. Carbon Dioxide capture Berlin, March 2008.
Coal to Liquids – CTL Reactors : Fixed Bed Reactor and Slurry Bed Reactor FT Catalysts : Precipitated iron and supported cobalt Espinoza Prime 3 offers.
XtL – the Topsøe Approach. 2 Presentation outline  General introduction –Haldor Topsøe –What is XtL? –Focus of this presentation  Building blocks –Gasification.
Gas to Liquids – GTL Espinoza Prime 3 offers the following GTL technology Reactors : Fixed Bed Reactor and Slurry Bed Reactor FT Catalysts : Precipitated.
Gas To Liquids Test Facility
“Garbage to Gas” Team Bravo Eleftherios Avtzis David Garcia Bryan Isles Zack Labaschin Alena Nguyen Mentor Dan Rusinak Che Team Bravo.
2005 OBP Bi-Annual Peer Review Fran Ferraro Merrick & Company Sealaska Corporation Southeast Alaska Ethanol Project Integrated Biorefinery Session November.
Educating the Customer: PI - What’s it all about? Dr Mike Jones, Protensive PROCESS INTENSIFICATION: Meeting the Business and Technical Challenges, Gaining.
Science based waste to renewable synthetic transportation fuels
Solid Biomass Conversion to Transportation Fuels with UOP RTP™ Upgrading Technology Jim Rekoske April 3, 2012 Washington, D.C.
Biodiesel Fact Sheet Transesterification The most well-established technology for biodiesel production is transesterification. The process involves filtering.
S-1007 Multi-State Research Committee
Novel Post Combustion CO2 Capture (PCC) Process - MU Static Spiral Perforated Wings (MU-SSPW) Mixing Element - December 11, 2015 Mu Company Ltd. & K-Coal.
Advancements in Coal Technology 2006 Mid-America Regulatory Conference Columbus Ohio Tom Hewson Energy Ventures Analysis Inc Arlington Virginia June 20.
Table of Content Introduction of heat exchanger. Design of Coolers. Introduction of fixed bed reactors. Design of reactors.
This project has received funding from the European Union’s Horizon 2020 Research and Innovation Programme under the Grant Agreement No INNOVATIVE.
Smart Cities - Driving a New Economy – March 2016 David Lynch General Manager, Research and Development Enerkem biorefineries: A Smart City Solution for.
“ The Solution to Future Fuel”. The Fischer Cats Ali Al Musabeh Auto-Thermal Reactor Specialist Faraj Almarri Auto-Thermal Reactor Specialist Mohammed.
Game-Changing Technology for Oil Water Separation. The Development of the RJOS High Efficiency Oil Water Separation System Presented by Wade Bozak C.E.T.
Prepared by: Pn. Hairul Nazirah Abdul Halim
Dr. Razima Souleimanova, GTI Mark Ritter, Xcel Energy
Fundamental Science Needs for Waste to Chemical Conversion: Fundamental Challenges and Opportunities in Catalyst Design Christopher W. Jones Georgia Institute.
Biofuels 2.0 Sustainable Startups Jack Oswald, CEO SynGest Inc.
Progress in the Commercialization of Virent’s BioForming Process for the Production of Renewable Hydrogen Greg Keenan Vice President Business Development.
中科合成油技术有限公司 SynfuelsChina Synfuels China Technologies For Heavy Oil Upgrading and CTL Yongbin Cui Synfuels China Technology Co., Ltd.
Yousef Ghotok Joseph Havelin Wednesday, 23rd April 2008
Optimum Process Design for Gas Conversion to Wax-free Hydrocarbons
Team Echo Leader: Matt Levy
Gas To Liquids Test Facility
Fischer-Tropsch Synthesis
Making Hydrogen with Nuclear Energy for Liquid Fuels
The challenges of designing a Fischer-Tropsch reactor.
Presentation transcript:

Microchannel Fischer-Tropsch for Biomass-to-Liquids Green Chemistry Conference June 25, 2008 Jeff S. McDaniel

Agenda Velocys Introduction Microchannel Process Technology Modular Fischer-Tropsch Technology 2

Velocys Incorporated Battelle Memorial Institute spin-out company in employees Commercializing microchannel process technology 78 U.S. Patents Over $100 million of funding from industrial partners

A Better Biofuel 4 FeedstockProcessDistributeUse Modular technology Distributed processing Compatible with existing infrastructure Geographically widespread available feedstocks Superior diesel and jet fuels Wood waste Municipal Solid Waste

5 FeedstockProcessDistributeUse Modular technology Distributed processing Compatible with existing infrastructure Geographically widespread available feedstocks Superior diesel and jet fuels Wood waste Municipal Solid Waste Lower Cost Non-Food Feedstocks Superior Fuel Product Enabling Velocys ® Technology Velocys Focus: Biomass-to-Liquids (BTL)

Microchannel Process Technology Accelerates chemical reactions Many obstacles have been overcome

~ mm ~ mm Conventional Characteristic dimension Microchannel Microchannel Technology

88 Impact of Technology Velocys ® Technology systems outperform conventional reactors Accelerates chemical processes by 10 – 1,000 fold Enables smaller, more productive reactors Allows use of new, novel, more active catalysts Controls reactions at optimal conditions

Fouling: Potential Issue with Microchannels Vaporizer after 2000 hours operation Significant performance degradation over 2000 hours Solids at 15 ppm, 80% initial vapor quality

Fouling: Demonstrated Success for >1 Year Vaporizer after 9600 hours operation No performance degradation over 9600 hours

Catalyst: Demonstrated Success AspectPrimary ChallengeStatus LoadingEvenly distributing and packing catalyst particles in microchannels Demonstrated. Successfully loaded multiple devices and identified commercial vendors RegenerationAchieving long, steady runs Removing wax which blocks catalyst sites Demonstrated. Current device at 1,500+ hours Multiple regenerations demonstrated in earlier devices UnloadingRemoving wax build-up Removing catalyst after extended operation Demonstrated. Process developed and demonstrated on multiple devices AspectPrimary ChallengeStatus LoadingEvenly distributing and packing catalyst particles in microchannels Demonstrated. Successfully loaded multiple devices and identified commercial vendors RegenerationAchieving long, steady runs Removing wax which blocks catalyst sites Demonstrated. Recent device at ~1,800 hours Multiple regenerations demonstrated in earlier devices AspectPrimary ChallengeStatus LoadingEvenly distributing and packing catalyst particles in microchannels Demonstrated. Successfully loaded multiple devices and identified commercial vendors AspectPrimary ChallengeStatus

Modular Fischer-Tropsch Excellent performance Demonstrations with U.S. Air Force and others forthcoming

13 FT Technology Today Slurry Bubble Zone (small catalyst particles) Vapor product Liquid product Catalyst/ Wax Separator Catalyst Return Syngas Boiler Feed Water Slurry bubble FT Reactors among the largest in the world FT Reactor during shipping Capacity = 15,000 bpd Weight = 2,200 tons Height = 60 m Outer Diameter = 10m

14 Microchannel Fischer-Tropsch Reactor Concept -(CH 2 )n- + H 2 O CO + 2 H 2 Water Water/Steam Close integration of the exothermic Fischer-Tropsch synthesis and steam generation 0.2 – 5.0 mm

FT Reactor Comparison Technology Characteristics Fixed Bed (Shell) Slurry (Sasol, Rentech) Microchannel (Velocys)Velocys Advantage Gas-phase Reaction Time required, sec ~ – 0.3Smaller reactor for same throughput Temperature Uniformity, o C ~25 o C~5 o C Use of more active catalysts Catalyst Productivity kg/m 3 /hr ,700Lower catalyst costs Minimum Economic Facility, bpd 5,00010,000500Enables BTL and Offshore GTL applications Technology Characteristics Fixed Bed (Shell) Slurry (Sasol, Rentech) Microchannel (Velocys)Velocys Advantage Gas-phase Reaction Time required, sec ~ – 0.3Smaller reactor for same throughput Temperature Uniformity, o C ~25 o C~5 o C Use of more active catalysts Catalyst Attrition Rate MinorSevereMinorFixed bed architecture Catalyst Productivity kg/m 3 /hr ,700Lower catalyst costs Technology Characteristics Fixed Bed (Shell) Slurry (Sasol, Rentech) Microchannel (Velocys)Velocys Advantage Gas-phase Reaction Time required, sec ~ – 0.3Smaller reactor for same throughput Temperature Uniformity, o C ~25 o C~5 o C Use of more active catalysts Catalyst Attrition Rate MinorSevereMinorFixed bed architecture Technology Characteristics Fixed Bed (Shell) Slurry (Sasol, Rentech) Microchannel (Velocys)Velocys Advantage Gas-phase Reaction Time required, sec ~ – 0.3Smaller reactor for same throughput Temperature Uniformity, o C ~25 o C~5 o C Use of more active catalysts Technology Characteristics Fixed BedSlurry Microchannel (Velocys)Velocys Advantage Gas-phase Reaction Time required, sec ~ – 0.3Smaller reactor for same throughput Technology Characteristics Fixed BedSlurry Microchannel (Velocys)Velocys Advantage

Cross Flow Design Partial Boiling Water Coolant Process length ~ 0.6 m Process microchannels = 40 Coolant Length ~ 0.3 m Coolant microchannels = 425 Pilot Scale Demonstration Unit Coolant In Coolant Out Process Out Process In Capacity = ~2 gallons/day Conversion of CO: ~70% Selectivity to CH 4 : ~15% 3,000+ operating hours with integrated devices

Manufacturing Scale-Up Scale-up complete through one-quarter scale Device: 24” x 24” x 6” Capacity if operated: ~8 barrels/day

Commercial FT Reactor Assembly Capacity = 300 – 500 barrels/day 1.5 M 8 M

FT Reactor Assembly

U.S. Air Force Demonstration Project Assured Aerospace Fuels Research Facility Wright Patterson Air Force Base (Dayton, OH) Phase I - Under construction -Steam reformer + Fischer Tropsch + Hydrocracker -~25 gallons/day of FT capacity Velocys supplying microchannel FT reactor system Initial operation in January 2009 with biomass gasifier Air Force demonstration in mid-2009 Velocys participating in key U.S. Air Force fuel demonstration

Summary Microchannel technology greatly improves FT synthesis Velocys FT technology unlocks BTL opportunities 21

22 Contact Information Jeff McDaniel Business Development Mgr. Velocys Inc 7950 Corporate Blvd. Plain City, OHIO USA Phone: 614/ Web:

23