VESTA a Novel SNG Technology

Size: px
Start display at page:

Download "VESTA a Novel SNG Technology"

Transcription

1 VESTA a Novel SNG Technology Bressan Luigi Director of Process and Technologies Foster Wheeler Page - 1 -

2 Agenda Introducing Foster Wheeler Coal to Gas: Available SNG Technologies Coal to Gas: VESTA SNG Technology Status of the Technology Development Experience transfer Catalyst for VESTA SNG technology Application Conclusions Page - 2 -

3 Foster Wheeler An Introduction Tracing our roots to 1884 A leading international EPC contractor and power equipment supplier Successfully executed full life-cycle projects from concept to commissioning and operation including the Upstream, Midstream and Downstream hydrocarbon processing sectors $4 bn operating revenues in 2010 NASDAQ-listed company with operating HQ in Switzerland Permanent offices in 28 countries Page - 3 -

4 Foster Wheeler Delivering EPC excellence Upstream oil & gas LNG, gas-to-products, coal-to-products Refining Gasification Carbon capture & storage Chemicals & petrochemicals Pharmaceuticals, biotechnology & healthcare Power Metals & mining Environmental Page - 4 -

5 Foster Wheeler and Sud-Chemie jointly developed d the novel VESTA process to solve your SNG problem Page - 5 -

6 Coal to Gas Available SNG Technologies COAL Gasification Block Adjustment of H2/CO Ratio 3:1 CO2 Removal H2S Removal SNG Process SNG Gasification CO Conversion Purification SNG Process Different Technologies Differences in H2/CO Differences in CH4 Sour Gas Shift Physical Solvent Complex scheme to separate H2S from CO2 Exothermic Reaction Expensive Reactors Material High temperature Superheater Recycle at high temperature Recycle Compressor Page - 6 -

7 Coal to Gas Available SNG Technologies COAL Gasification Block Adjustment of H2/CO Ratio 3:1 CO2 Removal H2S Removal SNG Process SNG SNG Process Criticalities Exothermic Reaction Expensive Reactors Material High temperature Superheater Recycle at high temperature Recycle Compressor H2/CO Ratio Coke formation Recycle mandatory Temperature runaway Brick lined reactors Unsafe Operation Metal dusting risk Limitation in train size Page - 7 -

8 Coal to Gas VESTA SNG Technology Can Foster Wheeler and Sud-Chemie do more for you? Can we avoid high temperatures? Can we avoid recycle compressors? Can we avoid high temperature superheaters? Can we avoid brick lined vessels? Can we avoid high h alloyed steel? Can we avoid metal dusting? Can we avoid isothermal reactors? Page - 8 -

9 Coal to Gas VESTA SNG Technology Foster Wheeler and Sud-Chemie s Novel Vesta Process! Page - 9 -

10 Coal to Gas VESTA SNG Technology Available Technologies COAL Gasification Block Adjustment of H2/CO Ratio 3:1 CO2 Removal H2S Removal SNG Process SNG Novel Process COAL Gasification Block H2S Removal SNG Process CO2 Removal SNG Page

11 Coal to Gas VESTA SNG Technology Novel Process COAL Gasification Block H2S Removal SNG Process / CO2 removal SNG Gasification Purification SNG Process / CO2 removal All gasification technlogies are compatible with the Novel VESTA Process High efficiency / WHB / dry type are more beneficial H2S removal Carbonyl removal Fine Purification No H2/CO ratio adjustment No limitations of H2/CO ratio Neither coke formation nor metal dusting risk Low alloyed steel reactors Low severity WHB No Recycle Compressor Final CO2 removal (high quality) Page

12 Coal to Gas VESTA SNG Technology The novel VESTA process benefits Low temperature process: MAXIMUM 550 C No coke formation No metal dusting risk Once-through operation: NO RECYCLE COMPRESSOR Low severity steam boiler No brick-lined vessel No high alloyed steel No isothermal reactor High quality CO 2 recovery Page

13 Coal to Gas VESTA SNG Technology Economics Investment no recycle compressor no HT superheater all equipment sourced locally all equipment easy to transport on road smaller foot print Operation easy to operate start-up and shut-down procedures fast and simple high turn-down rate Safe to operate no temperature runaway possible Page

14 Status of the Technology Development The SNG novel process has been developed by FW with Sud-Chemie for the catalyst required for the methanation reactors The process has been simulated and the relevant optimum parameters defined Reactions have been tested at equilibrium and kinetics simulations have been completed The catalyst has been tested in the laboratory both for performance and resistance and all theoretical calculations have been confirmed Page

15 Experience Transfer FW has a great deal of experience in hydrogen plants where syngas is produced, shifted and cleaned up FW has a great deal of experience in power generation following a gasification unit (designed, engineered, constructed and started-up one of the largest IGCC in the world) FW have a great deal of experience in Acid Gas Removal systems from all available licensors FW has the capabilities to engineer complex control systems for the simultaneous operation of multi-unit complexes Page

16 Catalyst for VESTA SNG Technology Sud-Chemie Catalyst Nickel-based Stabilized matrix Continuous operation up to 560 C Stability demonstrated Page

17 Application Foster Wheeler and Sud-Chemie are investigating for opportunities in Chinese market On the basis of the information collected have tried to fix a typical study case Application The followings have been calculated: The specific consumption of clean syngas for 1000 NM 3 of SNG produced. Analysis and heating value of syngas Utility requirement/production for/from the process The information shall be considered preliminary and may be subject to further optimization on the basis of specific data that customers would like to give us Page

18 Application Design Basis Syngas composition At gasification outlet downstream AGR Syngas composition mol% CO H CO H 2 S + COS < 4 ppm N 2 Traces CH NH Ar Traces H 2 O 0.31 (sat) Syngas condition Value Pressure, Bar g 30.0 Temperature, 0 C 40.0 Page

19 Application Design Basis Utilities characteristics Steam Pressure (Bar g) Temperature (deg C) HP MP LP 1.8 Sat. Page

20 Application Conceptual Block Scheme CO2 Clean Shift Methanation reactors Finishing reactor 1 Syngas AGR CO2 Remov. Scrubber SNG 2 Page

21 Application 3 Methanation reactors Performances for a 250,000 Nm 3 /h (2.1 bn/y) Feed consumption 3433 kg/h of syngas for the production of 1,000 Nm 3 /h of SNG SNG quality CH H CO CO H 2 O Inerts traces traces LHV(kCal/Nm 3 ) after drying 1 2 Real production Nm 3 /h 272, ,656 Page

22 Application 3 Methanation reactors Performances for a 250, Nm 3 /h (2.1 bn/y) Performances (based on 3 methanation reactors) Utilities AGR inclusive (CO 2 removal) HP steam (40) 276 t/h MP steam (12) LP steam (1.8) Heat import 124 Gcal/h Demi water 448 t/h Electric Power (no recirculation compressor) Page

23 Application 3 Methanation reactors Catalyst volumes (based on 3 methanation reactors) Shift reactor CLEAN 160 m m diam. 1 Methanation 150 m m diam. 2 Methanation 160 m 3 4.7m diam. 3 Methanation 160 m 3 4.7m diam. Finishing Methanation 45 m 3 Total Shift 160 m 3 Total Methanation 470 m 3 Total finishing 45 m 3 Total 675 m 3 Page

24 Application 4 Methanation reactors Performances for a 250,000 Nm 3 /h (2.1 bn/y) Feed consumption 3433 kg/h of syngas for the production of 1,000 Nm 3 /h of SNG SNG quality CH H CO CO H 2 O Inerts traces traces traces traces LHV(kCal/Nm 3 ) after drying after drying Real production Nm 3 /h 272, , , , Page

25 Application 4 Methanation reactors Performances for a 250, Nm 3 /h (2.1 bn/y) Performances (based on 3 methanation reactors) Utilities AGR inclusive (CO 2 removal) HP steam (40) 276 t/h 419 t/h MP steam (12) LP steam (1.8) Heat import 124 Gcal/h 209 Gcal/h Demi water 448 t/h 589 t/h Electric Power (no recirculation compressor) Page

26 Application 4 Methanation reactors Catalyst volumes (based on 3 methanation reactors) Shift reactor CLEAN 160 m m 3. 1 Methanation 150 m m 3 2 Methanation 160 m m 3 3 Methanation 160 m m 3 4 Methanation m 3 Finishing Methanation 45 m 3 45 m 3 Total Shift 160 m m 3 Total Methanation 470 m m 3 Total finishing 45 m 3 45 m 3 Total 675 m m 3 Page

27 Conclusion Foster Wheeler and Sud-Chemie can tailor the VESTA process for your specific SNG project requirements Page

28 Thank you. Any questions? Page

Optimal design of coal gasifiers in combination with sour shift

Optimal design of coal gasifiers in combination with sour shift Optimal design of coal gasifiers in combination with sour shift 6 th International Freiberg Conference on IGCC & XtL technologies, Dresden, 19-22 May 2014 Speaker: Rasmus Trane-Restrup Agenda Gasifier

More information

Efficient Technologies for Down Stream Gasification Process and Integration with IGCC Power Production

Efficient Technologies for Down Stream Gasification Process and Integration with IGCC Power Production Efficient Technologies for Down Stream Gasification Process and Integration with IGCC Power Production Research I Technology I Catalysts Jens Perregaard, Per Bakkerud and Poul Erik Højlund Nielsen Haldor

More information

Rectisol Wash Units Acid Gas Removal for Polygeneration Concepts downstream Gasification

Rectisol Wash Units Acid Gas Removal for Polygeneration Concepts downstream Gasification Rectisol Wash Units Acid Gas Removal for Polygeneration Concepts downstream Gasification Ulvi Kerestecioğlu, Thomas Haberle GTC Conference, Washington DC, USA, November 3rd, 2010 Agenda of the Presentation

More information

VESTA Methanation Applications for Small Scale, Multipurpose, Green SNG Production. Amec Foster Wheeler Italiana (a Wood Company)

VESTA Methanation Applications for Small Scale, Multipurpose, Green SNG Production. Amec Foster Wheeler Italiana (a Wood Company) VESTA Methanation Applications for Small Scale, Multipurpose, Green SNG Production Amec Foster Wheeler Italiana (a Wood Company) Wood in short The power of three: A new global leader in technical, engineering

More information

Integration of carbon capture unit with power generation: technology advances in oxy-combustion plants

Integration of carbon capture unit with power generation: technology advances in oxy-combustion plants Integration of carbon capture unit with power generation: technology advances in oxy-combustion plants 3 rd Oxyfuel Combustion Conference, OCC3 9 th -13 th September 2013, Ponferrada, Spain Luca Mancuso,

More information

Hydrogen: The Lifeblood of a Refinery Options for Refiners

Hydrogen: The Lifeblood of a Refinery Options for Refiners Hydrogen: The Lifeblood of a Refinery Options for Refiners ME-Tech (Middle East Technology Conference) Dubai - January 2011 Luigi Bressan Director of Process and Technologies Foster Wheeler Italiana 1

More information

1. Process Description:

1. Process Description: 1. Process Description: The coal is converted to Raw Syngas in the Gasification Section. The Raw Syngas produced out of the Gasifier would be shifted (water gas shift) to adjust required H2/CO ratio and

More information

Lurgi s MPG Gasification plus Rectisol Gas Purification Advanced Process Combination for Reliable Syngas Production

Lurgi s MPG Gasification plus Rectisol Gas Purification Advanced Process Combination for Reliable Syngas Production Lurgi s MPG Gasification plus Rectisol Gas Purification Advanced Process Combination for Reliable Syngas Production Ulrich Koss, Holger Schlichting Gasification Technologies 2005 San Francisco, 9. 12.

More information

An Opportunity for Methanol; the Production Starting from Coal

An Opportunity for Methanol; the Production Starting from Coal An Opportunity for Methanol; the Production Starting from Coal by Luigi Bressan and Luca Mancuso Foster Wheeler Italiana and Ermanno Filippi, Methanol Casale S.A. presented at the 2008 WORLD METHANOL CONFERENCE

More information

Integrated processes for converting coal to chemicals and fuels. Maninder Jit Singh Haldor Topsøe

Integrated processes for converting coal to chemicals and fuels. Maninder Jit Singh Haldor Topsøe Integrated processes for converting coal to chemicals and fuels Maninder Jit Singh Haldor Topsøe Converting coal to chemicals and fuels Sulfuric acid SNG Coal Coal gasification Syngas conditioning Ammonia

More information

Valorisation of Synthesis Gas from Biomass - the Piteå DME pilot. Esben Lauge Sørensen, May 2009

Valorisation of Synthesis Gas from Biomass - the Piteå DME pilot. Esben Lauge Sørensen, May 2009 Valorisation of Synthesis Gas from Biomass - the Piteå DME pilot Esben Lauge Sørensen, May 2009 Contents Presentation of Haldor Topsøe A/S Presentation of Chemrec AB The BioDME Project Lay-out of DME pilot

More information

Balancing Hydrogen Demand and Production: Optimising the Lifeblood of a Refinery Luigi Bressan Director of Process and Technology Foster Wheeler

Balancing Hydrogen Demand and Production: Optimising the Lifeblood of a Refinery Luigi Bressan Director of Process and Technology Foster Wheeler Balancing Hydrogen Demand and Production: Optimising the Lifeblood of a Refinery Luigi Bressan Director of Process and Technology Foster Wheeler Italiana Agenda Introduction The refinery hydrogen balance

More information

Evaluation of Hydrogen Production at Refineries in China. The new UOP SeparALL TM Process. Bart Beuckels, UOP NV

Evaluation of Hydrogen Production at Refineries in China. The new UOP SeparALL TM Process. Bart Beuckels, UOP NV Evaluation of Hydrogen Production at Refineries in China The new UOP SeparALL TM Process Bart Beuckels, UOP NV IChemE Gasification Conference March 12, 2014 Rotterdam, the Netherlands 1914-2014 A Century

More information

UOP Selexol TM Technology Applications for CO 2 Capture

UOP Selexol TM Technology Applications for CO 2 Capture UOP Selexol TM Technology Applications for CO 2 Capture 3rd Annual Wyoming CO2 Conference June 23rd and 24th 2005 2009 UOP LLC. All rights reserved. Typical Gasification Complex Typical Raw Syngas H2 30-50%

More information

VESTA Methanation Applications for Small Scale, Multipurpose, Green SNG Production

VESTA Methanation Applications for Small Scale, Multipurpose, Green SNG Production A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 65, 2018 Guest Editors: Eliseo Ranzi, Mario Costa Copyright 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-62-4; ISSN 2283-9216 The Italian Association

More information

IGCC Plants : a Practical Pathway for Combined Production of Hydrogen and Power from Fossil Fuels

IGCC Plants : a Practical Pathway for Combined Production of Hydrogen and Power from Fossil Fuels International Hydrogen Energy Congress and Exhibition IHEC 2005 Istanbul, Turkey, 13-15 July 2005 IGCC Plants : a Practical Pathway for Combined Production of Hydrogen and Power from Fossil Fuels Luigi

More information

IGCC FUJIAN PROJECT. Dario Camozzi - Snamprogetti, Italy Andrea Baldelli - Snamprogetti, Italy Sun Hong Sinopec Ningbo Engineering Company, China

IGCC FUJIAN PROJECT. Dario Camozzi - Snamprogetti, Italy Andrea Baldelli - Snamprogetti, Italy Sun Hong Sinopec Ningbo Engineering Company, China IGCC FUJIAN PROJECT Dario Camozzi -, Italy Andrea Baldelli -, Italy Sun Hong Sinopec Ningbo Engineering Company, China Gasification Technologies 2007 San Francisco, October 14-17, 2007 1 Fujian Refining

More information

HYDROGEN GENERATION FOR MODERN REFINERIES

HYDROGEN GENERATION FOR MODERN REFINERIES HYDROGEN GENERATION FOR MODERN REFINERIES Luigi Bressan, Guido Collodi, Fabio Ruggeri Foster Wheeler Italiana SpA Via Caboto, 1 20094 Corsico Milan - Italy Abstract With increasing demand for diesel, more

More information

Present and future opportunities downstream gasifiers

Present and future opportunities downstream gasifiers Present and future opportunities downstream gasifiers Klas J. Andersson, Martin Skov Skjøth-Rasmussen, Poul E. Højlund Nielsen 7 th International Freiberg/Inner Mongolia Conference, June 8-2015 Syngas

More information

Customizing Syngas Specifications with E-Gas Technology Gasifier

Customizing Syngas Specifications with E-Gas Technology Gasifier Customizing Syngas Specifications with E-Gas Technology Gasifier Arnold Keller, David Breton, Chancelor Williams and Graham Poulter, ConocoPhillips, Houston, Texas Gasification Technology Conference San

More information

2014 Gasification Technologies Conference Washington, DC Oct UOP LLC. All rights reserved.

2014 Gasification Technologies Conference Washington, DC Oct UOP LLC. All rights reserved. Techno-economic economic analysis of acid gas removal solutions for SNG applications Ganesh Nayak 2014 Gasification Technologies Conference Washington, DC Oct 26-29 2014 UOP LLC. All rights reserved. Criteria

More information

An Update On Shell Licensed Gasification Projects and the Performance of Pernis IGCC

An Update On Shell Licensed Gasification Projects and the Performance of Pernis IGCC An Update On Shell Licensed Gasification Projects and the Performance of Pernis IGCC 2000 Gasification Technologies Conference 8-11 October, San Francisco J.D. de Graaf Summary Introduction Shell Gasification

More information

2013 Instituto Petroquímico Argentino (IPA) Conference 09 October 2013 Buenos Aires, Argentina

2013 Instituto Petroquímico Argentino (IPA) Conference 09 October 2013 Buenos Aires, Argentina The UOP Selexol Process: Efficient Acid Gas Removal in Gasification Value Chain Henry Traylor UOP LLC, A Honeywell Company 2013 Instituto Petroquímico Argentino (IPA) Conference 09 October 2013 Buenos

More information

Methanol Production by Gasification of Heavy Residues

Methanol Production by Gasification of Heavy Residues Methanol Production by Gasification of Heavy Residues by C. A. A. Higman Presented at the IChemE Conference "Gasification: An Alternative to Natural Gas" London, 22-23 23 November, 1995 Methanol Production

More information

Synthesis Gas Processes for Synfuels Production

Synthesis Gas Processes for Synfuels Production Synthesis Gas Processes for Synfuels Production Christopher Higman presented at EUROGAS '90 Trondheim, June 1990 Abstract Synthesis Gas Processes for Synfuels Production Christopher Higman Synthetic fuels

More information

GASIFICATION TECHNOLOGIES 2003

GASIFICATION TECHNOLOGIES 2003 S.Francisco, California October 12-15, 2003 GASIFICATION TECHNOLOGIES 2003 COAL POWER PLANTS WITH CO2 CAPTURE: THE IGCC OPTION J.Davison - IEA Greenhouse Gas R&D Programme L.Bressan - R.M.Domenichini -

More information

Coupling gasification and metallurgical applications

Coupling gasification and metallurgical applications Coupling gasification and metallurgical applications Robert Pardemann, Tanja Schaaf, Jochen Grünig, Katharina Förster, Andreas Orth International Freiberg Conference on IGCC & XtL Technologies 12 16 June

More information

Analysis of flexibility options for electricity generating projects with pre-combustion capture of CO 2

Analysis of flexibility options for electricity generating projects with pre-combustion capture of CO 2 IC 4 S Imperial College Centre for Carbon Capture and Storage Workshop on Operating Flexibility of Power Plants with CCS Imperial College, London, 11 th 12 th November 2009 Analysis of flexibility options

More information

POXSYN A Novel Approach for Syngas to Chemicals Production

POXSYN A Novel Approach for Syngas to Chemicals Production POXSYN A Novel Approach for Syngas to Chemicals Production Alexander Roesch, Manager Process Engineering HyCO Technologies Colorado Springs, 16th October 2017- Air Liquide Global E&C Solutions Air Liquide

More information

CASALE COAL-BASED METHANOL SYNLOOPS

CASALE COAL-BASED METHANOL SYNLOOPS CASALE COAL-BASED METHANOL SYNLOOPS by Francesco Baratto METHANOL CASALE S.A. Lugano, Switzerland Huang Rong SHANGHAI COKING AND CHEMICAL CORP. (SCC), P. R. China Huang Anxin XINNENG ENERGY LIMITED - XIN'AO

More information

Slim POX Design for Gasification 4th International Freiberg Conference on IGCC & XtL Technologies 3-5. May 2010

Slim POX Design for Gasification 4th International Freiberg Conference on IGCC & XtL Technologies 3-5. May 2010 Slim POX Design for Gasification 4th International Freiberg Conference on IGCC & XtL Technologies 3-5. May 2010 H. Tautz, Dept. EV, Linde Engineering Contents Introduction Kinetic modeling Reactor design

More information

Linde Rectisol Wash Process 2 nd International Freiberg Conference on IGCC & XtL Technologies

Linde Rectisol Wash Process 2 nd International Freiberg Conference on IGCC & XtL Technologies Linde Rectisol Wash Process 2 nd International Freiberg Conference on IGCC & XtL Technologies 8 th -12 th May, 2007 Dr. A. Prelipceanu, Dr. H.-P. Kaballo, U. Kerestecioglu Acid Gas Removal is an Important

More information

Company Brochure 2012

Company Brochure 2012 Company Brochure 2012 2 Table of contents 1. Company Profile / Company Description... 3 2. Scope of Services... 4 3. Gasification... 6 4. Feedstocks and by-products... 7 5. History of gasification process...

More information

Carbon Capture Options for LNG Liquefaction

Carbon Capture Options for LNG Liquefaction Carbon Capture Options for LNG Liquefaction ME-Tech 25 January 2011, Dubai Chris Sharratt Manager, Midstream Business Solutions Group Images: Courtesy of Woodside Energy Ltd Outline LNG liquefaction sources

More information

Perspective on Coal Utilization Technology

Perspective on Coal Utilization Technology Perspective on Coal Utilization Technology 21st Annual International Pittsburgh Coal Conference on 14-16 September, 2004 Naokazu Kimura Director, Wakamatsu Research Institute J-Power/EPDC Agenda - About

More information

50 Years of PSA Technology for H2 Purification

50 Years of PSA Technology for H2 Purification 50 Years of PSA Technology for H 2 Purification 1 50 Years of PSA Technology for H2 Purification The first industrial application of Pressure Swing Adsorption (PSA) went on stream in 1966 at a Union Carbide

More information

WITH CO2 SEQUESTRATION

WITH CO2 SEQUESTRATION PROJECT DESIGNS FOR IGCC & SNG WITH CO2 SEQUESTRATION Gasification Technologies Conference October 5, 2009 Ron Herbanek, Bill Mooneyhan ConocoPhillips Company Presentation Outline Introduction Design Premise

More information

Topsøe Methanol Technology for Coal Based Plants

Topsøe Methanol Technology for Coal Based Plants Topsøe Methanol Technology for Coal Based Plants By Carsten Sejrbo Nielsen Topsøe Methanol Technology for Coal Based Plants 2/7 Fig 1 Introduction Due to the high cost of natural gas and oil, the more

More information

HEAVY CRUDE UPGRADING: AN OPTION FOR GASIFICATION

HEAVY CRUDE UPGRADING: AN OPTION FOR GASIFICATION / HEAVY CRUDE UPGRADING: AN OPTION FOR GASIFICATION Luigi Bressan Foster Wheeler Italiana Corporation Michael J. McGrath - Foster Wheeler USA Corporation Gasification Technologies Council Conference San

More information

Gasification to meet refinery hydrogen, electricity and steam demands: Availability vs Costs

Gasification to meet refinery hydrogen, electricity and steam demands: Availability vs Costs Gasification to meet refinery hydrogen, electricity and steam demands: Availability vs Costs GTC Annual Conference 4-7 October 2009 Colorado Springs S. Arienti Process Director Foster Wheeler Italiana

More information

Austro Energy Systems Int. AG. Gas reformer AES3000

Austro Energy Systems Int. AG. Gas reformer AES3000 Austro Energy Systems Int. AG Gas reformer AES3000 1 Gas reformer AES3000 Purification of associated gas from the hydrogen sulfide and high hydrocarbons and conversion of its qualities into similar properties

More information

TRONDHEIM CCS CONFERENCE

TRONDHEIM CCS CONFERENCE TRONDHEIM CCS CONFERENCE June 15, 2011 6th Trondheim Conference on CO 2 Capture, Transport and Storage Pedro Casero Cabezón (pcasero@elcogas.es) ELCOGAS S.A (www.elcogas.es) 1 SCOPE IGCC & ELCOGAS, S.A

More information

Tony Alderson & Steve Mabey Jacobs Consultancy

Tony Alderson & Steve Mabey Jacobs Consultancy GASIFICATION TECHNOLOGIES CONFERENCE 2008 Optimizing Capex and Reliability on Gasification Facilities Tony Alderson & Steve Mabey Jacobs Consultancy 1 Agenda Who we are Gasification business drivers Delivering

More information

environmental impacts. These impurity levels may be very heterogeneous and in

environmental impacts. These impurity levels may be very heterogeneous and in CO 2 IMPURITIES Captured CO 2 from an (industrial) activity (such as the CO 2 that will be handled by the CO 2 distribution hub) may contain impurities, which would have practical impacts on CO 2 transport

More information

Example SPC-2: Effect of Increasing Column P on a C3 splitter

Example SPC-2: Effect of Increasing Column P on a C3 splitter Example SPC-2: Effect of Increasing Column P on a C3 splitter Consider the separation of a mixture of 50 mol/hr of propane C 3 H 8 (1) and 50 mol/hr propene, C 3 H 6 (2) at a pressure of 1.1 bar and a

More information

A new HP version of Lurgi s FBDBTM gasifier is bringing more value to clients

A new HP version of Lurgi s FBDBTM gasifier is bringing more value to clients A new HP version of Lurgi s FBDBTM gasifier is bringing more value to clients 2011 Max-Michael Weiss Air Liquide E&C/ Lurgi GmbH, Frankfurt, Germany GAP Conference Beijing 2011 Outline AIR LIQUIDE Group

More information

Analysis of Exergy and Energy of Gasifier Systems for Coal-to-Fuel

Analysis of Exergy and Energy of Gasifier Systems for Coal-to-Fuel Analysis of Exergy and Energy of Gasifier Systems for Coal-to-Fuel 1 Nishant Sharma, 2 Bhupendra Gupta, 3 Ranjeet Pratap Singh Chauhan 1 Govt Engg College Jabalpur 2 GEC College Gwalior 3 Department of

More information

Thermodynamic performance of IGCC with oxycombustion

Thermodynamic performance of IGCC with oxycombustion Thermodynamic performance of IGCC with oxycombustion CO 2 capture G.Lozza, M. Romano, A. Giuffrida Dip. Energia, Politecnico di Milano, Italy Purpose of the study CO 2 capture from coal power plant. Configurations

More information

BASF Catalysts Yesterday, Today and Tomorrow

BASF Catalysts Yesterday, Today and Tomorrow BASF Catalysts Yesterday, Today and Tomorrow BASF Catalysts Fact and Figures Largest catalyst company worldwide Only company covering all fields of catalysis Leader in catalysis R+D with 600+ scientists

More information

Hydrogen is a particularly

Hydrogen is a particularly Optimised hydrogen production by steam reforming: part I Modelling optimisation of process and design parameters for minimising natural gas consumption in hydrogen production by steam reforming Sanke Rajyalakshmi,

More information

Pilot Scale Production of Mixed Alcohols from Wood. Supplementary Information

Pilot Scale Production of Mixed Alcohols from Wood. Supplementary Information Pilot Scale Production of Mixed Alcohols from Wood Supplementary Information Richard L. Bain, Kimberly A. Magrini-Bair, Jesse E. Hensley *, Whitney S. Jablonski, Kristin M. Smith, Katherine R. Gaston,

More information

Biosyngas from forest product industry by-products and residues

Biosyngas from forest product industry by-products and residues Biosyngas from forest product industry by-products and residues 1 Presentation at the VETAANI Conference 9 April 2014 Prof Rikard Gebart Luleå University of Technology Feedstock use in the forest product

More information

Enabling technologies for precombustion

Enabling technologies for precombustion Enabling technologies for precombustion TCCS-6 June 14-16 2011, Trondheim Nils Erland L. Haugen, SINTEF Energy Research Madhavan Poyyapakkam, ALSTOM Christian Brunhuber, SIEMENS Khawar Syed, ALSTOM Marie

More information

Topsoe Activities Downstream Gasifiers

Topsoe Activities Downstream Gasifiers Topsoe Activities Downstream Gasifiers Poul E. Højlund Nielsen, Klas J. Andersson 8 th International Freiberg/ Conference, June 12-16 - 2016 Haldor Topsøe in brief Established in 1940 by Dr. Haldor Topsøe.

More information

WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS

WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS BORSIG The Company BORSIG Process Heat Exchanger GmbH, a member of the BORSIG Group, is the international leading manufacturer of

More information

Production costs for different green gas qualities based on large-scale gasification of. biomass. Author: Bahlmann, R. Co-author(s): Roeterink, H.

Production costs for different green gas qualities based on large-scale gasification of. biomass. Author: Bahlmann, R. Co-author(s): Roeterink, H. Production costs for different green gas qualities based on large-scale gasification of biomass Author: Bahlmann, R. Co-author(s): Roeterink, H. DNV GL, Groningen, the Netherlands Abstract In the last

More information

METHANOL CASALE AND FOSTER WHEELER: JOINING FORCES FOR THE METHANOL MARKET

METHANOL CASALE AND FOSTER WHEELER: JOINING FORCES FOR THE METHANOL MARKET METHANOL CASALE AND FOSTER WHEELER: JOINING FORCES FOR THE METHANOL MARKET by Luigi Bressan, Director of Process and Technologies Foster Wheeler Italiana and Ermanno Filippi, Director of Research and Development

More information

PRENFLO: PSG and PDQ

PRENFLO: PSG and PDQ 1 PRENFLO: PSG and PDQ Latest Developments based on 10 years Operating Experience at Elcogas IGCC, Puertollano, Spain Karsten Radtke, Max Heinritz-Adrian; Uhde, Germany Max Hooper, Bill Richards; Uhde

More information

PEP Review METHANOL PRODUCTION VIA TOYO PROCESS By Syed N. Naqvi (December 2011) ABSTRACT

PEP Review METHANOL PRODUCTION VIA TOYO PROCESS By Syed N. Naqvi (December 2011) ABSTRACT PEP Review 2011-14 METHANOL PRODUCTION VIA TOYO PROCESS By Syed N. Naqvi (December 2011) ABSTRACT This Review updates PEP Review 2001-14 by presenting a techno-economic evaluation of a methanol production

More information

Selection of Wash Systems for Sour Gas Removal

Selection of Wash Systems for Sour Gas Removal Selection of Wash Systems for Sour Gas Removal 4 th International Freiberg Conference on IGCC & XtL Technologies 5 May 2010 B. Munder, S. Grob, P.M. Fritz With contribution of A. Brandl, U. Kerestecioglu,

More information

Noell Entrained-Flow Gasification

Noell Entrained-Flow Gasification Noell Entrained-Flow Gasification Industrial and chemical wastes Conventional fuels Industrial and chemical wastes high-salt ash-free ash-free ash-containing ash-containing Reactor with special cooling

More information

SYNERGI MELLEM BIOGAS- OPGRADERING OG SOEC

SYNERGI MELLEM BIOGAS- OPGRADERING OG SOEC SYNERGI MELLEM BIOGAS- OPGRADERING OG SOEC Christian Dannesboe Center for Biorefinery Technologies AU BIOGAS PLANT FOULUM Biogas produced from manure Production of 100 Nm3/h Biogas is 40% CO 2. (Only 60%

More information

Ammonia plants. Flexible solutions for all feedstocks.

Ammonia plants. Flexible solutions for all feedstocks. Ammonia plants. Flexible solutions for all feedstocks. Meeting the challenges of a volatile marketplace. 03 Meeting the challenges of a volatile marketplace. With volatility in worldwide energy prices

More information

WORLDWIDE REFINERY PROCESSING REVIEW. Third Quarter 2011

WORLDWIDE REFINERY PROCESSING REVIEW. Third Quarter 2011 WORLDWIDE REFINERY PROCESSING REVIEW Monitoring Technology Development and Competition in a Single Source Third Quarter 2011 Hydrogen Production, Purification, and Recovery HYDROCARBON PUBLISHING COMPANY

More information

CO 2 Capture and Storage: Options and Challenges for the Cement Industry

CO 2 Capture and Storage: Options and Challenges for the Cement Industry CO 2 Capture and Storage: Options and Challenges for the Cement Industry Martin Schneider, Düsseldorf, Germany CSI Workshop Beijing, 16 17 November 2008 CO 2 abatement costs will tremendously increase

More information

Sasol-Lurgi Fixed Bed Dry Bottom Gasification for Fuels and Chemicals

Sasol-Lurgi Fixed Bed Dry Bottom Gasification for Fuels and Chemicals Sasol-Lurgi Fixed Bed Dry Bottom Gasification for Fuels and Chemicals Sasol-Lurgi Technology Company (Pty) Ltd 2 nd International Freiberg Conference on IGCC & XtL Technologies, 8-12th May 2007, Freiberg

More information

Hydrogen Separation Membrane Applications

Hydrogen Separation Membrane Applications 2009 Hydrogen Separation Membrane Applications Eltron Research & Development Inc. 4600 Nautilus Court South Boulder, CO 80301-3241 Doug Jack VP Technology 303.530.0263 x118 djack@eltronresearch.com Carl

More information

METHANOL CONVERTER AND SYNLOOP DESIGNS FOR GASIFICATION PLANTS

METHANOL CONVERTER AND SYNLOOP DESIGNS FOR GASIFICATION PLANTS METHANOL CONVERTER AND SYNLOOP DESIGNS FOR GASIFICATION PLANTS By E. Filippi, M. Badano METHANOL CASALE S.A. Lugano, Switzerland For presentation at the 2007 WORLD METHANOL CONFERENCE November 27-29 2007,

More information

New Refinery Applications of Shell Gasification Technology

New Refinery Applications of Shell Gasification Technology New Refinery Applications of Shell Gasification Technology Joachim Wolff Piet Zuideveld Gasification Technologies Conference San Francisco, October 9-12, 2005 Shell Gasification Process & Refineries -

More information

WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS

WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS BORSIG PROCESS HEAT EXCHANGER GMBH WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS www.borsig.de/pro 1 About BORSIG Process Heat Exchanger GmbH BORSIG Process Heat Exchanger GmbH,

More information

Experience responsibility. Engineering. for the Process Industry. Chemistry & Metallurgy. Oil & Gas. Minerals

Experience responsibility. Engineering. for the Process Industry. Chemistry & Metallurgy. Oil & Gas. Minerals Experience responsibility Engineering for the Process Industry Chemistry & Metallurgy Oil & Gas Minerals Examples of Processes: multi-component distillation, solvent recovery chemical syntheses extraction

More information

Available online at Energy Procedia 4 (2011) Energy Procedia 00 (2010)

Available online at   Energy Procedia 4 (2011) Energy Procedia 00 (2010) Available online at www.sciencedirect.com Energy Procedia 4 (2011) 1925 1932 Energy Procedia 00 (2010) 000 000 Energy Procedia www.elsevier.com/locate/procedia www.elsevier.com/locate/xxx GHGT-10 Evaluation

More information

Warm Syngas Clean-up Process Development: Multi-Contaminant Removal using Sorbents and Ir-Ni Tar Reforming Catalyst

Warm Syngas Clean-up Process Development: Multi-Contaminant Removal using Sorbents and Ir-Ni Tar Reforming Catalyst Warm Syngas Clean-up Process Development: Multi-Contaminant Removal using Sorbents and Ir-Ni Tar Reforming Catalyst Robert A. Dagle, Kurt A. Spies, David L. King Pacific Northwest National Laboratory,

More information

Oxidative Coupling of Methane: A Design of Integrated Catalytic processes

Oxidative Coupling of Methane: A Design of Integrated Catalytic processes CHEMICAL ENGINEERING TRANSACTIONS Volume 21, 2010 Editor J. J. Klemeš, H. L. Lam, P. S. Varbanov Copyright 2010, AIDIC Servizi S.r.l., ISBN 978-88-95608-05-1 ISSN 1974-9791 DOI: 10.3303/CET1021234 1399

More information

SYNTHETIC NATURAL GAS PLANT. Philadelphia, PA

SYNTHETIC NATURAL GAS PLANT. Philadelphia, PA SYNTHETIC NATURAL GAS PLANT Philadelphia, PA SYNTHETIC NATURAL GAS PLANT The SNG facility was constructed in 1977 but has seen very little operational activity. The SNG Facility employs the British Gas

More information

Improving Flexibility of IGCC for Harmonizing with Renewable Energy - Osaki CoolGen s Efforts -

Improving Flexibility of IGCC for Harmonizing with Renewable Energy - Osaki CoolGen s Efforts - Improving Flexibility of IGCC for Harmonizing with Renewable Energy - Osaki CoolGen s Efforts - Table of Contents 1. Project Background 2. Progress of Osaki CoolGen Project (1) Outline of Osaki CoolGen

More information

We accept the challenge!

We accept the challenge! Synthesis Gas Generation for Transportation Fuel Production Gasification Technologies Conference 2014, October 26-29 Washington, DC Andras I. Horvath / ANDRITZ Oy, Niels R. Udengaard /Haldor Topsoe Inc.

More information

COAL POWER PLANTS WITH CO 2 CAPTURE: THE IGCC OPTION

COAL POWER PLANTS WITH CO 2 CAPTURE: THE IGCC OPTION COAL POWER PLANTS WITH CO 2 CAPTURE: THE IGCC OPTION J. Davison IEA Greenhouse Gas R&D Programme L. Bressan - R.M. Domenichini - Foster Wheeler Italiana ABSTRACT One of the most promising technologies

More information

ENI REFINING & MARKETING SANNAZZARO GASIFICATION PLANT PROJECT UPDATE AND START UP EXPERIENCE

ENI REFINING & MARKETING SANNAZZARO GASIFICATION PLANT PROJECT UPDATE AND START UP EXPERIENCE Gasification Technologies 2006 Washington, DC October 1-4, 2006 ENI REFINING & MARKETING SANNAZZARO GASIFICATION PLANT PROJECT UPDATE AND START UP EXPERIENCE Dario Camozzi -, Italy Raffaella Lucarno -

More information

Air Products Pressure Swing Adsorption at the National Carbon Capture Center

Air Products Pressure Swing Adsorption at the National Carbon Capture Center Air Products Pressure Swing Adsorption at the National Carbon Capture Center Project Objectives Gasification is a promising alternative to traditional coal-fired combustion that can be adapted to CO 2

More information

2.0 HYDROGEN GENERATION UNIT 2.1 INTRODUCTION

2.0 HYDROGEN GENERATION UNIT 2.1 INTRODUCTION 2.0 HYDROGEN GENERATION UNIT 2.1 INTRODUCTION 2.1.1 PURPOSE The objective of the unit is to produce hydrogen by steam reforming of full range naphtha i.e. C 5-140 O C SR naphtha & coker naphtha to meet

More information

Plasma Gasification Facility

Plasma Gasification Facility Westinghouse Plasma Corporation Plasma Gasification Facility Westinghouse Plasma has over 30 years of experience in research, development, testing, design and commercial use of proven plasma torch technology.

More information

with Physical Absorption

with Physical Absorption meinschaft Mitglied der Helmholtz-Gem Pre-Combustion Carbon Capture with Physical Absorption Sebastian Schiebahn, Li Zhao, Marcus Grünewald 5. Juli 2011 IEK-3, Forschungszentrum Jülich, Germany ICEPE Frankfurt

More information

Gasification & Water Nexus

Gasification & Water Nexus Gasification & Water Nexus GTC Workshop on Gasification Technologies Denver, Colorado March 14, 2007 Richard D. Boardman, Ph.D. INL R&D Lead for Gasification & Alternative Fuels (208) 526-3083; Richard.Boardman@inl.gov

More information

Petroleum Coke Gasification Sweeny E-GasE. Gas Project

Petroleum Coke Gasification Sweeny E-GasE. Gas Project Petroleum Coke Gasification Sweeny E-GasE Gas Project Michael Culligan Manager, Sweeny Gasification Project Development October 7, 2008 1 Key Points ConocoPhillips believes gasification technology and

More information

Indirect Coal Liquefaction Better Solution to Clean Energy System

Indirect Coal Liquefaction Better Solution to Clean Energy System Indirect Coal Liquefaction Better Solution to Clean Energy System Yong-Wang Li, Director, Chief Scientist State Key Laboratory of Coal Conversion Institute of Coal Chemistry Chinese Academy of Sciences

More information

THE ASSESSMENT OF A WATER-CYCLE FOR CAPTURE OF CO2

THE ASSESSMENT OF A WATER-CYCLE FOR CAPTURE OF CO2 THE ASSESSMENT OF A WATER-CYCLE FOR CAPTURE OF CO2 Report Number PH3/4 November 1998 This document has been prepared for the Executive Committee of the Programme. It is not a publication of the Operating

More information

Eltron Research & Development

Eltron Research & Development Technology Readiness Level: 4 Component and/or Breadboard Validation in Laboratory Environment Eltron Research & Development Maximum, Economical CO2 Capture for IGCC Power Plants In partnership with the

More information

Coal Gasification Study

Coal Gasification Study AIChE National Design Competition Coal Gasification Study Process Design Report By: Kaitlyn D. Kelly March 7, 2008 Summary Rising oil prices and increased demand for chemical feedstock have added to the

More information

GoBiGas a First-of-a-kind-plant

GoBiGas a First-of-a-kind-plant GoBiGas a First-of-a-kind-plant Forrest Biomass to Biomethane (SNG) Henrik Thunman Chalmers University of Technology Gothenburg, Sweden Short Facts of the GoBiGas Demonstration-Plant Built, owned and operated

More information

Mk Plus The Next Generation Lurgi FBDB Gasification. Leipzig, 22/05/2012 Dr. Henrik Timmermann

Mk Plus The Next Generation Lurgi FBDB Gasification. Leipzig, 22/05/2012 Dr. Henrik Timmermann Mk Plus The Next Generation Lurgi FBDB Gasification Leipzig, 22/05/2012 Dr. Henrik Timmermann Outline Air Liquide E&C Perspective Next Generation Lurgi FBDB TM Gasification Lurgi FBDB Clean Conversion

More information

PRODUCTION OF SYNGAS BY METHANE AND COAL CO-CONVERSION IN FLUIDIZED BED REACTOR

PRODUCTION OF SYNGAS BY METHANE AND COAL CO-CONVERSION IN FLUIDIZED BED REACTOR PRODUCTION OF SYNGAS BY METHANE AND COAL CO-CONVERSION IN FLUIDIZED BED REACTOR Jinhu Wu, Yitain Fang, Yang Wang Institute of Coal Chemistry, Chinese Academy of Sciences P. O. Box 165, Taiyuan, 030001,

More information

Production of Electric Power and Chemicals in a Carbon Constrained Environment

Production of Electric Power and Chemicals in a Carbon Constrained Environment Production of Electric Power and Chemicals in a Carbon Constrained Environment Guido Collodi, Luca Mancuso, Federico Fazi Foster Wheeler Italiana SpA Via Caboto 1, 20094 Corsico Milan - Italy The Chemical

More information

Research and Development Program on HTTR Hydrogen Production System

Research and Development Program on HTTR Hydrogen Production System GENES4/ANP2003, Sep. 15-19, 2003, Kyoto, JAPAN Paper 1062 Research and Development Program on HTTR Hydrogen Production System Yoshiyuki INAGAKI, Tetsuo NISHIHARA, Tetsuaki TAKEDA, Koji HAYASHI, Yoshitomo

More information

Power Generation and Utility Fuels Group. Reynolds Frimpong Andy Placido Director: Kunlei Liu

Power Generation and Utility Fuels Group. Reynolds Frimpong Andy Placido Director: Kunlei Liu Power Generation and Utility Fuels Group Reynolds Frimpong Andy Placido Director: Kunlei Liu Gasification Background and Process Description Combustion vs. Gasification Combustion with oxygen Partial combustion

More information

Pre-Commercial Demonstration of High Efficiency, Low Cost Syngas Cleanup Technology for Chemical, Fuel, and Power Applications

Pre-Commercial Demonstration of High Efficiency, Low Cost Syngas Cleanup Technology for Chemical, Fuel, and Power Applications Pre-Commercial Demonstration of High Efficiency, Low Cost Syngas Cleanup Technology for Chemical, Fuel, and Power Applications 2012 Gasification Technologies Conference October 30, 2012 David Denton (speaker)

More information

EFFECTIVE WAY TO BOOST YOUR UREA PLANT CAPACITY - REVAMPING OF FERTIL UNIT

EFFECTIVE WAY TO BOOST YOUR UREA PLANT CAPACITY - REVAMPING OF FERTIL UNIT EFFECTIVE WAY TO BOOST YOUR UREA PLANT CAPACITY - REVAMPING OF FERTIL UNIT ALI ALIA Ruwais Fertilizer Industries (FERTIL) Abu Dhabi, United Arab Emirates PAOLO BERTINI Urea Casale S.A. Lugano, Switzerland

More information

CHOREN entrained flow gasification

CHOREN entrained flow gasification CHOREN entrained flow gasification update of technology and projects 9 th International Freiberg Conference June 2018 Berlin CHOREN Industrietechnik GmbH 德国科林工业技术有限责任公司 www.choren.com www.choren.cn Content

More information

Novel CO 2 Separation Technology Using MSM-1 Zeolite Membrane

Novel CO 2 Separation Technology Using MSM-1 Zeolite Membrane JOGMEC Techno Forum 2014 B-2 : R&D of JOGMEC and Japanese Companies (2) Novel CO 2 Separation Technology Using MSM-1 Zeolite Membrane (CO 2 Separation From Natural Gas) November 27 th, 2014 Kenichi Kawazuishi

More information

Handling of Trace Components for Rectisol Wash Units

Handling of Trace Components for Rectisol Wash Units Handling of Trace Components for Rectisol Wash Units Ulvi Kerestecioğlu, Thomas Haberle Washington DC, 08 th Oct. 2008 Rectisol Wash Unit in Jilin, China General Information about the Rectisol Process

More information