Report No. 35 BUTADIENE. March A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I PARK, CALIFORNIA

Size: px
Start display at page:

Download "Report No. 35 BUTADIENE. March A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I PARK, CALIFORNIA"

Transcription

1 Report No. 35 BUTADIENE by GEORGE E. HADDELAND March 1968 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA

2 CONTENTS 1 INTRODUCTION SUMMARY INDUSTRY STATUS... History... Butadiene Production... Raw Material Sources... Butadiene from Alcohol... Butadiene End Uses... Butadiene and Butane Prices... Butadiene Production Outside the United States... 4 CHEMISTRY... The Chemistry of C4 Hydrocarbons... Butadiene Properties and Structure... Butane and Butene Structure... The Chemistry of Butadiene Manufacture... Methods of Production... Commercial Routes to Butadiene... Butane and Butene Dehydrogenation... Reaction Products... Dehydrogenation Equilibria... Dehydrogenation Catalysts... Dehydrogenation Rates... C, Separation Methods... Fractional Distillation... Extractive Distillation... Solvent Efficiency in Extractive Distillation... 5 BUTADIENE BY DEHYDROGENATION OF BUTANE... Review of Processes... Phillips Two-Stage Process... Dehydrogenation Catalysts... Houdry Single Stage Process... Process Description... Process Discussion... Cost Estimates... Capital Costs... Production Costs... Discussion of Costs , iii

3 CONTENTS 6 BUTADIENE FROM REFINERY BUTENES... Historical Summary... Process Development... Catalyst Development... Purification... Review of Technology... Isobutene Separation... Feed Preparation... Dehydrogenation... Purification (Cuprous Ammonium Acetate)... Cuprous Ammonium Acetate Extraction Patents... Process Description... Isobutene Separation... Feed Preparation... Dehydrogenation... Purification... Process Discussion... Cost Estimates... Capital Costs... Production Costs... Discussion of Costs... 7 BUTADIENE, BY-PRODUCT OF NAPHTHA CRACKING... Background... Ethylene Production... By-Product Butadiene.... Process Technology... Process Description... Process Discussion... Cost Estimates... Capital Investment... Production Costs... Discussion of Costs BUTADIENE BY OXIDATIVE DEHYDROGENATION Background Oxidative Dehydrogenation of Butenes Advantages of Oxidative Dehydrogenation of Butenes Oxidative Dehydrogenation of Butane Butane Oxy-Halo-Dehydrogenation Review of Processes iv

4 CONTENTS 8 (continued) Catalytic and Noncatalytic Reactors Molten Acceptor Salt Reactor Fixed Acceptor Bed Reactor Fluidized Acceptor Bed Reactor Process Description Oxy-Halo-Dehydrogenation Acceptor Recovery Purification Process Discussion Oxy-Halo-Dehydrogenation Acceptor Recovery Purification Cost Estimates Capital Investment Production Costs Discussion of Costs SOLVENTS FOR C, SEPARATION Introduction Desirable Solvent Properties Comparison of Commercial Solvents Capital and Operating Costs for Several Solvents Other Solvents Azeotropic Distillation ACETYLENE REMOVAL FROM BUTADIENE Adverse Effects of Acetylenes... Acetylene Compounds... Amounts of Acetylenes... Specifications... Removal Methods... Selective Hydrogenation or Polymerization... Other Methods... Process Description... Process Discussion... Cost Estimates... Capital Investment... Production Costs... Discussion of Costs V

5 CONTENTS APPENDIX A DESIGN AND COST BASIS APPENDIX B PHYSICAL DATA APPENDIX C SPECIFICATIONS APPENDIX D MATERIALS OF CONSTRUCTION, HANDLING, SAFETY, AND POLLUTION CITED REFERENCES vi

6 ILLUSTRATIONS 3.1 Butadiene Production in the United States Some Reactions of Butadiene Equilibrium Constants for Reactions Involved in the Production of Butadiene Calculated Thermodynamic Equilibria for n-butane and n-butene Dehydrogenation at 1.0 Atm and 0.1 Atm Butadiene by Dehydrogenation of Butane Estimated Butadiene Total Production Costs for Various Plant Sizes, Operating Rates, and Raw Material Costs.., Equilibrium Curves for Isobutene in Hydrocarbon and 65% Sulfuric Acid Extraction Rate for Isobutene by 65% Sulfuric Acid Effect of Temperature upon the Absorption of Hydrocarbons in CAA Solution Schematic CAA Extraction Process Butadiene from Refinery Butenes Estimated Butadiene Net Production Cost for Various Plant Sizes, Operating Rates, Refinery Butenes Values and By-Product Credits Butadiene Separation: BASF Scheme Butadiene, By-Product of Naphtha Cracking Effect of Naphtha Raw Material Cost and Butene and Isobutene By-Product Credits on the Net Production Costs of Ethylene and Butadiene Change in Butadiene Net Production Cost with Ethylene and Butadiene Plant Capacities vii

7 ILLUSTRATIONS 7.5 Estimated Influence of Butadiene Feed Concentration upon Extraction Plant Investment and Butadiene Production cost Hydrogen Iodide Acceptor Systems Butadiene by the Oxy-Halo-Dehydrogenation of Butane Estimated Butadiene Production Cost by the Oxy-Halo- Dehydrogenation of Butane for Various Plant Sizes, Operating Rates, Butane Costs and Oxygen Costs Selective Hydrogenation of Acetylenes B.l Relative Volatilities, "a," of C, Hydrocarbons Relative to 1,3-Butadiene B.2 Relative Volatilities of C, Hydrocarbons in Acetone, Acetonitrile, and Furfural Solvents B.3 Acetonitrile--Water Liquid-Vapor Equilibrium B.4 Solubility of Iodine in Aqueous Hydrogen Iodide and in Water B.5 Vapor Pressures of Hydrogen and Iodine B.6 Solubilities of 1,3-Butadiene, l-butene, and n-butane in Dimethylformamide viii

8 TABLES Summary of Butadiene Processes Summary of Butadiene Purification Cost Components.... Butadiene Producers in the United States Percentage of Butadiene Production by Source United States Consumption of Butadiene Butadiene Producers outside the United States Estimated Butadiene Consumption outside the United States 33 Commercial Routes to Butadiene Catalytic Dehydrogenation of n-butane or n-butane- Butylene Mixtures Summary of Patents A Comparison of Dehydrogenation Catalysts Butadiene by Dehydrogenation of Butane Major Process Equipment and Utilities Summary Butadiene by Dehydrogenation of Butane Stream Flows Butadiene by Dehydrogenation of Butane Process Unit and Utilities Investment Butadiene by Dehydrogenation of Butane Total Capital Investment Butadiene by Dehydrogenation of Butane Production Costs A Comparison of Butene Dehydrogenation Catalysts Catalytic Dehydrogenation of Butenes Summary of Patents ix

9 TABLES 6.3 Butadiene from Refinery Butenes Major Process Equipment and Utilities Summary Butadiene from Refinery Butenes Stream Flows Butadiene from Refinery Butenes Process Unit and Utilities Investment Butadiene from Refinery Butenes Total Capital Investment Butadiene from Refinery Butenes Production Costs Estimated Capital and Operating Costs for Ethylene Typical Yields from Commercial Fired Tubular Heaters Butadiene By-Product of Naphtha Cracking Major Process Equipment and Utilities Summary Butadiene By-Product of Naphtha Cracking Stream Flows Butadiene By-Product of Naphtha Cracking Process Unit and Utilities Investment Butadiene By-Product of Naphtha Cracking Total Capital Investment Butadiene By-Product of Naphtha Cracking Production Costs Oxidative Dehydration of n-butane and Butenes Summary of Patents Butadiene by Oxidative Dehydrogenation of Butenes Summary of Recently Published Research...., Oxy-Halo-Dehydrogenation of Butane and Butenes Summary of Patents.....,

10 TABLES B.l B.2 Butadiene by Oxy-Halo-Dehydrogenation of n-butane Summary of U.S.S.R. Research Butadiene by the Oxy-Halo-Dehydrogenation of Butane Major Process Equipment and Utilities Summary Butadiene by the Oxy-Halo-Dehydrogenation of Butane Stream Flows Butadiene by the Oxy-Halo-Dehydrogenation of Butane Process Unit and Utilities Investment Butadiene by the Oxy-Halo-Dehydrogenation of Butane Total Capital Investment Butadiene by the Oxy-Halo-Dehydrogenation of Butane Production Costs Physical Properties of Solvents for C, Separations Summary of Capital and Operating Costs for Preceding C, Separations Destruction of Acetylenes in Butadiene by Selective Hydrogenation or Polymerization Summary of Patents Selective Hydrogenation of Acetylenes Major Process Equipment, Utilities Summary, and Stream Flows Selective Hydrogenation of Acetylenes Process Unit and Utilities Investment Selective Hydrogenation of Acetylenes Production Costs Comparative Costs for Solvent Extraction of Acetylenes Physical Properties of 1,3-Butadiene Houdry Chrome-Alumina Catalyst Typical Properties Xi

11 TABLES B.3 Hydrocarbon Relative Volatilities B.4 Physical Properties of Extractive Distillation Solvents. 241 B.5 Properties of Cuprous Ammonium Acetate Solution B.6 Solubilities of Hydrocarbons in N-Methylpyrrolidone xii

ETHYLENE-PROPYLENE PROCESS ECONOMICS PROGRAM. Report No. 29A. Supplement A. by SHIGEYOSHI TAKAOKA With contributions by KIICHIRO OHYA.

ETHYLENE-PROPYLENE PROCESS ECONOMICS PROGRAM. Report No. 29A. Supplement A. by SHIGEYOSHI TAKAOKA With contributions by KIICHIRO OHYA. Report No. 29A ETHYLENE-PROPYLENE Supplement A by SHIGEYOSHI TAKAOKA With contributions by KIICHIRO OHYA March 1971 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO

More information

ACRYLICACID AND ACRYLIC ESTERS

ACRYLICACID AND ACRYLIC ESTERS Report No. 6A ACRYLICACID AND ACRYLIC ESTERS Supplement A by RICHARD G. DENNEY April 1967 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA CONTENTS

More information

PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM 7 Report No. 34 PHTHALIC ANHYDRIDE by LLOYD M. ELKIN contributions by Kenneth E. Lunde March 1968 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA CONTENTS

More information

PEP Review ON-PURPOSE BUTADIENE PRODUCTION By Richard Nielsen with a Contribution by Russell Heinen (June 2011)

PEP Review ON-PURPOSE BUTADIENE PRODUCTION By Richard Nielsen with a Contribution by Russell Heinen (June 2011) PEP Review 2011-05 ON-PURPOSE BUTADIENE PRODUCTION By Richard Nielsen with a Contribution by Russell Heinen (June 2011) ABSTRACT 1,3-Butadiene is currently almost entirely produced as a by-product of ethylene

More information

OX0 ALCOHOLS PROCESS ECONOMICS PROGRAM. Report No. 21. contributions by Shigeyoshi Takaoka. November A private report by the

OX0 ALCOHOLS PROCESS ECONOMICS PROGRAM. Report No. 21. contributions by Shigeyoshi Takaoka. November A private report by the Report No. 21 OX0 ALCOHOLS by RICHARD G. DENNEY contributions by Shigeyoshi Takaoka November 1966 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO PARK, CALIFORNIA

More information

AROMATIC AMINES PROCESS ECONOMICS PROGRAM. Report No. 76Al Interim. by YEN-CHEN. July A private report by the MENLO PARK, CALIFORNIA

AROMATIC AMINES PROCESS ECONOMICS PROGRAM. Report No. 76Al Interim. by YEN-CHEN. July A private report by the MENLO PARK, CALIFORNIA Report No. 76Al Interim AROMATIC AMINES by YEN-CHEN YEN July 1975 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA CONTENTS 1 INTRODUCTION........................

More information

XYLENES SEPARATION SUPPLEMENT

XYLENES SEPARATION SUPPLEMENT Report No. 25A XYLENES SEPARATION SUPPLEMENT A by HAROLD C. RIES July 1970 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO PARK, CALIFORNIA CONTENTS INTRODUCTION,..,....................

More information

Abstract Process Economics Program Report No. 203 ALKANE DEHYDROGENATION AND AROMATIZATION (September 1992)

Abstract Process Economics Program Report No. 203 ALKANE DEHYDROGENATION AND AROMATIZATION (September 1992) Abstract Process Economics Program Report No. 203 ALKANE DEHYDROGENATION AND AROMATIZATION (September 1992) Propylene, isobutene, and BTX (benzene, toluene, and xylenes) have traditionally been recovered

More information

Abstract Process Economics Program Report 21F NEW GENERATION OXO ALCOHOLS (October 2012)

Abstract Process Economics Program Report 21F NEW GENERATION OXO ALCOHOLS (October 2012) Abstract Process Economics Program Report 21F NEW GENERATION OXO ALCOHOLS (October 2012) This report follows a series of Process Economics Program reports on the topic of oxo alcohols. The last report

More information

Abstract Process Economics Program Report No. 158A OCTANE IMPROVERS FOR GASOLINE (February 1992)

Abstract Process Economics Program Report No. 158A OCTANE IMPROVERS FOR GASOLINE (February 1992) Abstract Process Economics Program Report No. 158A OCTANE IMPROVERS FOR GASOLINE (February 1992) Lead phaseout in the United States has brought about a strong interest in oxygenated octane improvers for

More information

ISOMERIZATION OF PARAFFINS FOR GASOLINE

ISOMERIZATION OF PARAFFINS FOR GASOLINE Report No. 91 ISOMERIZATION OF PARAFFINS FOR GASOLINE by EARL D. OLIVER and RYOSUKE HASHIMOTO OCTOBER 1974 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA

More information

PROTEINS FROM HYDROCARBONS

PROTEINS FROM HYDROCARBONS Report No. 60 PROTEINS FROM HYDROCARBONS by WING SIEN FONG February 19 70 A private report by the - PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO PARK, CALIFORNIA CONTENTS 1 INTRODUCTION...,...............

More information

DIOXIDE REMOVAL FROM STACK GASES

DIOXIDE REMOVAL FROM STACK GASES Report No. 63 SULFUR DIOXIDE REMOVAL FROM STACK GASES by EARL D. OLIVER July 1970 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA CONTENTS 1 INTRODUCTION.......,.................

More information

CONTENTS 1 INTRODUCTION SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2

CONTENTS 1 INTRODUCTION SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2 CONTENTS GLOSSARY xxiii 1 INTRODUCTION 1-1 2 SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2 3 INDUSTRY STATUS 3-1 TRENDS IN TRANSPORTATION FUEL DEMAND 3-3 TRENDS IN ENVIRONMENTAL REGULATION 3-3

More information

HYDROFLUORIC ACID FLUOROCARBONS AND PROCESS ECONOMICS PROGRAM. Report No. 89. November A private report by the MENLO PARK, CALIFORNIA

HYDROFLUORIC ACID FLUOROCARBONS AND PROCESS ECONOMICS PROGRAM. Report No. 89. November A private report by the MENLO PARK, CALIFORNIA Report No. 89 HYDROFLUORIC ACID FLUOROCARBONS AND by HAROLD W. SCHEELINE November 1973 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO PARK, CALIFORNIA -. _ CONTENTS

More information

PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM PROCESS ECONOMICS PROGRAM Abstract Process Economics Program Report No. 29C SRI INTERNATIONAL Menlo Park, California 94025 ETHYLENE PLANT CONVERSION (July 1985) This report deals with the technology and

More information

PEP Review METHYL TERTIARY BUTYL ETHER PRODUCTION FROM STEAM CRACKER C 4 STREAM By Syed N. Naqvi (December 2012)

PEP Review METHYL TERTIARY BUTYL ETHER PRODUCTION FROM STEAM CRACKER C 4 STREAM By Syed N. Naqvi (December 2012) PEP Review 2012-07 METHYL TERTIARY BUTYL ETHER PRODUCTION FROM STEAM CRACKER C 4 STREAM By Syed N. Naqvi (December 2012) ABSTRACT This Review presents a technoeconomic evaluation of a methyl tertiary butyl

More information

Process Economics Program

Process Economics Program IHS Chemical Process Economics Program Report 290 Bio-Butadiene By Dipti Dave and Susan Bell December 2014 ihs.com/chemical IHS Chemical agrees to assign professionally qualified personnel to the preparation

More information

ALIPHATIC SURFACTANTS

ALIPHATIC SURFACTANTS Report No. 59 ALIPHATIC SURFACTANTS by MIKIO KUMAGAI and SHIGEYOSHI TAKAOKA December 1969 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO PARK, CALIFORNIA CONTENTS

More information

PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM PROCESS ECONOMICS PROGRAM Abstract Process Economics Program Report No. 158 SRI INTERNATIONAL Menlo Park, California 94025 OCTANE IMPROVERS FOR GASOLINE (November 1983) There la currently worldwide interest

More information

Abstract Process Economics Program Report 43D MEGA METHANOL PLANTS (December 2003)

Abstract Process Economics Program Report 43D MEGA METHANOL PLANTS (December 2003) Abstract Process Economics Program Report 43D MEGA METHANOL PLANTS (December 2003) World scale, grass roots methanol plants currently have production capacities as high as 3,000 metric tons per day. A

More information

Stephen Stanley Jose de Barros Fred Gardner Lummus Technology 1 st Indian Oil Petrochemical Conclave March 16, 2012 New Delhi

Stephen Stanley Jose de Barros Fred Gardner Lummus Technology 1 st Indian Oil Petrochemical Conclave March 16, 2012 New Delhi Increasing Petrochemicals Project Earnings by Upgrading Steam Cracker C4s and C5s Stephen Stanley Jose de Barros Fred Gardner Lummus Technology 1 st Indian Oil Petrochemical Conclave March 16, 2012 New

More information

LINEAR POLYETHYLENE AND POLYPROPYLENE

LINEAR POLYETHYLENE AND POLYPROPYLENE Report No. 19-A LINEAR POLYETHYLENE AND POLYPROPYLENE Supplement A by ROBERT Consultant L. MAGOVERN October 1969 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK,

More information

Abstract Process Economics Program Report 251 BIODIESEL PRODUCTION (November 2004)

Abstract Process Economics Program Report 251 BIODIESEL PRODUCTION (November 2004) Abstract Process Economics Program Report 251 BIODIESEL PRODUCTION (November 2004) Biodiesel is an ester of fatty acids produced from renewable resources such as virgin vegetable oil, animal fats and used

More information

IHS CHEMICAL PEP Report 29J. Steam Cracking of Crude Oil. Steam Cracking of Crude Oil. PEP Report 29J. Gajendra Khare Principal Analyst

IHS CHEMICAL PEP Report 29J. Steam Cracking of Crude Oil. Steam Cracking of Crude Oil. PEP Report 29J. Gajendra Khare Principal Analyst ` IHS CHEMICAL PEP Report 29J Steam Cracking of Crude Oil December 2015 ihs.com PEP Report 29J Steam Cracking of Crude Oil Gajendra Khare Principal Analyst Michael Arné Sr. Principal Analyst PEP Report

More information

IHS CHEMICAL Light Hydrocarbon and Light Naphtha Utilization. Process Economics Program Report 297. Light Hydrocarbon and Light Naphtha Utilization

IHS CHEMICAL Light Hydrocarbon and Light Naphtha Utilization. Process Economics Program Report 297. Light Hydrocarbon and Light Naphtha Utilization ` IHS CHEMICAL Light Hydrocarbon and Light Naphtha Utilization Process Economics Program Report 297 September 2016 ihs.com PEP Report 297 Light Hydrocarbon and Light Naphtha Utilization Girish Ballal Principal

More information

PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California

PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California Abstract Process Economics Program Report No. 169 REFINERY/CHEMICALS INTERFACE (January 1985) Demand for most major refinery products

More information

ACRYLONITRILE THERMOPLASTICS

ACRYLONITRILE THERMOPLASTICS Report No. 78 ACRYLONITRILE THERMOPLASTICS by ROBERT H. SCHWAAB August 1972 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA CONTENTS 1 INTRODUCTION,........................

More information

TREATMENTOF PETROCHEMICAL WASTEWATERS

TREATMENTOF PETROCHEMICAL WASTEWATERS Report No. 80 TREATMENTOF PETROCHEMICAL WASTEWATERS by EARL D. OLIVER September 1972 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I I MENLO PARK, CALIFORNIA CONTENTS 1

More information

Abstract PEP Review PROCESS ECONOMICS OF COAL-BASED OLEFINS PRODUCTION IN CHINA By R. J. Chang and Jamie Lacson (May 2012)

Abstract PEP Review PROCESS ECONOMICS OF COAL-BASED OLEFINS PRODUCTION IN CHINA By R. J. Chang and Jamie Lacson (May 2012) Abstract PEP Review 2012-04 PROCESS ECONOMICS OF COAL-BASED OLEFINS PRODUCTION IN CHINA By R. J. Chang and Jamie Lacson (May 2012) ABSTRACT China has started or planned several large commercial projects

More information

Process Economics Program

Process Economics Program IHS Chemical Process Economics Program Report 291 Aromatics from Light Hydrocarbons By Syed Naqvi November 2014 ihs.com/chemical IHS Chemical agrees to assign professionally qualified personnel to the

More information

Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES

Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES 1 Physical and chemical processes Physical Thermal Chemical Catalytic Distillation Solvent extraction Propane deasphalting Solvent dewaxing

More information

Abstract Process Economics Program Report 195A ADVANCES IN FLUID CATALYTIC CRACKING (November 2005)

Abstract Process Economics Program Report 195A ADVANCES IN FLUID CATALYTIC CRACKING (November 2005) Abstract Process Economics Program Report 195A ADVANCES IN FLUID CATALYTIC CRACKING (November 2005) Recent emphasis in fluid catalytic cracking is on maximum light olefins production, gasoline sulfur reduction

More information

Abstract Process Economics Program Report 211A HYDROCRACKING FOR MIDDLE DISTILLATES (July 2003)

Abstract Process Economics Program Report 211A HYDROCRACKING FOR MIDDLE DISTILLATES (July 2003) Abstract Process Economics Program Report 211A HYDROCRACKING FOR MIDDLE DISTILLATES (July 2003) Middle distillate is the collective petroleum distillation fractions boiling above naphtha (about 300 F,

More information

PEP Review HIGH-PURITY ISOBUTYLENE PRODUCTION BY MTBE CRACKING By Sumod Kalakkunnath (December 2012)

PEP Review HIGH-PURITY ISOBUTYLENE PRODUCTION BY MTBE CRACKING By Sumod Kalakkunnath (December 2012) PEP Review 2012-06 HIGH-PURITY ISOBUTYLENE PRODUCTION BY MTBE CRACKING By Sumod Kalakkunnath (December 2012) ABSTRACT This Review presents a technoeconomic evaluation of an isobutylene from methyl tertiary

More information

Reliable. Efficient. Economical. Distillation Technology ENGINEERING - EQUIPMENT - TURNKEY SYSTEMS

Reliable. Efficient. Economical. Distillation Technology ENGINEERING - EQUIPMENT - TURNKEY SYSTEMS TM Economical Efficient Reliable Distillation Technology ENGINEERING - EQUIPMENT - TURNKEY SYSTEMS DISTILLATION TECHNOLOGY Distillation is by far the most important separation process in the petroleum

More information

Production of Dimethyl Ether

Production of Dimethyl Ether Production of Dimethyl Ether Background A feasibility study on the production of 99.5 wt% dimethyl ether (DME) is to be performed. The plant is capable of producing 50,000 metric tons of DME per year via

More information

Preface... xii. 1. Refinery Distillation... 1

Preface... xii. 1. Refinery Distillation... 1 Preface... xii Chapter Breakdown... xiii 1. Refinery Distillation... 1 Process Variables... 2 Process Design of a Crude Distillation Tower... 5 Characterization of Unit Fractionation... 11 General Properties

More information

Unipar Oxo Alcohols Plant. Start Up: August, 1984 Location: Mauá - São Paulo - Brasil. Nameplate Capacity:

Unipar Oxo Alcohols Plant. Start Up: August, 1984 Location: Mauá - São Paulo - Brasil. Nameplate Capacity: page 1 Unipar Oxo Alcohols Plant Start Up: August, 1984 Location: Mauá - São Paulo - Brasil Nameplate Capacity:! Oxo plant: 33 KTA in Isodecyl Alcohol [6 t/day of Isodecyl Alcohol or 70 t/day of Tridecyl

More information

PEP Review HIGH-PURITY ISOBUTYLENE FROM T-BUTANOL BY LYONDELLBASELL PROCESS By Sumod Kalakkunnath (February 2013)

PEP Review HIGH-PURITY ISOBUTYLENE FROM T-BUTANOL BY LYONDELLBASELL PROCESS By Sumod Kalakkunnath (February 2013) PEP Review 2013-06 HIGH-PURITY ISOBUTYLENE FROM T-BUTANOL BY LYONDELLBASELL PROCESS By Sumod Kalakkunnath (February 2013) ABSTRACT This Review presents a technoeconomic evaluation of an isobutylene from

More information

CONTENTS. Chapter 1 Industrial Catalysts. Chapter 2 The First Catalysts

CONTENTS. Chapter 1 Industrial Catalysts. Chapter 2 The First Catalysts CONTENTS Chapter 1 Industrial Catalysts 1.1 Introduction 1 1.2 What is a Catalyst? 5 1.2.1 Activity 6 1.2.2 Selectivity and Yield 7 1.2.3 Stability 7 1.2.4 Strength 8 1.3 Catalyst Production 8 1.3.1 Precipitation

More information

WORLDWIDE REFINERY PROCESSING REVIEW. Fourth Quarter 2009

WORLDWIDE REFINERY PROCESSING REVIEW. Fourth Quarter 2009 WORLDWIDE REFINERY PROCESSING REVIEW Monitoring Technology Development and Competition in One Single Source Fourth Quarter 2009 HYDROCARBON PUBLISHING COMPANY Translating Knowledge into Profitability SM

More information

IHS CHEMICAL High Olefins Fluid Catalytic Cracking Processes. Process Economics Program Report 195B. High Olefins Fluid Catalytic Cracking Processes

IHS CHEMICAL High Olefins Fluid Catalytic Cracking Processes. Process Economics Program Report 195B. High Olefins Fluid Catalytic Cracking Processes ` IHS CHEMICAL High Olefins Fluid Catalytic Cracking Processes Process Economics Program Report 195B November 2016 ihs.com PEP Report 195B High Olefins Fluid Catalytic Cracking Processes Mike Kelly Sr.

More information

Distillation process of Crude oil

Distillation process of Crude oil Distillation process of Crude oil Abdullah Al Ashraf; Abdullah Al Aftab 2012 Crude oil is a fossil fuel, it was made naturally from decaying plants and animals living in ancient seas millions of years

More information

Fig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy Agency.)[16,17]

Fig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy Agency.)[16,17] Introduction :Composition of petroleum,laboratory tests,refinery feedstocks and products Fig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy

More information

POLYAMIDES OTHER THAN NYLONS 6 AND 66

POLYAMIDES OTHER THAN NYLONS 6 AND 66 Report No. 94 POLYAMIDES OTHER THAN NYLONS 6 AND 66 PART I by YEN-CHEN YEN November 1974 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA CONTENTS,

More information

CHAPTER 3 OIL REFINERY PROCESSES

CHAPTER 3 OIL REFINERY PROCESSES CHAPTER 3 OIL REFINERY PROCESSES OUTLINE 1. Introduction 2. Physical Processes 3. Thermal Processes 4. Catalytic Processes 5. Conversion of Heavy Residues 6. Treatment of Refinery Gas Streams INTRODUCTION

More information

Catalytic Reforming for Aromatics Production. Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC 1

Catalytic Reforming for Aromatics Production. Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC 1 Catalytic Reforming for Aromatics Production Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC GAM Engineering LLC 1 REFINERY CONFIURATION LPG NAPHTHA HYDROTREATING

More information

Fischer-Tropsch Refining

Fischer-Tropsch Refining Fischer-Tropsch Refining by Arno de Klerk A thesis submitted in partial fulfillment of the requirements for the degree Philosophiae Doctor (Chemical Engineering) in the Department of Chemical Engineering

More information

Brief Summary of the Project

Brief Summary of the Project Brief Summary of the Project 1. BackGround: HPCL Mittal Energy Limited (HMEL) currently operates a 9.0 MMTPA Guru Gobind Singh Refinery in Bathinda-Punjab, supplying EURO-III and EURO-IV compliant fuels

More information

AlkyClean Solid Acid Alkylation

AlkyClean Solid Acid Alkylation Development of a Solid Acid Catalyst Alkylation Process AlkyClean Solid Acid Alkylation October 6, 2006-1 - AlkyClean solid acid alkylation Presentation Outline Introduction Process Development Demonstration

More information

Process Economics Program

Process Economics Program IHS Chemical Process Economics Program Report 247C Land-Based Small-Scale GTL By Ron Smith December 2014 ihs.com/chemical IHS Chemical agrees to assign professionally qualified personnel to the preparation

More information

Catalysts for olefin processes. A range of performance catalysts and absorbents for use across the olefins value chain.

Catalysts for olefin processes. A range of performance catalysts and absorbents for use across the olefins value chain. Catalysts for olefin processes A range of performance catalysts and absorbents for use across the olefins value chain. Information contained in this publication or as otherwise supplied to Users is believed

More information

Petroleum Refining Fourth Year Dr.Aysar T. Jarullah

Petroleum Refining Fourth Year Dr.Aysar T. Jarullah Catalytic Reforming Catalytic reforming is the process of transforming C 7 C 10 hydrocarbons with low octane numbers to aromatics and iso-paraffins which have high octane numbers. It is a highly endothermic

More information

Abstract Process Economics Program Report 246 NEAR ZERO SULFUR DIESEL FUEL (November 2002)

Abstract Process Economics Program Report 246 NEAR ZERO SULFUR DIESEL FUEL (November 2002) Abstract Process Economics Program Report 246 NEAR ZERO SULFUR DIESEL FUEL (November 2002) Desulfurization of diesel fuel is growing worldwide into a process critical to petroleum refinery profitability.

More information

On-Line Process Analyzers: Potential Uses and Applications

On-Line Process Analyzers: Potential Uses and Applications On-Line Process Analyzers: Potential Uses and Applications INTRODUCTION The purpose of this report is to provide ideas for application of Precision Scientific process analyzers in petroleum refineries.

More information

Acrolein from propylene and oxygen from air [ ]

Acrolein from propylene and oxygen from air [ ] Acrolein from propylene and oxygen from air [107-02-8] CONTENTS OF FACTORY GATE TO FACTORY GATE LIFE CYCLE INVENTORY SUMMARY Chemistry... 2 Process Summary... 3 Summary of LCI Information... 5 Process

More information

KBR Technology Business

KBR Technology Business KBR Technology Business Tanya Niu ------ Director, Chemicals 2013 Ethane to Ethylene Global Summit, Houston, TX Oct 30 th 2013 KBR, Inc. All Rights Reserved 1 KBR Technology Portfolio Refining ROSE Visbreaking

More information

PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Mod0 Park, California 94025 Abstract Process Economics Program Report No. 1C ISOCYANATES/POLYISOCYANATES In this supplementary report, several processes for

More information

HOW OIL REFINERIES WORK

HOW OIL REFINERIES WORK HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on

More information

Process Economics Program

Process Economics Program IHS Chemical Process Economics Program Review 2013-10 Adipic Acid from Free Fatty Acids via Verdezyne Fermentation By Anthony Pavone IHS Chemical agrees to assign professionally qualified personnel to

More information

Annex A: General Description of Industry Activities

Annex A: General Description of Industry Activities Annex A: General Description of Industry Activities 65. The EHS Guidelines for Petroleum Refining cover processing operations from crude oil to finished liquid products, including liquefied petroleum gas

More information

Alkylation & Polymerization Chapter 11

Alkylation & Polymerization Chapter 11 Alkylation & Polymerization Chapter 11 Petroleum Refinery Schematic Gasses Polymerization Sulfur Plant Sulfur Gas Sat Gas Plant Alkyl Feed Butanes LPG Fuel Gas Alkylation LPG Gas Separation & Stabilizer

More information

HOW OIL REFINERIES WORK

HOW OIL REFINERIES WORK HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on

More information

Refining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing Engineered to Innovate

Refining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing Engineered to Innovate Refining/Petrochemical Integration-A New Paradigm Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals

More information

Results Certified by Core Labs for Conoco Canada Ltd. Executive summary. Introduction

Results Certified by Core Labs for Conoco Canada Ltd. Executive summary. Introduction THE REPORT BELOW WAS GENERATED WITH FEEDSTOCK AND PRODUCT SAMPLES TAKEN BY CONOCO CANADA LTD, WHO USED CORE LABORATORIES, ONE OF THE LARGEST SERVICE PROVIDERS OF CORE AND FLUID ANALYSIS IN THE PETROLEUM

More information

SOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins

SOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins SOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins ME Tech Dubai, February 18 & 19, 2014 Steve Beeston - Vice President, Technology Business Environment Requirements Improve refinery

More information

PEP Review CONTINUOUS SAP PRODUCTION VIA DOUBLE KNEADER REACTOR By Anthony Pavone (November 2011)

PEP Review CONTINUOUS SAP PRODUCTION VIA DOUBLE KNEADER REACTOR By Anthony Pavone (November 2011) PEP Review 2011-12 CONTINUOUS SAP PRODUCTION VIA DOUBLE KNEADER REACTOR By Anthony Pavone (November 2011) ABSTRACT Superabsorbent polymer (SAP) is a partially neutralized homo-polymer of glacial acrylic

More information

Unit 1. Naphtha Catalytic Reforming. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna

Unit 1. Naphtha Catalytic Reforming. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna Unit 1. Naphtha Catalytic Reforming Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna Introduction Catalytic reforming of heavy naphtha and isomerization of light naphtha constitute

More information

Bottom of Barrel Processing. Chapters 5 & 8

Bottom of Barrel Processing. Chapters 5 & 8 Bottom of Barrel Processing Chapters 5 & 8 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha

More information

CONVERSION OF GLYCEROL TO GREEN METHANOL IN SUPERCRITICAL WATER

CONVERSION OF GLYCEROL TO GREEN METHANOL IN SUPERCRITICAL WATER CONVERSION OF GLYCEROL TO GREEN METHANOL IN SUPERCRITICAL WATER Maša Knez Hrnčič, Mojca Škerget, Ljiljana Ilić, Ţeljko Knez*, University of Maribor, Faculty of Chemistry and Chemical Engineering, Laboratory

More information

Refining/Petrochemical Integration-A New Paradigm

Refining/Petrochemical Integration-A New Paradigm Refining/Petrochemical Integration-A New Paradigm Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals

More information

Crude Distillation Chapter 4

Crude Distillation Chapter 4 Crude Distillation Chapter 4 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha Isomerization

More information

HOW OIL REFINERIES WORK

HOW OIL REFINERIES WORK HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on

More information

Handbook of Petroleum Processing

Handbook of Petroleum Processing Handbook of Petroleum Processing Handbook of Petroleum Processing Edited by DAVID S. J. STAN JONES retired chemical engineer (Fluor) Calgary, Canada and PETER R. PUJADÓ UOP LLC (retired)-illinois, U.S.A.

More information

ON-PURPOSE PROPYLENE FROM OLEFINIC STREAMS

ON-PURPOSE PROPYLENE FROM OLEFINIC STREAMS 1 ON-PURPOSE PROPYLENE FROM OLEFINIC STREAMS Michael W. Bedell ExxonMobil Process Research Laboratories Baton Rouge, La Philip A. Ruziska ExxonMobil Chemical Company Baytown, TX Todd R. Steffens ExxonMobil

More information

WINTER-15 EXAMINATION Model Answer

WINTER-15 EXAMINATION Model Answer Subject code :(17651) Page 1 of 6 Important Instructions to examiners: 1) The answers should be examined by key words and not as word-to-word as given in the model answer scheme. ) The model answer and

More information

GTC TECHNOLOGY WHITE PAPER

GTC TECHNOLOGY WHITE PAPER GTC TECHNOLOGY WHITE PAPER Refining/Petrochemical Integration FCC Gasoline to Petrochemicals Refining/Petrochemical Integration - FCC Gasoline to Petrochemicals Introduction The global trend in motor fuel

More information

Alcohols to Hydrocarbons (ATH)

Alcohols to Hydrocarbons (ATH) Alcohols to Hydrocarbons (ATH) Advanced Bioeconomy Leadership Conference 6 th Annual Aviation & Military Biofuels Summit Washington, D.C. Friday March 13th 2015 Forward-Looking Statements Certain statements

More information

Investment Planning of an Integrated Petrochemicals Complex & Refinery A Best Practice Approach

Investment Planning of an Integrated Petrochemicals Complex & Refinery A Best Practice Approach Investment Planning of an Integrated Petrochemicals Complex & Refinery A Best Practice Approach RPTC, Moscow, 19 September 2012 David Gibbons Principal Process Consultant Foster Wheeler. All rights reserved.

More information

Abstract Process Economics Program Report 222 PETROLEUM INDUSTRY OUTLOOK (July 1999)

Abstract Process Economics Program Report 222 PETROLEUM INDUSTRY OUTLOOK (July 1999) Abstract Process Economics Program Report 222 PETROLEUM INDUSTRY OUTLOOK (July 1999) Global energy demand is rising, with fossil fuels oil, natural gas, and coal continuing to provide more than 90% of

More information

The Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels. 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004

The Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels. 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004 The Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004 Dennis Sullivan UOP LLC The specifications for transportation

More information

Zeolite Catalyst. Methanol. Propylene. Petrochemical Research & Technology پژوهش و فناوري پتروشیمی

Zeolite Catalyst. Methanol. Propylene.  Petrochemical Research & Technology پژوهش و فناوري پتروشیمی NPC-RT Propylene via Methanol Technology Methanol Zeolite Catalyst December 2016 Propylene ١ Natural Gas Value Chain Methanol Demand & Supply Methanol and Propylene Price Overview of NPC-RT PVM Technology

More information

Dimethyl Ether Production Material Balances

Dimethyl Ether Production Material Balances Dimethyl Ether Production Material Balances Dimethyl ether (DME) is used primarily as a propellant. It is miscible with most organic solvents and has high solubility with water. Recently, the use of DME

More information

GTC Technology Day. 16 April Hotel Le Meridien New Delhi. Isomalk Technologies for Light Naphtha Isomerization

GTC Technology Day. 16 April Hotel Le Meridien New Delhi. Isomalk Technologies for Light Naphtha Isomerization 16 April Hotel Le Meridien New Delhi Isomalk Technologies for Light Naphtha Isomerization Naphtha Processing Technology by GTC n-c4 Isomalk-3 i-c4 Light Naphtha Isomalk-2 C5/C6 Isomerate C7 Paraffins Isomalk-4

More information

Petroleum Refining Fourth Year Dr.Aysar T. Jarullah

Petroleum Refining Fourth Year Dr.Aysar T. Jarullah Catalytic Operations Fluidized Catalytic Cracking The fluidized catalytic cracking (FCC) unit is the heart of the refinery and is where heavy low-value petroleum stream such as vacuum gas oil (VGO) is

More information

Where We Are. Today: Finish up Chapter 4, hopefully! Discussion: Alternative fuels, the benefits of conservation Where to go next?

Where We Are. Today: Finish up Chapter 4, hopefully! Discussion: Alternative fuels, the benefits of conservation Where to go next? Where We Are Today: Finish up Chapter 4, hopefully! Discussion: Alternative fuels, the benefits of conservation Where to go next? Thursday: Start in on Chapter 5, The Water We Drink. Quiz! NEXT Thursday:

More information

Maximizing Refinery Margins by Petrochemical Integration

Maximizing Refinery Margins by Petrochemical Integration Topic Maximizing Refinery Margins by Petrochemical Integration Presented by : Rajeev Singh Global Demand for Refined Products 29% 29% 29% 29% 30% 30% 33% 10% 10% 10% 9% 8% 8% 7% 7% 7% 7% 7% 7% 7% 22% 22%

More information

Innovative Solutions for Optimizing Refining & Petrochemicals Synergies. Jean-Paul Margotin

Innovative Solutions for Optimizing Refining & Petrochemicals Synergies. Jean-Paul Margotin Innovative Solutions for Optimizing Refining & Petrochemicals Synergies Jean-Paul Margotin 1 Agenda Refining & Petrochemical (R&P) synergies: Flow exchanges R&P synergies for olefins production Propylene

More information

PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM PROCESS ECONOMICS PROGRAM Abstract SRI INTERNATIONAL Mado Park, California 94025 Process Economics Program Report No. 170 SWEETENERS (September 1984) Low calorie and nonnutritive sweeteners, once used

More information

Appendix A.1 Calculations of Engine Exhaust Gas Composition...9

Appendix A.1 Calculations of Engine Exhaust Gas Composition...9 Foreword...xi Acknowledgments...xiii Introduction... xv Chapter 1 Engine Emissions...1 1.1 Characteristics of Engine Exhaust Gas...1 1.1.1 Major Components of Engine Exhaust Gas...1 1.1.2 Units Used for

More information

White Paper.

White Paper. The Advantage of Real Atmospheric Distillation Complying with the ASTM D7345 Test Method in the Distillation Process Introduction / Background In the past, refiners enjoyed a constant supply of the same

More information

Course: Chemical Technology (Organic) Lecture 7 Alkylation, Isomerisation And Polymerisation

Course: Chemical Technology (Organic) Lecture 7 Alkylation, Isomerisation And Polymerisation Course: Chemical Technology (Organic) Module VI Lecture 7 Alkylation, Isomerisation And Polymerisation LECTURE 7 ALKYLATION, ISOMERISATION AND POLYMERISATION ALKYLATION Alkylation process commercialized

More information

clean Efforts to minimise air pollution have already led to significant reduction of sulfur in motor fuels in the US, Canada, Keeping it

clean Efforts to minimise air pollution have already led to significant reduction of sulfur in motor fuels in the US, Canada, Keeping it Maurice Korpelshoek, CDTECH, The Netherlands, and Kerry Rock and Rajesh Samarth, CDTECH, USA, discuss sulfur reduction in FCC gasoline without octane loss. Keeping it clean without affecting quality Efforts

More information

Molecular Sieves Application Guide for the Natural Gas Industry Molecular Sieve Molecular Sieve Recommendations

Molecular Sieves Application Guide for the Natural Gas Industry Molecular Sieve Molecular Sieve Recommendations Application Guide for the Natural Gas Industry Natural Gas / DG Natural Gas / EPG to less than 0.1 ppm(v) prior to liquefaction or Natural Gas liquids Extraction. to less than 0.1 ppm(v) while minimizing

More information

A New Refining Process for Efficient Naphtha Utilization: Parallel Operation of a C 7+ Isomerization Unit with a Reformer

A New Refining Process for Efficient Naphtha Utilization: Parallel Operation of a C 7+ Isomerization Unit with a Reformer A New Refining Process for Efficient Naphtha Utilization: Parallel Operation of a C 7+ Isomerization Unit with a Reformer Authors: Dr. Cemal Ercan, Dr. Yuguo Wang and Dr. Rashid M. Othman ABSTRACT Gasoline

More information

Process Production of Conventional Liquid Fuels from Sugar

Process Production of Conventional Liquid Fuels from Sugar BioForming Process Production of Conventional Liquid Fuels from Sugar Dr. Randy D. Cortright CTO/Founder Virent Energy Systems www.virent.com ACS/EPA Green Chemistry Conference June 23, 2009 Virent s BioForming

More information

PRACTICE EXAMINATION QUESTIONS FOR 1.6 ALKANES (includes some questions from 1.5 Introduction to Organic Chemistry)

PRACTICE EXAMINATION QUESTIONS FOR 1.6 ALKANES (includes some questions from 1.5 Introduction to Organic Chemistry) PRACTICE EXAMINATION QUESTIONS FOR 1.6 ALKANES (includes some questions from 1.5 Introduction to Organic Chemistry) 1. (a) Name the process used to separate petroleum into fractions....... Give the molecular

More information

Onboard Plasmatron Generation of Hydrogen Rich Gas for Diesel Engine Exhaust Aftertreatment and Other Applications.

Onboard Plasmatron Generation of Hydrogen Rich Gas for Diesel Engine Exhaust Aftertreatment and Other Applications. PSFC/JA-02-30 Onboard Plasmatron Generation of Hydrogen Rich Gas for Diesel Engine Exhaust Aftertreatment and Other Applications L. Bromberg 1, D.R. Cohn 1, J. Heywood 2, A. Rabinovich 1 December 11, 2002

More information

Renewable Liquids as Steam Cracker Feedstocks

Renewable Liquids as Steam Cracker Feedstocks PERP/PERP ABSTRACTS 2010 Renewable Liquids as Steam Cracker Feedstocks PERP 09/10S12 Report Abstract October 2010 Report Abstract Renewable Liquids as Steam Cracker Feedstocks PERP 09/10S12 October 2010

More information