ISOMERIZATION OF PARAFFINS FOR GASOLINE
|
|
- Austin Lang
- 5 years ago
- Views:
Transcription
1 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
2 CONTENTS LIST OF ABBREVIATIONS... GLOSSARY.,... xv xvii INTRODUCTION. 1 SUMMARY... General Aspects... Current Situation... Processes. Summary of Evaluations... Technical Aspects... Chemistry. Processes. INDUSTRY STATUS... History and Prospects for Isomerization... Capacities.. Production, Consumption, and Operating Rates. Raw Materials PROCESS COMPARISONS AND ANALYSIS LOW-TEMPERATURE ISOMERIZATION Chemistry.. Kinetics.. Poisons.. Review of Processes... UOPPene# BP Isomerizatio;... Process Description... Process Discussion... Cost Estimates SRIDesign. UOPDesign. BPDesign. ISOMERIZATION OVER ZEOLITE CATALYSTS... Review of Processes... Process Description... Process Discussion... Cost Estimates vii
3 CONTENTS 7 ISOMERIZATION WITH RECYCLE OF NORMAL PENTANE Review of Processes... Process Description... Process Discussion... Cost Estimates ISOMERIZATION WITH RECYCLE OF nc5, nc6, and MP Review of Processes... Process Description... Process Discussion... Cost Estimates ISOMERIZATION WITH RECYCLE OF NORMAL PARAFFINS Chemistry.. Review of Processes... Union Carbide Total Isomerization Process. BP Normal Paraffin Extraction... UOP Molex@ Process... Process Description... Process Discussion... Cost Estimates ISOMERIZATION OF BUTANE Chemistry.. Review of Processes... British Petroleum Process. Universal Oil Products: Butameg Process. Process Description... Process Discussion... Cost Estimates APPENDIX A DESIGN AND COST BASIS APPENDIX B PHYSICAL DATA... APPENDIX C HANDLING AND SAFETY. CITED REFERENCES. PATENT REFERENCES BY COMPANY viii
4 Cost, Capacity, and Octane Gain Cost of Octane Gain Equilibrium Composition: Vapor Phase., , BP Isomerization Process with Cs/C, or Ce Feedstock...., ,, Isomerization dver Zeolite Catalyst..,..... Isomerization with Recycle of nc,, nc,, and BP...,.,. Isomerization with Recycle of ncr, nc,, and MP on Production Cost....., Equilibrium Composition of Butanes: Vapor Phase IX
5 TABLES Summary of Evaluations... Plants for Normal Paraffin Isomerization.. Plants for Butane Isomerization... Various Octane Gains and Costs... Friedel-Crafts Isomerization of Normal Paraffins Patent Summary.... Hydroisomerization of Normal Paraffins... Design Bases and Assumptions StreamFlows Summary of Waste Products. Total Capital Investment.. Production Costs... BP Isomerization Process Material Balance... BP Isomerization Process Capital and Operation Cost Estimates, Utilities and Chemical Requirements for 8,400 BSD C,/C, Unit... Design Bases and Assumptions Stream Flows Summary of Waste Products. Total Capital Investment xi
6 TABLES Production Costs Patent Summary Design Bases and Assumptions Major Process Equipment and Utilities Summary StreamFlows Summary of Waste Products Total Capital Investment Production Costs. i Isomerization with Recycle of ncs, ncs, and MP Patent Summary , Isomerization with Recycle of nc,, nc,, and MP Design Bases and Assumptions Isomerization with Recycle of nc,, ncs, and MP Major Process Equipment and Utilities Summary Isomerization with Recycle of ncs, nc,, and MP StreamFlows 161 Isomerization with Recycle of ncs, ncs, and MP Summary of Waste Products Isomerization with Recycle of ncs, ncs, and IMP Total Capital Investment , Isomerization with Recycle of ncs, nce, and MP Production Costs Patent Summary Design Bases and Assumptions xii
7 TABLES B.1 B.2 StreamFlows Summary of Waste Products. Total Capital Investment.. Production Costs... Costs of Total Isomerization Process from the Literature.. Friedel-Crafts Patent Summary.... Hydroisomerization of Butane Patent Summary.... Design Bases and Assumptions StreamFlows Summary of Waste Products. Total Capital Investment.. Production Costs... Properties of Hydrocarbons. Composition of Feedstock Xiii
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 informationAROMATIC 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 informationETHYLENE-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 informationACRYLICACID 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 informationOX0 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 informationReport No. 35 BUTADIENE. March A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I PARK, CALIFORNIA
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 CONTENTS 1 INTRODUCTION.......................
More informationDIOXIDE 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 informationHYDROFLUORIC 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 informationCONTENTS 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 informationPROTEINS 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 informationXYLENES 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 informationACRYLONITRILE 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 informationLINEAR 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 informationAbstract 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 informationALIPHATIC 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 informationPOLYAMIDES 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 informationPROCESS 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 informationAbstract 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 informationTREATMENTOF 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 informationAbstract 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 informationPROCESS 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 informationIHS 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 informationPEP 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 informationAbstract 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 informationPROCESS 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 informationProcess 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 informationAbstract 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 informationProcess 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 informationAbstract 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 informationAbstract 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 informationAbstract 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 informationPROCESS 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 informationPEP 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 informationAbstract 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 informationPEP 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 informationUnit 2. Light Naphtha Isomerization. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna
Unit 2. Light Naphtha Isomerization Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna Isomerization of Light Naphtha Isomerization is the process in which light straight chain
More informationIHS 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 informationAbstract 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 informationR&D on New, Low-Temperature, Light Naphtha Isomerization Catalyst and Process
2000M1.1.2 R&D on New, Low-Temperature, Light Naphtha Isomerization Catalyst and Process (Low-temperature isomerization catalyst technology group) Takao Kimura, Masahiko Dota, Kazuhiko Hagiwara, Nobuyasu
More informationReplacing the Volume & Octane Loss of Removing MTBE From Reformulated Gasoline Ethanol RFG vs. All Hydrocarbon RFG. May 2004
Replacing the Volume & Octane Loss of Removing MTBE From Reformulated Gasoline Ethanol RFG vs. All Hydrocarbon RFG May 2004 Prepared and Submitted by: Robert E. Reynolds President Downstream Alternatives
More informationGTC 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 informationPEP 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 informationFischer-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 informationDEVELOPMENT AND COMMERCIALIZATION OF ATIS-2L, A HIGH ACTIVITY, LOW COST PARAFFIN ISOMERIZATION CATALYST
DEVELOPMENT AND COMMERCIALIZATION OF, A HIGH ACTIVITY, LOW COST PARAFFIN ISOMERIZATION CATALYST W.S. Graeme, M.N.T. van der Laan Akzo Nobel Catalysts ABSTRACT Akzo Nobel s high activity paraffin isomerization
More informationPreface... 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 informationPROCESS 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 informationProcess 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 informationIHS 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 informationANALYSIS OF OPTIMAL PROCESS FLOW DIAGRAMS OF LIGHT NAPHTHA ISOMERIZATION PROCESS BY MATHEMATIC MODELLING METHOD
ANALYSIS OF OPTIMAL PROCESS FLOW DIAGRAMS OF LIGHT NAPHTHA ISOMERIZATION PROCESS BY MATHEMATIC MODELLING METHOD Vjacheslav Chuzlov 1,*, Konstantin Molotov 2 1 Tomsk Polytechnic University, Lenin av. 30,
More informationStephen 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 informationEnhance Naphtha Value and Gasoline Reformer Performance Using UOP s MaxEne TM Process
Enhance Naphtha Value and Gasoline Reformer Performance Using UOP s MaxEne TM Process Mark Turowicz UOP IPL, A Honeywell Company 1st IndianOil Petrochemical Conclave March 16, 2012 Gurgaon, India 2011
More informationLinear Alkylbenzene (LAB)
PERP/PERP ABSTRACTS 2009 Report Abstract Linear Alkylbenzene (LAB) Production Costs & Technology for UOP DETAL and HF (Pacol, Define, PEP, Alkylation), EniChem/SASOL Monochloroparaffins LAB processes;
More informationPROCESS ECONOMICS PROGRAM
PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California Abstract 94025 Process Economics Program Report No. t75a BLENDS CONTAINING POLYOLEFINS (June 1990) This report expands the scope of PEP
More informationProven process. Proven plants. Proven performance.
Methanol to gasoline technology Proven process. Proven plants. Proven performance. Background High crude oil prices beginning in the mid-2000s spurred worldwide interest in finding and developing additional
More informationHandbook 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 information1. Introduction Regional Analysis...4
Table of Contents i Table of Contents 1. Introduction...1 1.1 Opportunities for international manufacturers...1 1.2 Objectives and structure of this report...2 2. Regional Analysis...4 2.1 Description
More informationChanges to America s Gasoline Pool. Charles Kemp. May 17, Baker & O Brien, Inc. All rights reserved.
Changes to America s Gasoline Pool Charles Kemp May 17, 2016 Baker & O Brien, Inc. All rights reserved. Discussion Points Light Naphtha Definitions Sources and Uses of Light Naphtha Octane Challenges Tier
More informationRenewable 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 informationTechnology for Producing Clean Diesel Utilizing Moderate Pressure Hydrocracking With Hydroisomerization
Technology for Producing Clean Diesel Utilizing Moderate Pressure Hydrocracking With Hydroisomerization XIII Refining Technology Forum IMP-Pemex Pemex Refinacion Mexico City, Mexico November 14, 2007 J.
More information(Syn)Gas to Fuel HIGH QUALITY GASOLINE FROM METHANOL
(Syn)Gas to Fuel HIGH QUALITY GASOLINE FROM METHANOL Public N. Ringer/ R. Rakoczy Business Unit Catalysts 09.09.2013 2 Agenda Introduction MTG: History & Chemistry The Catalysts CAC s STF Process Conclusions
More informationPEP 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 informationContinuous Plat forming
Continuous Plat forming By E. L. Pollitzer Corporate Research Center, UOP Inc., Des Plaines, Illinois, U.S.A. In the most recent innovation in catalytic reforming very small quantities of the platinum
More informationPILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days
Training Title PILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days Training Date Pilot Plant Design, Installation & Operation 5 21 25 Sep $3,750 Dubai, UAE In any of the 5 star hotels.
More informationCourse: 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 informationFoundations of Thermodynamics and Chemistry. 1 Introduction Preface Model-Building Simulation... 5 References...
Contents Part I Foundations of Thermodynamics and Chemistry 1 Introduction... 3 1.1 Preface.... 3 1.2 Model-Building... 3 1.3 Simulation... 5 References..... 8 2 Reciprocating Engines... 9 2.1 Energy Conversion...
More informationPEP Review ACETIC ACID, UPDATE OF THE CELANESE AO PLUS PROCESS By P D Pavlechko, PhD (February 2013)
PEP Review 2013-01 ACETIC ACID, UPDATE OF THE CELANESE AO PLUS PROCESS By P D Pavlechko, PhD (February 2013) ABSTRACT Acetic acid production shifted toward methanol carbonylation with the advent of Monsanto
More informationTHE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING
THE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING J. Mike Brown, Ph.D. Senior Vice President Technology BASICS OF REFINERY OPERATIONS Supply and Demand Where Does The Crude Oil Come From?
More informationMISSION VALLEY REGIONAL OCCUPATIONAL PROGRAM TRANSPORTATION SECTOR BASIC CAR CARE COURSE OUTLINE
MISSION VALLEY REGIONAL OCCUPATIONAL PROGRAM TRANSPORTATION SECTOR BASIC CAR CARE COURSE OUTLINE 1. Course Title: Basic Car Care 2. CBEDS Title: Automotive Mechanics 3. CBEDS Number: 5655 4. Job Titles/DOT
More informationProcess 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 informationStudy on Relative CO2 Savings Comparing Ethanol and TAEE as a Gasoline Component
Study on Relative CO2 Savings Comparing Ethanol and TAEE as a Gasoline Component Submitted by: Hart Energy Consulting Hart Energy Consulting 1616 S. Voss, Suite 1000 Houston, Texas 77057, USA Terrence
More informationTHE INSTITUTE OF PAPER CHEMISTRY. Appleton, Wisconsin MODIFIED RING COMPRESSION TESTS ON CORRUGATING MEDIUM. / Project Preliminary Report
. --.c.l. < 4.../ti.-1 i /cf.?- f:.... '( [, 0 THE INSTITUTE OF PAPER CHEMISTRY '4d-~-W-ktWLt:e cl.3 Appleton, Wisconsin I' 9~) MODIFIED RING COMPRESSION TESTS ON CORRUGATING MEDIUM / Project 1108-55 Preliminary
More informationTable of Contents. Foreword...xiii. Chapter One Introduction, Objectives of the Guide...1
Table of Contents Foreword...xiii Chapter One Introduction, 9 1.1 Objectives of the Guide...1 Chapter Two Pumping System Hydraulic Characteristics, 3 2.1 System Characteristics...3 2.2 Pump Curves...9
More informationSolvent Deasphalting Conversion Enabler
Kevin Whitehead Solvent Deasphalting Conversion Enabler 5 th December 2017 Bottom of the Barrel Workshop NIORDC, Tehran 2017 UOP Limited Solvent Deasphalting (SDA) 1 Natural Gas Refinery Fuel Gas Hydrogen
More informationPage 1 of 10. Motor Pool Policies & Procedures
Page 1 of 10 Motor Pool Policies & Procedures Page 2 of 10 I. Request Vehicle from Motor Pool A. Call Motor Pool to check availability of desired vehicle and make reservation. B. Complete and submit Motor
More informationChapter 11 Gasoline Production
Petroleum Refining Chapter 11: Gasoline Production Chapter 11 Gasoline Production INTRODUCTION Convert SR naphtha to motor gasoline stocks through 1. Reforming 2. Isomerization Production of motor gasoline
More informationPolyethylene Terephthalate
Polyethylene Terephthalate (PET) Table of Contents A Report by Nexant s CHEMSYSTEMS Process Evaluation/Research Planning (PERP) Program PERP 2012-6 Published April 2013 Section Page 1 Executive Summary...
More informationEXPERIMENT AND ANALYSIS OF MOTORCYCLE EXHAUST DESIGN ABDUL MUIZ BIN JAAFAR
EXPERIMENT AND ANALYSIS OF MOTORCYCLE EXHAUST DESIGN ABDUL MUIZ BIN JAAFAR Report submitted in partial fulfilment of the requirement for the award of the degree of Bachelor of Mechanical Engineering with
More informationUnit MC07K Knowledge of Diagnosis and Rectification of Motorcycle Engine Faults
Assessment Requirements Unit MC07K Knowledge of Diagnosis and Rectification of Motorcycle Engine Faults Content: Single cylinder and multi-cylinder fuel injection systems a. The operation and construction
More informationPotential Environmental and Economic Benefit s of Higher-Oct ane Gasoline
Potential Environmental and Economic Benefit s of Higher-Oct ane Gasoline Raymond Speth, Eric Chow, Robert Malina, Steven Barrett, J ohn Heywood, W illiam Green CRC W orkshop, Argonne National Laboratory
More informationReactivity of several olefins in the HDS of full boiling range FCC gasoline over PtPd/USY
Book of Abstracts European Congress of Chemical Engineering (ECCE-6) Copenhagen, 16- September 7 Reactivity of several olefins in the HDS of full boiling range FCC gasoline over PtPd/USY Szabolcs Magyar,
More informationStrategies for Maximizing FCC Light Cycle Oil
Paste Logo Here Strategies for Maximizing FCC Light Cycle Oil Ann Benoit, Technical Service Representative Refcomm, March 4-8, 2015 LCO and Bottoms Selectivity 90 Bottoms wt% 24 LCO wt% Hi Z/M Low Z/M
More informationOCTANE THE NEW ECONOMICS OF. What Drives the Cost of Octane and Why Octane Costs Have Risen Since 2012 T. J. HIGGINS. A Report By:
THE NEW ECONOMICS OF OCTANE What Drives the Cost of Octane and Why Octane Costs Have Risen Since 2012 A Report By: T. J. HIGGINS Contents Foreword... 1 1. Executive Summary... 2 2. Tracking the Changing
More informationEngineering Entrepreneurship. Ron Lasser, Ph.D. EN 0062 Class #
Engineering Entrepreneurship Ron Lasser, Ph.D. EN 0062 Class #4 9-29-06 1 Biodiesel Incorporated The Case: It is about one group s efforts to identify a business opportunity Look at the Entrepreneurial
More informationContents INTRODUCTION...
INTRODUCTION... xiii CHAPTER 1. FROM THE SYSTEM TO THE SOFTWARE... 1 1.1. Introduction... 1 1.2. Command/control system... 2 1.3. System... 6 1.4. Software application... 8 1.4.1. What is software?...
More informationAlkylation & 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 informationUnit 4. Fluidised Catalytic Cracking. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna
Unit 4. Fluidised Catalytic Cracking Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna Introduction Catalytic cracking is the process in which heavy low-value petroleum stream
More informationFig: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 informationPetroleum 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 informationLCO Processing Solutions. Antoine Fournier
LCO Processing Solutions Antoine Fournier 1 Outline Market trends and driving factors The light cycle oil Feedstock characteristics Hydroprocessing challenges Main option for LCO upgrading Catalyst update
More informationLive Crude Oil Volatility
Live Crude Oil Volatility Dan Wispinski : Alberta Innovates Technology Futures Bob Falkiner : Imperial Oil Engineering Services CCQTA/COQA October 31, 2014 Food-Agriculture Environment Health Pipeline
More informationAbout the authors xi. Woodhead Publishing Series in Energy. Preface
v Contents About the authors xi Woodhead Publishing Series in Energy Preface xiii xv 1 Biodiesel as a renewable energy source 1 1.1 Introduction 1 1.2 Energy policy 2 1.3 Transformation of biomass 20 1.4
More informationCOMPRESSOR STATION OPERATIONS
CONTENTS FIGURES AND TABLES... viii PREFACE... xi ACKNOWLEDGEMENTS... xiii CHAPTER 1. INTRODUCTION... 1 Scope and Outline... 1 Types of Stations... 2 Production Stations... 2 Storage Stations... 3 Transmission
More informationHigh Temperature Thermoplastic Nylons 01/02S3
High Temperature Thermoplastic Nylons 01/02S3 May 2002 Nexant, Inc./Chem Systems 44 South Broadway White Plains, New York 10601-4425 Telephone (914) 609-0300 Facsimile (914) 609-0399 www.chemsystems.com
More informationWORLDWIDE 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 informationPREDICTION OF REMAINING USEFUL LIFE OF AN END MILL CUTTER SEOW XIANG YUAN
PREDICTION OF REMAINING USEFUL LIFE OF AN END MILL CUTTER SEOW XIANG YUAN Report submitted in partial fulfillment of the requirements for the award of the degree of Bachelor of Engineering (Hons.) in Manufacturing
More informationAlkyClean 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 informationSTUDY OF CHANGES IN THE HYDROCARBON COMPOSITION OF GASOLINE AFTER EACH STAGE REFORMING REACTOR
Int. J. Chem. Sci.: 13(2), 2015, 875-884 ISSN 0972-768X www.sadgurupublications.com STUDY OF CHANGES IN THE HYDROCARBON COMPOSITION OF GASOLINE AFTER EACH STAGE REFORMING REACTOR A. E. KALDYGOZOV *, E.
More informationUnit 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 informationEvaluation of phase separator number in hydrodesulfurization (HDS) unit
IOP Conference Series: Materials Science and Engineering PAPER OPEN ACCESS Evaluation of phase separator number in hydrodesulfurization (HDS) unit To cite this article: A D Jayanti and A Indarto 2016 IOP
More informationPRACTICE 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