Report No. 46. by PARK L. MORSE. January A private report by the PROCESS ECONOMICS PROGRAM PARK, CALIFORNIA STANFORD RESEARCH INSTITUTE I

Similar documents
PROCESS ECONOMICS PROGRAM

Abstract Process Economics Program Report 37B ACETIC ACID AND ACETIC ANHYDRIDE (November 1994)

CHLORINE PROCESS ECONOMICS PROGRAM. Report No. 61A. Supplement A. by YEN CHEN YEN. May A private report by the STANFORD RESEARCH INSTITUTE

PHENOL PROCESS ECONOMICS PROGRAM. Report No. 22A. Supplement A. by YEN-CHEN. September A private report by the PARK, CALIFORNIA

SULFUR DIOXIDE REMOVAL

Abstract. Process Economics Program Report No. 146 BULK CHEMICALS FROM SYNTHESIS GAS. (.Iune 1982)

PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM

Abstract Process Economics Program Report 37C ACETIC ACID (December 2001)

Abstract Process Economics Program Report 174A HIGH-OUTPUT FLUIDIZED-BED POLYETHYLENE TECHNOLOGY (July 1999)

Abstract Process Economics Program Report 128E POLYPROPYLENE (September 2011)

Abstract Process Economics Program Report 36E LINEAR LOW DENSITY POLYETHYLENE (August 2008)

Lecture 25: Manufacture of Maleic Anhydride and DDT

Abstract Process Economics Program Report 51C POLYMER NANOCOMPOSITES (June 2002)

Advanced Olefin Polymer Reactor Fundamentals and Troubleshooting

Anhydrides and Acids. Intermediates

Abstract Process Economics Program Report 232 CHIRAL INTERMEDIATES (March 2001)

January 19, 2012, Workshop on Chemical Data Reporting (CDR) Rule Case Studies for Byproduct/Recycling Reporting

Synthesis of Methyl Methacrylate from Coal-derived Syngas

The characteristic and superiority of Mitsubishi Oxo Process are following points.

PROCESS TECHNOLOGY- ORGANIC II. 51. Gas phase dehydrogenation of ethyl-benzene to styrene occurs over catalyst based on

Petrochemical Processes and Catalysis A Eurotek training course

Badger Licensing LLC. Through Reformate Alkylation Catalytic Technology. Dr. El-Mekki El-Malki ExxonMobil Research & Engineering Company (EMRE)

Abstract Process Economics Program Report 153C SINGLE-SITE CATALYSTS FOR PROPYLENE-BASED POLYMERS (June 2002)

Effect of the Reaction Bath Temperature in a Fixed-bed Reactor for Oxidation of o-xylene over V 2 O 5 /TiO 2 Catalysts

1,4-Butanediol/ Tetrahydrofuran (BDO/THF)

Chemicals and petroleum industries account for 50% of industrial energy usage.

Chemical Technology Prof. Indra D. Mall Department of Chemical Engineering Indian Institute of Technology, Roorkee

ACETIC ACID BY THE CHIYODA/UOP ACETICA PROCESS. Aspen Model Documentation

Willi Michael Brandstädter. Partial Oxidation of Raffinate II and other Mixtures of n-butane and n-butenes to Maleic Anhydride in a Fixed-Bed Reactor

Towards intensified separation processes in gas/vapour-liquid systems. Chair of Fluid Process Engineering Prof. Dr.-Ing.

G-L Taylor Flow reactor system Oxidation of ethylbenzene R. Sumbharaju L.A. Correia D.F. Meyer Y.C. van Delft A. de Groot

INTENSIFICATION OF THE PERFORMANCE OF A GASOLINE ISOMERIZATION UNIT

The Oxidation Activity and Acid-base Properties of. V2O5-K2SO4-H2SO4 Catalysts* by Mamoru Ai**

Supported molybdenum oxides as effective catalysts for the catalytic fast pyrolysis of lignocellulosic biomass

CHLORINE RECOVERY FROM HYDROGEN CHLORIDE

Catalytic Membrane Reactors

Alkylation process, Feedstocks, reactions, products, catalysts and effect of process variables.

Lecture (9) Reactor Sizing. Figure (1). Information needed to predict what a reactor can do.

Process Design Decisions and Project Economics Prof. Dr. V. S. Moholkar Department of Chemical Engineering Indian Institute of Technology, Guwahati

ADVANCES IN AROMATICS PRODUCTION

Polymer Isolation as important process step in rubber production processes

MOLECULAR SIEVES UOP MOLECULAR SIEVES*

Oxidative Dehydrogenation of Olefin*

Level 2: Input output structure

Recovery of Aromatics from Pyrolysis Gasoline by Conventional and Energy-Integrated Extractive Distillation

Towards integration of continuous reactors, separation technology and process analysis

SINOPEC MTP and MTX technologies

Studies on Mo/HZSM-5 Complex catalyst for Methane Aromatization

Balancing chemical reaction equations (stoichiometry)

School of Chemistry UNIVERSITY OF KWAZULU-NATAL, WESTVILLE NOVEMBER 2007 EXAMINATION APCH221: CHEMISTRY & INDUSTRY DURATION: 3 HOURS TOTAL MARKS: 100

PROCESS ECONOMICS PROGRAM

ADVANCES IN OLEFIN CO-MONOMER AND POLYOLEFIN PRODUCTION

Technology offer: Regeneration of chemical oxidants and reducers

Chapter 9 The Chemical Reaction Equation and Stoichiometry 9.1 Stoichiometry

HANDBOOK SECOND EDITION. Edited by

TRITIUM RECOVERY FROM WASTE USING A PALLADIUM MEMBRANE REACTOR

Integrated Knowledge Based System for Process Synthesis

2Fe 2 O 3 +3H 2 S FeS+FeS x +S+3H 2 O

Improved hydrogen yield in catalytic reforming

Ceramic Membranes in Process Technology

Wednesday 02/05/2018. Friday 11/05/2018. Day Date. B. Tech. (Chemical. Engineering Engineering. B. Tech (Chemical Technology) Day Date. B.

Structural and Catalytic Investigation of Active-Site Isolation in Pd-Ga Intermetallic Compounds

Production of Acetic Acid by Catalytic Oxidation of Butene*

Polymer plants continue to seek ways to increase production and efficiency without compromising safety.

STP-TS THERMOPHYSICAL PROPERTIES OF WORKING GASES USED IN WORKING GAS TURBINE APPLICATIONS

turopaiscnes patentamt European Patent Office Office europeen des brevets <3> Publication number: A2 EUROPEAN PATENT APPLICATION

Technical Resource Package 1

A Green Oxidant for In-Situ Chemical Oxidation. Jack Peabody Regenesis

Gas Splitting of SO3-in-Air for Sulfonation

PROCEEDINGS of the 5 th International Conference on Chemical Technology 5 th International Conference on Chemical Technology

Mixed Oxides in Selective Oxidation Catalysis: The Role of Disordered Surface Layers

Nonlinear Operability of a Membrane Reactor for Direct Methane Aromatization

Design for Environment : Green Chemistry Principles for Product Design

Experiment 30: Identification of a Conjugated Diene from Eucalyptus Oil

GRAPHENE: TECHNOLOGIES, APPLICATIONS AND MARKETS

COPYRIGHTED MATERIAL INTRODUCTION CHAPTER 1

Simulation of 1,3-butadiene extractive distillation process using N-methyl-2-pyrrolidone solvent

In The Name Of God. Ali Hashempour. M.Sc. Student at School of Chemical Engineering, College of Engineering, University of Tehran, Tehran, Iran.

Selective Hydrogenation of 1-Hexyne Using Pd-Cu and Pd- W Supported on Alumina Catalysts

HW Help. How do you want to run the separation? Safety Issues? Ease of Processing

InnovaRig - an Instrument for a European Geothermal Drilling Program

Wikisheet Dividing Wall Column

Computer Aided Simulation and Process Design of a Hydrogenation Plant Using Aspen HYSYS 2006

Liquid-Liquid Equilibrium for Extraction of Benzene from 1-Hexene Using Two Different Solvents

Transformation of Lower Alkanes into Aromatic. Hydrocarbons over ZSM-5 Zeolites

BY ye; v P. April 29, 1969 C. S. KELLEY 3,441,626. TEMPERATURE CONTROL of EXOTHERMIC REACTIONS Filed March 6, 1967 INVENTOR. PRODUCT C. S.

Real-Time Optimization (RTO)

Asset Life and pricing the use of infrastructure: the case of Electricity Transmission in Chile

GTC Technology. Rethinking Xylenes Production via Toluene Methylation

Acetone Process Energy Recovery by Means of Energy Analysis

(12) United States Patent (10) Patent No.: US 6,242,661 B1

NEW ADIABATIC REACTORS FOR THE OXYDATION OF METHANOL TO FORMALDEHYDE

Exercise 1. Material balance HDA plant

Investigation of benzene and cycloparaffin containing hexane fractions skeletal isomerization on Pt/sulphated metal-oxide catalyst

CHAPTER 4 ISOPROPYLATION OF TOLUENE

Process Design Decisions and Project Economics Prof. Dr. V. S. Moholkar Department of Chemical Engineering Indian Institute of Technology, Guwahati

Report Abstract Benzene/Toluene PERP06/07-6 January 2009

Successful Development of a New Catalyst for Efficiently Collecting Tritium in Nuclear Fusion Reactors

SCR Catalyst Layer Addition Specification and Management

Transcription:

Report No. 46 MALEIC ANHYDRIDE by PARK L. MORSE January 1969 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA

CONTENTS 1 INTRODUCTION......................... 1 2 SUMMARY........................... 3 3 INDUSTRY STATUS... 11 4 MALEIC ANHYDRIDE FROM BENZENE... 19 Chemistry... Review of Processes... Effect of Temperature and Pressure... Catalysts... Reactor Types... Effect of Air to Benzene Ratio... Space Velocity, Yield, Conversion, and Selectivity By-Products... Recovery of Maleic Anhydride (Cr or benzene feed) Dehydration, Purification, and Color Stabilization benzene feed)... Description of Design Case... Discussion of Design Case... Cost Estimates........ 19..... 27..... 27..... 34..... 36..... 38..... 38..... 40 41 ic; Ar' '..... 46..... 51..... 61..... 63 5 MALEIC ANHYDRIDE FROM n-butane... 69 Chemistry... 69 Review of Processes... 70 Selection of Data for Design Case... 70 Description of Design Case... 74 Discussion of Design Case... 83 Cost Estimates... 85 6 MALEIC ANHYDRIDE FROM C4 OLEFINS... I Chemistry... Review of Processes... Effect of Temperature and Pressure... Catalysts... Reactor Types... Effect of Air to C, Olefin Ratio... Space Velocity, Yield, Conversion, and Selectivity... By-Products... Recovery and Purification of Maleic Anhydride... Description of Design Case... 91 91 92 92 97 98 98 100 102 103 103 iii

CONTENTS (continued) Discussion of Design Case............... 110 Cost Estimates..,.................. 111 MALEIC ANHYDRIDE FROM BUTENE-BUTADIENE FEED...... 117 Description of Design Case...... 118 Discussion of Design Case...... 126 Cost Estimates...... 128 MALEIC ANHYDRIDE FROM BENZENE--HIGH SPACE VELOCITY CASE... 133 Background for Design Case... Description of Design Case... Fixed Capital and Production Costs... Discussion of Results...... 133... 133... 138... 138 FUMARIC ACID FROM MALEIC ANHYDRIDE... Review of Processes... Industry Status............... 141 141 141 APPENDIX A APPENDIX B APPENDIX C APPENDIX D DESIGN CONDITIONS, COST BASIS AND DEFINITIONS... PHYSICAL DATA... SPECIFICATIONS... HANDLING AND SAFETY... 145 149 151 153 CITED REFERENCES... SUPPLEMENTARY REFERENCES.... 169 187 iv

ILLUSTRATIONS 4.1 4.2 4.3 4.4 5.1.............. 5.2 cost........................... 6.1 6.2 7.1 7.2 Rate Data for Catalytic Oxidation of Benzene to Maleic Anhydride and Carbon Oxides............................... Alternative Purification System (Maleic Anhydride from Benzene)......................... cost........................... Maleic Anhydride from n-butene.............. Maleic Anhydride from Butene cost.,......................... Maleic Anhydride from Butene-Butadiene Feed........ Maleic Anhydride from Butene-Butadiene Feed cost........................... 24 57 60 68 79 89 107 115 123 132 V

TABLES 2.1 3.1 3.2 4.1 4.2 4.3 4.4 4.5 4.6 4.7 4.8 5.1 5.2 5.3 5.4 5.5 5.6 6.1 Process Costs for Producing Maleic Anhydride... 5 Maleic Anhydride Producers... 15 Recent New Plants and Expansions... 17 Summary of Processes... 29 Recovery of Maleic Anhydride Summary of Processes... 42 Dehydration and Purification Summary of Processes... 47 Major Process Equipment and Utilities Summary... 57 Stream Flows... 59 Battery Limits and Utilities Investment... 64 Total Capital Investment... 66 Production Costs... 67 Summary of Processes... 71 Major Process Equipment and Utilities Summary... 78 Stream Flows... 81 Battery Limits and Utilities Investment... 86 Total Capital Investment... 87 Production Costs... 88 Maleic Anhydride from C, Olefins Summary of Processes... 93 vii

TABLES 6.2 Maleic Anhydride from n-butene Major Process Equipment and Utilities Summary....... 107 6.3 Maleic Anhydride from n-butene Stream Flows... 109 6.4 Maleic Anhydride from n-butene Battery Limits and Utilities Investment.......... 112 6.5 Maleic Anhydride from n-butene Total Capital Investment.................. 113 6.6 Maleic Anhydride from n-butene Production Costs...................... 114 7.1 Maleic Anhydride from Butene-Butadiene Feed Major Process Equipment and Utilities Summary....... 123 7.2 Maleic Anhydride from Butene-Butadiene Feed Stream Flows... 125. 7.3 Maleic Anhydride from Butene-Butadiene Feed Battery Limits and Utilities Investment.......... 129 7.4 Maleic Anhydride from Butene-Butadiene Feed Total Capital Investment..,,.............. 130 7.5 Maleic Anhydride from Butene-Butadiene Feed Production Costs......,............... 131 8.1 -- High Space Velocity Case Utilities Summary..................... 136 8.2 --High Space Velocity Case Battery Limits and Utilities Investment.......... 137 8.3 -- High Space Velocity Case Total Capital Investment.................. 138 8.4 -- High Space Velocity Case Production Costs...................... 139 9.1 Fumaric Acid from Maleic Anhydride Summary of Processes.................... 142 viii

1 INTRODUCTION This report describes processes for producing maleic anhydride from four starting materials--benzene, normal butane, normal butenes, and a mixture of 1,3-butadiene and normal butenes. Both low and high space velocity design cases using benzene as feed are evaluated. scopeofthereportwasexpandedtoincludeabriefdiscussiononfumaric The original acid. Information for the study was obtainedonly from patents and general literature sources. Stanford Research Institute did not have access to unpublished process diagrams or plans of any company. None of the process designs developed completely represents the technology of one company. Because the patents reviewed describe only limited parts of a process, it was necessary to use personal judgment to integrate and complete the design. The Institute does not know whether the patents used for the design cases also were the basis for commercial installations. However, it is known that, with the exception of butane, the starting materials studied have been used, or will be used,in the near future, as feedetocks for maleic anhydride plants.