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Handbook of petrochemicals production processes, Second Edition PDF

637 Pages·2018·64.788 MB·English
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HANDBOOK OF PETROCHEMICALS PRODUCTION PROCESSES 00_Meyers_FM_i-xxviii.indd 1 24/08/18 5:53 pm This page intentionally left blank 00_Meyers_FM_i-xxviii.indd 2 24/08/18 5:53 pm HANDBOOK OF PETROCHEMICALS PRODUCTION PROCESSES Robert A. Meyers Second Edition New York Chicago San Francisco Athens London Madrid Mexico City Milan New Delhi Singapore Sydney Toronto 00_Meyers_FM_i-xxviii.indd 3 24/08/18 5:53 pm Copyright © 2019 by McGraw-Hill Education. All rights reserved. Except as permitted under the United States Copyright Act of 1976, no part of this publication may be reproduced or distributed in any form or by any means, or stored in a database or retrieval system, without the prior written permission of the publisher. ISBN: 978-1-25-964314-9 MHID: 1-25-964314-X The material in this eBook also appears in the print version of this title: ISBN: 978-1-25-964313-2, MHID: 1-25-964313-1. eBook conversion by codeMantra Version 1.0 All trademarks are trademarks of their respective owners. Rather than put a trademark symbol after every occurrence of a trade- marked name, we use names in an editorial fashion only, and to the benefit of the trademark owner, with no intention of infringe- ment of the trademark. Where such designations appear in this book, they have been printed with initial caps. McGraw-Hill Education eBooks are available at special quantity discounts to use as premiums and sales promotions or for use in corporate training programs. To contact a representative, please visit the Contact Us page at www.mhprofessional.com. Information contained in this work has been obtained by McGraw-Hill Education from sources believed to be reliable. However, neither McGraw-Hill Education nor its authors guarantee the accuracy or completeness of any information published herein, and neither McGraw-Hill Education nor its authors shall be responsible for any errors, omissions, or damages arising out of use of this information. This work is published with the understanding that McGraw-Hill Education and its authors are supplying informa- tion but are not attempting to render engineering or other professional services. If such services are required, the assistance of an appropriate professional should be sought. TERMS OF USE This is a copyrighted work and McGraw-Hill Education and its licensors reserve all rights in and to the work. Use of this work is subject to these terms. Except as permitted under the Copyright Act of 1976 and the right to store and retrieve one copy of the work, you may not decompile, disassemble, reverse engineer, reproduce, modify, create derivative works based upon, transmit, distribute, disseminate, sell, publish or sublicense the work or any part of it without McGraw-Hill Education’s prior consent. You may use the work for your own noncommercial and personal use; any other use of the work is strictly prohibited. Your right to use the work may be terminated if you fail to comply with these terms. THE WORK IS PROVIDED “AS IS.” McGRAW-HILL EDUCATION AND ITS LICENSORS MAKE NO GUARANTEES OR WARRANTIES AS TO THE ACCURACY, ADEQUACY OR COMPLETENESS OF OR RESULTS TO BE OBTAINED FROM USING THE WORK, INCLUDING ANY INFORMATION THAT CAN BE ACCESSED THROUGH THE WORK VIA HYPERLINK OR OTHERWISE, AND EXPRESSLY DISCLAIM ANY WARRANTY, EXPRESS OR IMPLIED, INCLUD- ING BUT NOT LIMITED TO IMPLIED WARRANTIES OF MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE. McGraw-Hill Education and its licensors do not warrant or guarantee that the functions contained in the work will meet your requirements or that its operation will be uninterrupted or error free. Neither McGraw-Hill Education nor its licensors shall be liable to you or anyone else for any inaccuracy, error or omission, regardless of cause, in the work or for any damages resulting therefrom. McGraw-Hill Education has no responsibility for the content of any information accessed through the work. Under no circumstances shall McGraw-Hill Education and/or its licensors be liable for any indirect, incidental, special, punitive, consequential or similar damages that result from the use of or inability to use the work, even if any of them has been advised of the possibility of such damages. This limitation of liability shall apply to any claim or cause whatsoever whether such claim or cause arises in contract, tort or otherwise. CONTENTS Contributors xix Preface xxiii Licensing Contacts xxv Part 1 Intermediates Chapter 1.1. Badger Cumene Technology Kevin J. Fallon 1.3 Introduction / 1.3 Cumene Uses and Industry / 1.3 Physical Properties / 1.5 Process Chemistry / 1.5 Catalyst Performance and Contaminants / 1.8 Process Description / 1.8 Performance / 1.9 Commercial Experience / 1.9 Chapter 1.2. Badger Ethylbenzene Technology Brian Maerz and Lawrence Stein 1.11 Introduction / 1.11 Feedstocks for Ethylbenzene Production / 1.12 ExxonMobil EBMax Catalysts / 1.14 Process Chemistry and EBMax Catalyst Performance / 1.14 Process Description / 1.16 Process Design Optimization / 1.18 EBMax Designs Using Chemical-Grade Ethylene Feedstocks / 1.18 Ethylbenzene Product Quality / 1.19 Raw Materials, Utilities, and Catalyst Requirements / 1.20 EBMax Plant Design / 1.21 Reference / 1.21 Chapter 1.3. BP Para-Xylene Process Homok Lee and Elizabeth Tyson 1.23 Introduction / 1.23 Para-Xylene Recovery in an Aromatics Complex / 1.24 Development of Crystallization Process / 1.25 Comparison of Crystallization to Selective Adsorption / 1.27 Process Fundamentals / 1.29 Process Discussion / 1.30 Environmental Impact / 1.33 Case Study / 1.33 Bibliography / 1.34 v 00_Meyers_FM_i-xxviii.indd 5 24/08/18 5:53 pm vi CONTENTS Chapter 1.4. Isomalk-3 (n-Butane Isomerization) Ilya Aranovich and Saurav De 1.35 Introduction / 1.35 Process Flow Scheme / 1.36 Reverse Isomerization / 1.36 Reaction Mechanism / 1.38 Catalyst Regeneration / 1.38 Process Variables / 1.38 Isomalk-3 Catalyst Contaminants / 1.39 Makeup Gas Quality / 1.39 Nitrogen Quality / 1.40 Advantages of SI-3 Catalyst / 1.40 Isomalk-3 Reactors / 1.40 Hydrocarbon Feed and Makeup Gas Dryers / 1.41 Wastes and Emissions / 1.41 Commercial Experience / 1.42 Estimated Yields / 1.42 Utility Requirements / 1.42 Chapter 1.5. CrystPXSM: Modern Crystallization Technology for Para-Xylene Production Weihua Jin 1.43 Introduction / 1.43 CrystPX for High-Purity Para-Xylene Production / 1.43 Process Chemistry and Thermodynamics / 1.44 Detailed Process Description / 1.45 Product and By-Product Specifications / 1.47 Process Economics / 1.48 Commercial Experience / 1.48 Conclusion / 1.48 Chapter 1.6. EB-X: A Process for Ethylbenzene Separation and Xylenes Upgrade Sachin Joshi and Alisa Kammafoo 1.51 Introduction / 1.51 Process Chemistry (Separation Enhancing of Ethylbenzene from Para-Xylene by the Solvent Function) / 1.51 Process Description / 1.52 Feeds and Products / 1.53 Process Design / 1.54 Commercial Description / 1.54 Chapter 1.7. GT-BTX PluSø: Aromatics and Sulfur Extraction from FCC Gasoline Charlie Chou 1.55 Introduction / 1.55 General Process Description / 1.55 Commercial Experience / 1.61 Conclusion / 1.64 Chapter 1.8. GT-BTXø Aromatics Extraction Process Lucia Cretoiu 1.65 Introduction / 1.65 General Process Description / 1.65 Process Perspective / 1.68 00_Meyers_FM_i-xxviii.indd 6 24/08/18 5:53 pm CONTENTS vii Process Description / 1.70 Key/Proprietary Equipment / 1.72 Product Specifications / 1.72 Wastes and Emissions / 1.74 Process Economics / 1.74 Chapter 1.9. GT-DWCø Applications Manish Bhargava and Roomi Kalita 1.75 Introduction / 1.75 General Information for GT-DWC / 1.75 GT-DWC for Naphtha Splitter Revamp / 1.85 Process Economics / 1.87 GT-DWC for LPG Recovery / 1.89 Feed and Product Specifications / 1.91 Commercial Experience / 1.92 Conclusion / 1.92 Chapter 1.10. GT-HDSSM Process for C8/C9 Pygas Components Andrei Cimpeanu, Mircea Cretoiu, and Joseph C. Gentry 1.93 General Process Description / 1.93 Process Chemistry and Thermodynamics / 1.93 Catalyst Chemistry / 1.94 Reactor Temperature / 1.95 Reactor Pressure / 1.95 Detailed Process Description / 1.95 Wastes and Emissions / 1.98 Commercial Description / 1.98 Chapter 1.11. GT-TolAlkSM: Toluene Methylation to Xylenes Zhongyi Ding and Pradeep Pawar 1.99 Introduction / 1.99 Process Chemistry / 1.99 Description of the Process Flow / 1.100 Process Performance / 1.101 Process Advantages / 1.102 Equipment Considerations / 1.102 Case Study / 1.103 Conclusion / 1.104 Bibliography / 1.104 Chapter 1.12. Lummus/UOP Liquid-Phase EBone Process and Mixed-Phase CDTECH EBø Process Kevin J. Schwint 1.105 Introduction / 1.105 Process Perspective / 1.106 Process Chemistry / 1.106 Process Description / 1.106 Economics / 1.111 Summary of Process Features / 1.113 Chapter 1.13. Lurgi Distapex Extractive Distillation Process Sabine Mittelstädt 1.115 Introduction / 1.115 Chemistry Overview / 1.115 00_Meyers_FM_i-xxviii.indd 7 24/08/18 5:53 pm viii CONTENTS Specifications / 1.115 Process Description / 1.116 Highlights and Benefits of the Technology / 1.117 Economics of the Technology / 1.118 Commercial Experience / 1.118 Chapter 1.14. MaxEne¡ Process Gregory Funk, Ernest Boehm, and Stephen Sohn 1.121 Introduction / 1.121 Description of the Honeywell UOP MaxEne Process / 1.121 MaxEne Process Configurations / 1.123 Case Study / 1.124 MaxEne Process Specifications / 1.126 Commercial Experience / 1.127 References / 1.127 Chapter 1.15. UOP Parex™ Process Linda Shi Cheng 1.129 Introduction / 1.129 Parex Versus Crystallization / 1.129 Process Performance / 1.131 Feedstock Considerations / 1.132 Description of the Process Flow / 1.133 Equipment Considerations / 1.134 Case Study / 1.135 Commercial Experience / 1.135 Bibliography / 1.135 Part 2 Olefins Chapter 2.1. Lurgi Megamethanol¡ Technology Tobias Oelmann and Martin Gorny 2.3 History / 2.3 Lurgi Megamethanol Technology / 2.4 Process Description / 2.5 Chapter 2.2. Axens On-Purpose 1-Butene and 1-Hexene Production Technologies Vinel Daniel-Jean, Liege Xavier, and Rolland Gildas 2.15 Introduction / 2.15 On-Purpose Dimerization and Trimerization Chemistry / 2.16 Economics / 2.18 Conclusion / 2.19 Chapter 2.3. BASF Selective and Full Hydrogenation Technology SELOPø Stefan Iselborn 2.21 Introduction / 2.21 History / 2.21 Process Description and Reactor Designs / 2.22 Process Safety and Hot Spot Prevention / 2.23 00_Meyers_FM_i-xxviii.indd 8 24/08/18 5:53 pm CONTENTS ix Characteristics of SELOP Hydrogenation Performance / 2.23 Catalysts for Hydrogenation Technologies / 2.28 Chapter 2.4. Lummus Ethylene Process Nicholas M. Kinnis, Peter Kuzma Jr., and William D. Quitmeier 2.29 Introduction / 2.29 Development and Commercial History / 2.29 Commercial Operations / 2.31 Process Chemistry / 2.33 Pyrolysis Reactions / 2.35 Ethylene Process Flow Schematic / 2.37 Refinery and Ethylene Plant Integration / 2.47 Recent Technology Advances / 2.47 Economic Aspects / 2.51 Chapter 2.5. Olefins Conversion Technology Kerman N. Dukandar and Daniel Mckenzie 2.53 Introduction / 2.53 Process Chemistry / 2.55 Process Description / 2.56 Process Advantages / 2.57 OCT Commercial Applications / 2.58 Flexible Reverse OCT / 2.64 Conclusion / 2.65 References / 2.66 Chapter 2.6. Lummus Methanol to Olefins Recovery and Olefin Interconversion Carmen A. Fornarotto and Dennis P. Maloney 2.67 Introduction / 2.67 Development and Commercial History / 2.67 Process Chemistry / 2.68 Process Description / 2.70 Process Economics / 2.73 Summary of Process Features / 2.74 Bibliography / 2.75 Chapter 2.7. INDMAX FCC: Advanced Fluid Catalytic Cracking Technology for Producing Petrochemicals Rama Rao Marri and Debasis Bhattacharyya 2.77 Introduction / 2.77 INDMAX FCC Process Description / 2.78 Bibliography / 2.88 Chapter 2.8. UOP Oleflex Process for Light Olefin Production Wolfgang Spieker, Gregory J. Nedohin, and Michael Marsh 2.89 Introduction / 2.89 Process Description / 2.90 Process Chemistry and Contaminants / 2.92 Oleflex Process Configurations and Conditions / 2.93 Commercial Experience / 2.95 00_Meyers_FM_i-xxviii.indd 9 24/08/18 5:53 pm

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