PROCESS ECONOMICS PROGRAM

Transcription

1 PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Abstract Menlo Park, California Process Economics Program Report No. 189 THERMOPLASTIC POLYESTERS (January 1987) This report presents modern processes and manufacturing costs for polyethylene terephthalate (PET) and polybutylene terephthalate (PBT), and the costs for converting these materials into special grades of resins, specifically, the engineering resin grades for both PET and PBT, and bottle-grade (IV = 0.72) and "specialty*' resin grade (IV 1.04) PET. Another important feature in this report is the evaluation of a new route to 1,4-butanediol (l,&bd), currently under development by Union Carbide, but based on the initial work done by Davy McKee. Recently, the process was also licensed to Standard Oil Company (Cleveland). For comparison, we present updated costs for the conven- tional route to l,&bd, the acetylene/formaldehyde route. This report summarizes many of the patents on PET, PBT, and 1,4-BD manufacture (and related subjects) that have been granted since our last major reports on PET (18A, January 1972) and PBT/1,4-BD (96A, November 1977). Also included is a section on the industry status of PET, PBT, and 1,4-BD, and a section on the basic chemistry of the evalu- ated processes. PEP'85 LME

2 Report No. 189 THERMOPLASTIC POLYESTERS by LLOYD M. ELKIN With Contributions by ABDULRHMAN A. AL DAYEL a cl m A private report by the January 1987 PROCESS ECONOMICS PROGRAM Menlo Park, California 94025

3 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLD PETROCHEMICALS Program covers major hydrocarbons and their derivatives on a worldwide basis. In addition, the SRI DIRECTORY OF CHEMICAL PRODUCERS services provide detailed lists of chemical producers by company, product, and plant for the United States and Western Europe. ii

4 CONTENTS 1 INTRODUCTION SUMMARY General Aspects Economic Aspects Technical Aspects and and 1,4-Butanediol ,4-Butanediol from Maleic Anhydride, Diethyl Maleate Intermediate ,4-Butanediol from Acetylene and Formaldehyde Polyethylene Terephthalate, Solid State Polymerization to Bottle Grade and Specialty Grade Resins Compounding Polybutylene Terephthalate and Polyethylene Terephthalate with Glass Fibers INDUSTRY STATUS Polyester Engineering Resins Polyethylene Terephthalate, Other Applications l,&butanediol CHEMISTRY Polyethylene Terephthalate..... Polyethylene Terephthalate..... Polybutylene Terephthalate 1,4-Butanediol ,4-Butanediol from Maleic from Terephthalic Acid and ;r~m'd;rn;t~y; ie;,ph;h;l;t; ini ;,h'd;m~thy; ie;eih;h&; ini kiyrir;dl POLYETHYLENE TEREPHTHALATE FROM TEREPHTHALIC ACID AND ETHYLENEGLYCOL Process Review Reaction Conditions Catalysts Reactor Design Coupling or Linking Agents Purification iii

5 CONTENTS 5 POLYETHYLENE TEREPHTHALATE FROMTEREPHTHALIC ACID AND ETHYLENE GLYCOL (Continued) Equipment Cleaning Methods... Solid Phase Polymerization... Ethylene Oxide... Polyethylene Terephthalate Scrap Recovery... Process Description... Process Discussion... Davy McKee/Zimmer Brochures... Reactor Residence Times... Recycle of Reaction Mixture... Side Reactions... Plant Size... Refrigeration in Vacuum System... Vacuum Jets... Heating System.... Delusterant... Alternative Design and Costs... Capital Costs... Production Costs... Reactor Costs... Wiped Thin-Film Reactors... Cost Case, Direct Recycle of POLYETHYLENE TEREPHTHALATE FROM DIMETHYL TEREPHTHALATE AND ETHYLENEGLYCOL Process Review Process Description Process Discussion Davy McKee/Zimmer Brochures Side Reactions Catalyst/Stabilizer System Residence Time in Prepolycondensation Reactors Capital Costs Production Costs Reactor Costs POLYBUTYLENE TEREPHTHALATF, FROMDIMETHYL TEREPHTHALATE AWD 1,4-BUTAWEDIOL Process Review Process Description iv

6 CONTENTS 7 POLYBUTYLENE TEREPRTHALATg FROMDIMETRYL l,&butanediol Process Discussion Design Basis Reactor Design-Material Balance... Reactor Design, Construction Details. Vacuum System Methanol Recovery Overall Yield Capital Costs, Design Case Production Costs, Design Case..... Capital and Production Costs, High Intrinsic Viscosity Case..... Thin Film Reactors TEJUIPHTHALATE AND ,4-BUTANEDIOL FROM MALEIC ANHYDRIDE Process Review Process Description Process Discussion Esterification Reactor Hydrogenolysis Reactors Separation of Tetrahydrofuran, Water, and Ethanol by Distillation Capital and Production Costs, Maleic Anhydride Capital and Production Costs, Acetylene and Formaldehyde Feed Cost Comparison and Discussion Concurrent Production of Y-Butyrolactone... Effect on Costs of Process Improvements... New Process for Maleic Anhydride ie;d' POLYETHYLENE TEREPHTHALATE, COST OF SOLID STATE POLYMERIZATION POLYESTER COMPOUNDING COSTS APPENDIX A EQUIPMENT SUPPLIERS CITED REFERENCES PATENT BEFEEENCES V

7 ILLUSTBATIONS 5.1 Polyethylene Terephthalate from Terephthalic Acid Foldout Foldout and 1,4-Butanediol Foldout ,4-Butanediol from Maleic Anhydride (Diethyl Maleate Intermediate) Foldout Polyethylene Terephthalate, IWO.72 (Bottle Grade) from PET, IWO.6 Foldout Glass-Filled Polyester Foldout Vii

8 TABLES Polyethylene Terephthalate and Polybutylene Terephthalate Polymer Chips Manufacturing Cost Comparisons Glass-filled Polyethylene Terephthalate and Polybutylene Terephthalate Manufacturing Cost Comparisons Special Polyethylene Terephthalate Products Made by Solid State Polymerization Cost Summary ,4-Butanediol Manufacturing Cost Comparisons Polyethylene Terephthalate and Polybutylene Terephthalate Manufacturing Processes Sunvnary of Process Design Operating Conditions Producers of PET Engineering Resins Producers of PBT Engineering Resins Polyethylene Terephthalate Capacities for Fibers, Films, and Resins Polyethylene Terephthalate Production Capacity United States Polyethylene Terephthalate Production Capacity Western Europa Polyethylene Terephthalate Production Capacity Japan Producers of 1,4-Butanediol PatentSummary Recovery of Polyethylene Terephthalate Scrap Patent Summary Major Equipment Utilities Summary IX

9 TABLES Stream Flows Esterification Reactor Conditions Conditions in Pre- and Final Polycondensation Reactors Total Capital Investment Production Costs c Total Capital Investment Production Costs PatentSummary MajorEquipment Utilities Summary Stream Flows Summary of Transesterification Reaction Conditions X

10 TABLES Summary of Pre- and Final Polycondensation Reactor Conditions Total Capital Investment , Production Costs and 1,4=Butanediol PatentSummary and 1,4-Butanediol Major Equipment and l,&butanediol Utilities Summary and 1,4-Butanediol Stream Flows and l,&butanediol Summary of Transesterification Reactor Conditions... and'l,q-butanediol Summary of Pre- and Final Polycondensation Reactor Conditions and 1,4-Butanediol Total Capital Investment and l,&butanediol Production Costs and 1,4-Butanediol Total Capital Investment Xi

11 TABLES 7.10 and 1,4-Butanediol Production Costs ,4=Butanediol from Acetylene and Formaldehyde PatentSummary ,4-Butanediol from Butadiene PatentSummary ,4-Butanediol from Ally1 Alcohol Patent Summary ,4=Butanediol from Maleic Anhydride Patent Summary ,4-Butanediol, Miscellaneous Processes PatentSummary ,4-Butanediol from Maleic Anhydride Major Equipment ,4-Butanediol from Maleic Anhydride Utilities Summary ,4-Butanediol from Maleic Anhydride (Diethyl Maleate Intermediate) Stream Flows ,4-Butanediol from Maleic Anhydride (Diethyl Maleate Intermediate) Esterification Reactor Conditions ,4-Butanediol from Maleic Anhydride (Diethyl Maleate Intermediate) Hydrogenation Reactor Conditions ,4-Butanediol from Maleic Anhydride Total Capital Investment ,/r-Butanediol from Maleic Anhydride Capital Investment by Section ,4-Butanediol from Maleic Anhydride Production Costs ,4-Butanediol from Maleic Anhydride Direct Operating Costs by Section ,4-Butanediol from Acetylene and Formaldehyde (Butynediol Intermediate) Total Capital Investment Xii

12 TABLES ,4-Butanediol from Acetylene and Formaldehyde (Butynediol Intermediate) Capital Investment by Section ,4=Butanediol from Acetylene and Formaldehyde (Butynediol Intermediate) Production Costs ,4-Butanediol from Acetylene and Formaldehyde (Butynediol Intermediate) Direct Operating Costs by Section Polyethylene Terephthalate, IVsO.72 (Bottle Grade) from PET, IVoO.6 Major Equipment ' Polyethylene Terephthalate, IVsO.72 (Bottle Grade) from PET, IV=O.6 Utilities Summary Polyethylene Terephthalate, IVoO.72 (Bottle Grade) from PET, IV=O.6 Stream Flows Polyethylene Terephthalate, IV=O.72 (Bottle Grade) from PET, IV=O.6 Total Capital Investment Polyethylene Terephthalate, IVb0.72 (Bottle Grade) from PET, IV=O.6 Production Costs Polyethylene Terephthalate, IVz1.04 (Special Grade) from PET, IV=O.6 Total Capital Investment Polyethylene Terephthalate, IV=1.04 (Special Grade) from PET, IVpO.6 Production Costs Polyethylene Terephthalate, Solid State Polymerization Cost Comparison Polyester (Glass Filled, 30 WtX) from Polyester and Glass Fibers Major Equipment xiii

13 TABLES 10.2 Polyester (Glass Filled, 30 Wt%) from Polyester and Glass Fibers Utilities Summary Polyester (Glass Filled, 30 Wt%) from Polyester and Glass Fibers Total Capital Investment Polyethylene Terephthalate (Glass Filled, 30 WtX) from Polyethylene Terephthalate and Glass Fibers Production Costs Polybutylene Terephthalate (Glass Filled, 30 WtX) from Polybutylene Terephthalate and Glass Fibers Production Costs , xiv