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Ethylene-Vinyl Acetate Copolymers

Process Economics Program Report 155B

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Published September 2012

Despite the threat of linear low-density polyethylene (LLDPE) resin substitution, global ethylene-vinyl acetate (EVA) copolymers consumption continues to grow, with new capacity expansions expected. Although easier-processing LLDPE is being introduced, EVAs are still the easiest polymers to process for numerous applications. Its high melt strength makes it the material of choice for wide films, foam applications, and extrusion coating. Technology improvements enable increased plant capacities and higher operating efficiencies. While most of the newly installed LDPE/EVA capacities are based on tubular reactors, autoclave reactors are still relevant, especially for producing specialty-grade EVAs. 

This report reviews the technology and evaluates the process economics for producing EVAs with a high-pressure autoclave reactor process and a high-pressure tubular reactor process. Base case single-line capacities for both processes are 221 million lb/yr (100,000 metric ton/yr). Also discussed are the properties of the various grades of EVAs and the effect of the copolymerization processes on product properties.

In addition to present and future EVA producers, this report can assist high-pressure polyethylene manufacturers in their evaluation of whether to include EVAs in their product mix. EVA users can also benefit from the discussion on the economics of manufacturing the various grades of EVAs.

Other PEP Related Reports:

  • Ethylene Copolymers 155
  • Ethylene-Vinyl Acetate Copolymers 155A
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Table of Contents

Section Page Number

INTRODUCTION 1-1
SUMMARY 2-1
INDUSTRY STATUS 2-1
Consumption 2-1
Production 2-1
PRODUCTS AND PRODUCT PROPERTIES 2-2
Density 2-2
Vinyl Acetate Content 2-2
Melt Index 2-2
Molecular Weight, Molecular Weight Distribution and Molecular Branching 2-3
Other Physical Properties 2-3
Chemical and Electrical Properties 2-4
COMMERCIAL EVA PRODUCTS AND PROCESSING 2-4
Film Grades 2-4
Injection Molding Grades 2-4
Extrusion, Coextrusion, Coating, Lamination, Adhesive, and Hot-Melt Grades 2-4
Polymer Blending and Grafting Grades 2-5
PRODUCTS FROM AUTOCLAVE AND TUBULAR REACTOR PROCESSES 2-5
TECHNICAL ASPECTS 2-5
Initiator Preparation 2-6
Monomer Feed Preparation 2-6
Autoclave Reactor Processes 2-6
Tubular Reactor Processes 2-7
Autoclave Reactor Processes versus Tubular Reactor Processes 2-7
Product Finishing 2-8
Process Effluents 2-8
Modifying a High-Pressure LDPE Process for EVA Production 2-8
PROCESS ECONOMICS 2-8
An Autoclave Reactor Process 2-9
Cost Estimates 2-9
A Tubular Reactor Process 2-10
Cost Estimates 2-10
INDUSTRY STATUS 3-1
NORTH AMERICA 3-2
Production 3-2
Consumption 3-4
Trade 3-5
WESTERN EUROPE 3-6
MIDDLE EAST 3-8
OTHER AISA AND CHINA 3-9
REVIEW OF EVA PRODUCTS 4-1
FUNDAMENTAL STRUCTURE ATTRIBUTES 4-1
Vinyl Acetate Content 4-2
Molecular Weight and Molecular Weight Distribution 4-3
Molecular Branching 4-4
TYPICAL EVA PRODUCT PROPERTIES 4-4
Melt Index 4-5
Density 4-7
Other Physical Properties 4-8
Chemical and Electrical Properties 4-9
COMMERCIAL EVA PRODUCTS AND PROCESSING 4-10
Film Grades 4-10
Injection Molding Grades 4-11
Extrusion, Coextrusion, Coating, Lamination, Adhesive, and Hot-Melt Grades 4-12
Polymer Blending and Grafting Grades 4-13
PRODUCTS FROM AUTOCLAVE AND TUBULAR REACTOR PROCESSES 4-14
END USES 4-15
Adhesives 4-16
Films 4-17
Thermo Adhesive Films 4-18
Packaging 4-18
Cartons and Folding Boxes 4-18
Deep Freeze Packages 4-18
Bottle Labeling 4-18
Yogurt Labeling 4-19
Blow Molding and Foam Molding 4-19
Cables and Wires Applications 4-19
Extrusion, Coextrusion, Coating, Lamination 4-19
Injection Molding 4-19
Oil/Gasoil/Fuel Oil/Bitumen Additives and Asphalt Modifiers 4-20
Applications with High-growth Potential 4-21
Photovoltaic Cell and Protective Solar Film Applications 4-21
Medical and Pharmaceutical Applications 4-22
Formulations for Halogen-Free Flame Retardant (HFFR) Cables 4-22
REVIEW OF COMMERCIAL EVA PROCESSES 5-1
INTRODUCTION 5-1
Chemistry 5-2
Mechanism 5-3
CONTINUOUS BULK COPOLYMERIZATION 5-4
Initiator Preparation 5-5
Monomer Feed Preparation 5-7
Copolymerization 5-8
Autoclave Reactor Processes 5-8
Tubular Reactor Processes 5-9
Autoclave Reactor Processes versus Tubular Reactor Processes 5-10
Product Recovery 5-10
Product Finishing 5-11
Process Effluents 5-11
Modifying a High-Pressure LDPE Process for EVA Production 5-11
ENVIRONMENTAL 5-13
REVIEW OF SELECTED PROCESSES 5-14
LyondellBasell Lupotech™ T Tubular Reactor Process 5-14
LyondellBasell Autoclave Reactor Process 5-16
ExxonMobil’s LDPE-EVA Process Technology 5-17
Recent Licensing Activities 5-18
The Polimeri Europa Autoclave Reactor and Tubular Reactor Processes 5-19
Autoclave Reactor Process 5-20
Tubular Reactor Process 5-21
Recent Developments 5-22
SABTEC Clean Tubular Reactor (CTR) Process 5-22
DuPont Autoclave Process 5-23
Sumitomo Chemical Autoclave and Tubular Reactor Processes 5-24
Autoclave Reactor Process 5-25
Tubular Reactor Process 5-25
EVA COPOLYMERS BY AN AUTOCLAVE REACTOR PROCESS 6-1
BASE CASE 6-1
PROCESS DESCRIPTION 6-1
Polymerization 6-4
Product/Recycle Recovery 6-4
Product Finishing 6-5
PROCESS DISCUSSION 6-5
COST ESTIMATES 6-12
Capital Costs 6-12
Production Costs 6-15
EVA COPOLYMERS BY A TUBULAR REACTOR PROCESS 7-1
BASE CASE 7-1
PROCESS DESCRIPTION 7-1
Polymerization 7-4
Product/Recycle Recovery 7-4
Product Finishing 7-5
PROCESS DISCUSSION 7-5
COST ESTIMATES 7-12
Capital Costs 7-12
Production Costs 7-15
APPENDIX A PATENT SUMMARY TABLES A-1
APPENDIX B DESIGN AND COST BASES B-1
APPENDIX C CITED REFERENCES C-1
APPENDIX D PATENT REFERENCES BY COMPANY D-1
APPENDIX E PROCESS FLOW DIAGRAMS E-1

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