书名:PEP Report 290 Bio-Butadiene
责任者:By Dipti Dave and Susan Bell | Dave, Dipti | Bell, Susan
出版时间:2014
出版社:IHS Chemical
前言
The global butadiene market, with current annual production at about 11 million MT and valued at $30-40 billion, is slated to grow at 4.1% per year through 2016. Approximately two-thirds of the butadiene produced is used in synthetic rubber manufacturing. This growth is primarily based on increased demand via derivative expansion and rapid economic growth, particularly in Asia.
High crude oil prices and low natural gas prices in the U.S. have caused petrochemical companies to shift from oil-based naphtha cracking to natural gas-based ethane cracking, and have resulted in reduced butadiene supply. This has spurred interest in on-purpose butadiene production both from conventional feedstocks and renewable feedstocks.
Meanwhile, there has been great interest in green tires, which are manufactured from synthetic rubber derived from bio-based monomers such as bio-isoprene and bio-butadiene. Indeed, the bio-butadiene area is particularly active with companies including Genomatica and Cobalt Technologies announcing their plans to commercialize in the next five years.
IHS Chemical Process Economics Program (PEP) has reviewed the latest patents and selected open literature made available by the companies mentioned above. Comparative process design and economics are provided for the production of 220 million lb/yr (100,000 ton/yr) of bio-based 1,3-butadiene. These bio-processes will be compared to the dominant, conventional process for butadiene production to understand its feasibility. This report is of interest to biochemical companies, Asian chemical companies in expansion mode, global petrochemical companies seeking to reduce their environmental footprint and polymer/plastic/rubber industries that rely on butadiene as a raw material.
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目录
1. Introduction 1
Background 1
Bio-Based Production Routes 2
Feedstock Properties 3
Cobalt Technologies Process 3
Genomatica Indirect Process 4
Genomatica Direct Process 4
Product Properties 5
Report Overview 5
2. Summary 6
Introduction 6
Global Butadiene Demand 7
Global Butadiene Growth 8
Technologies Covered 8
Cobalt Process Technology 8
Process Sections 9
Chemistry – Cobalt Process 9
Genomatica Indirect Process Technology 10
Genomatica Direct Process Technology 11
Existing Conventional Butadiene Technology 12
Feedstock Pricing 12
Effect of Glucose Cost 12
Economic Summaries: Production Costs 14
Cobalt Process at Different Glucose Feedstock Costs 18
Genomatica Indirect Process at Different Glucose Feedstock Costs 18
Genomatica Direct Process at Different Glucose Feedstock Costs 19
Conclusion 19
3. Industry status 20
Introduction 20
Uses 21
Butadiene Demand 23
Butadiene Supply 26
Crude C4 27
Butadiene 28
Prices 30
Mixed C4s 30
1,3 Butadiene 31
Specifications 34
C4 Stream 34
1,3 Butadiene 35
Plant Capacity 37
New Capacity 43
Bio-Butadiene developments 44
4. Technology review 45
Introduction 45
Cobalt Technologies' Bio-Butanol 45
Manufacturing of bio-butanol by different routes 45
Cobalt Immobilized Cell Bioreactor 46
Bioreactor concept nomenclature 47
Cobalt Technologies Fermentation Flow Scheme 48
Product Recovery 49
1,3-Butadiene Production by an Indirect technology 50
Fermentation 51
Conversion Pathways to 1,3-BDO 51
1,3-BDO Recovery 55
1,3-BDO Dehydration to 1,3-Butadiene 56
1,3-Butadiene Recovery and Purification 57
1,3-Butadiene Production by a Direct Technology 57
Fermentation 58
1,3-Butadiene Recovery and Purification 62
By-Product Recovery 63
5. Cobalt Process for Bio-Butadiene 64
Introduction 64
Cobalt Technology 64
Process Sections 64
Chemistry 65
Basis for Design and Evaluation 65
Process Description 68
Section 100 and 200 –Media Preparation and Fermentation 69
Section 300 – Separation and Recovery 70
Section 400 – Dehydration of Butanol 70
Section 500 & 600 Oxidative Dehydrogenation of Butenes & Butadiene Extraction 71
Stream Flows 71
Major equipment and utilities summary 74
Process discussion 77
Heat-Exchanger Sizing 78
Product Recovery 79
Offsite Storage 79
Environmental 79
Cost estimates 80
Fixed-Capital Costs 81
Production Costs 81
Effect of Glucose Cost 88
6. Economic Evaluation of Bio-Based 1,3-Butadiene Production by an Indirect Route via 1,3 Butanediol 92
Introduction 92
1,3-Butadiene Production by an Indirect Route 92
Fermentation 93
Conversion Pathways to 1,3-BDO 93
1,3-BDO Recovery 98
1,3-BDO Dehydration to 1,3-Butadiene 98
1,3-Butadiene Recovery and Purification 100
Process Description 100
Section 100 –Fermentation 107
Section 200 – BDO Recovery 108
Section 300 – Butadiene Production 108
Cost Estimates 109
Capital Costs 109
Production Costs 112
Effect of Glucose Cost 115
7. Economic Evaluation of Bio-Based 1,3-Butadiene Production by a Direct Route 118
Introduction 118
1,3-Butadiene Production by a Direct Route 118
Fermentation 119
1,3-Butadiene Recovery and Purification 123
By-Product Recovery 123
Process Description 124
Section 100 –Fermentation 132
Section 200 – Butadiene Recovery and Purification 132
Section 300 – By-Product Recovery 132
Cost Estimates 133
Capital Costs 133
Production Costs 136
Effect of Glucose Cost 139
Appendix A: Patent Summary Tables 143
Appendix B: Design and cost bases 154
Design Conditions 154
Cost Bases 154
Capital Investment 154
Project Construction Timing 156
Available Utilities 156
Production Costs 156
Effect of Operating Level on Production Costs 157
Appendix C: Cited references 158
Appendix D: Patent references by company 163
Appendix E: Process Flow Diagrams 165
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