List of Illustrations

List of Tables

1.0

Introduction

2.0

Executive Summary

Westinghouse Gasifier Performance with Western Coal

Indirect Liquefaction of Illinois #6 Coal

2.3

Conclusions and Recommendations

2.3.1

Westinghouse Gasification

2.3.2

Indirect Liquefaction of Illinois #6 Coal

3.0

Indirect Liquefaction Using Westinghouse Fluid Bed Gasification

3.1

Introduction

3.2

Plant Configuration

3.3

Westinghouse Gasification

3.3.1

Gasifier Operation

3.3.2

Gasifier Performance

3.4

Synthesis Gas Preparation

3.5

Product Synthesis and Upgrading

3.5.1

Introduction

3.5.2

Performance of Plant Employing Synthol Synthesis

3.5.3

Performance of Plants Employing Kolbel Synthesis

3.6

Economic Comparisons

3.6.1

Plant Construction Costs

3.6.2

Product Costs

3.7

Environmental Considerations

4.0

Indirect Liquefaction Using Fixed Bed Gasification of Illinois #6 Coal

4.1

Introduction

4.2

Data Sources Used for Process Evaluation

4.2.1

Lurgi Dry-Ash

4.2.2

BGC Slagging Lurgi

4.3

General Plant Assumptions

4.4

System Description and Analyses

4.4.1

Dry-Ash Lurgi/Synthol

4.4.2

Plant Construction Cost

4.4.3

Product Costs

4.4.4

BGC Slagging Lurgi Systems

4.4.5

Plant Construction Cost

4.4.6

Product Costs

5.0

Indirect Liquefaction Using Entrained Gasification of Illinois #6 Coal

5.1

Introduction

5.2

Data Sources Used for Process Evaluation

5.2.1

Texaco

5.2.2

Shell-Koppers

5.3

Systems Descriptions and Analyses

5.3.1

Texaco

5.3.2

Plant Construction Costs

5.3.3

Product Costs

5.3.4

Shell Koppers

5.3.5

Plant Construction Costs

5.3.6

Product Costs

Appendix A  Plant Steam Coal Requirements

Appendix B  Shift Analysis

Appendix C  Computation of Entrained Gasifiers Product Gas Output

Appendix D  Gasoline Cost Computations

References