1 |
Introduction |
1 |
1.1 |
Authorization |
1-1 |
1.2 |
General Conclusions |
1-2 |
1.3 |
Scope of Evaluation |
1-3 |
1.4 |
Results and Specific Conclusions |
1-5 |
2 |
Basis of Study |
2 |
2.1 |
Base Case - GA/S&W Synthetic Pipeline Gas Process |
2-1 |
2.2 |
Comparable Coal-Fueled Coal Conversion Processes |
2-1 |
2.3 |
Sources of Cost Data |
2-1 |
2.4 |
Cost Factors and Methods Used |
2-2 |
2.5 |
Scaling Factors |
2-3 |
2.6 |
Types of Coal Used |
2-3 |
2.7 |
Efficiency |
2-4 |
2.8 |
Product Pressure |
2-4 |
3 |
Nuclear-Heated Coal Gasification
Processes |
3 |
3.1 |
GA/S&W Pipeline Gas Plan |
3-1 |
3.2 |
GA/S&W Synthesis Gas Plant |
3-10 |
3.3 |
GA/S&W Hydrogen Plant |
3-16 |
4 |
Coal-Fueled Coal Conversion Processes |
4 |
4.1 |
Lurgi Synthetic Pipeline Gas Plant |
4-1 |
4.2 |
Hygas Pipeline Gas Plant |
4-9 |
4.3 |
Koppers-Totzek Synthesis Gas Plant |
4-25 |
4.4 |
Koppers-Totzek Hydrogen Plant |
4-34 |
5 |
Coal Liquefaction |
5 |
5.1 |
Description of the Process |
5-1 |
5.2 |
Economic Evaluation |
5-4 |
5.3 |
Major Pollution Outputs |
5-6 |
5.4 |
References |
5-7 |
6 |
Application of Synthesis Gas to
Methanol Production |
6 |
6.1 |
Methanol Process Requirements |
6-1 |
6.2 |
Synthesis Gas Suitability |
6-2 |
6.3 |
Costs of Methanol from Selected Synthesis Gases |
6-4 |
6.4 |
References |
6-6 |
7 |
Application to Steel Production |
7 |
7.1 |
Nuclear Energy Applications in Steel Making |
7-1 |
7.2 |
Economics of Nuclear Steel Making |
7-3 |
7.3 |
Pollution |
7-8 |
7.4 |
Reference |
7-10 |
8 |
Westinghouse Hydrogen Production
Process |
8 |
8.1 |
Description of the Process |
8-1 |
8.2 |
Major Pollution Outputs |
8-4 |
8.3 |
Process Thermal Efficiency |
8-4 |
8.4 |
Costs |
8-5 |
8.5 |
References |
8-7 |