Gasification of Solid Fuels In Germany By The Lurgi, Winkler, and Leuna Slagging-type Gas-Producer Processes1 - 1947
William W. Odell2
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Introduction | 3 | ||
| Acknowledgements | 3 | |||
| The Lurgi pressure-gasification process | 5 | |||
| Major reactions involved | 5 | |||
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Effect of pressure upon the composition of the gas | 7 | ||
| The Lurgi gas generating plant and its operation | 9 | |||
| Operating results making gas in the Lurgi pressure generators at Böhlen, Germany | 12 | |||
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Capacity of the Lurgi generator and standard water-gas sets compared | 14 | ||
| Braunkohle used in German | 16 | |||
| Other reported data on the Lurgi gas-making process | 16 | |||
| Gasification at moderate pressure below 10 atmospheres of a brown coal of low tar content | 17 | |||
| Gasification of carbon at different pressures at 1,340º F. (theoretical values) | 18 | |||
| Results obtained in a small generator with an internal sectional area of approximately 10.765 square feet and using various fuels | 19 | |||
| Results obtained under test conditions on the small generator with an internal diameter of approximately 4 feet and which are said to be "average results" | 19 | |||
| Heat balance of pressure-gas operation of a small test generator using screened, partly dried, brown coal containing 27 percent moisture | 21 | |||
| Operation with various coals at 20 atmospheres absolute pressure | 21 | |||
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Factors relating to comparative costs | 22 | ||
| Relative costs of materials used in making water gas and pressure-process gas | 23 | |||
| Relative costs of materials used in making carbureted-water gas and Lurgi pressure process gas | 24 | |||
| Annual costs | 26 | |||
| The Winkler generator and gasification process | 27 | |||
| Kind of fuel adapted for use in a Winkler generator | 28 | |||
| Sizes and range in sizes of fuel used | 28 | |||
| Softening point of the fuel ash | 28 | |||
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Reactivity | 29 | ||
| Tar content of the fuel | 29 | |||
| Some results of operation of the Winkler process | 29 | |||
| Miscellaneous notes on operation at Zeitz | 31 | |||
| Operations of Winkler process at Leuna, Germany | 32 | |||
| Notes on the use of air instead of oxygen in making gas in a Winkler generator | 33 | |||
| The Leuna slagging-type gas producer | 34 | |||
| Composition of producer gas from coke | 35 | |||
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Remarks | 37 | ||
| The cost of oxygen | 38 | |||
| Summary and conclusions | 39 | |||
| Appendix | 42 | |||
| Data relating to the production of city gas and liquid fuel from oven gas and water gas in Fischer-Tropsch converters | 42 | |||
| Description of plant and proposed operating procedure | 43 | |||
1 The Bureau of Mines will welcome reprinting of this paper, provided the following footnote acknowledgment is used: "Reprinted from Bureau of Mines Information Circular 7415."
2 Former chief, Synthesis Gas Production Division, Office of Synthetic Liquid Fuels, Bureau of Mines, Washington, D. C.