Noncaking Coal Gasified In A Stirred-Bed Producer

The National Institute for Occupational Safety and Health (NIOSH)
R. V. Rahfuse
Organization:
The National Institute for Occupational Safety and Health (NIOSH)
Pages:
11
File Size:
3316 KB
Publication Date:
Jan 1, 1974

Abstract

Noncaking 0- by 2 -inch subbituminous coal from New Mexico was gasified with air and steam at 205 prig using a stirred-bed producer to determine coal losses by entrainment in the gas for this low-sulfur, high-ash coal which contained 20 percent particles smaller than 1/16-inch sieve size. The use of fine-sized coal has particular importance because most production from mechanized mines is smaller than 2-inch size. This initial attempt showed technical feasibility for gasifying New Mexico subbituminous coal containing small-sized particles in fixed-bed producers without excessive coal loss by entrainment. Dust loss averaged about 2 percent of moisture-free coal, most of which was recovered from the gas. Ash clinkering was controlled by adding 1,010 lb/hr steam to reduce tempera¬tures in the combustion zone. Yield of low-Btu fuel gas, 150 Btu per scf, dry, amounted to 69,800 scfh from 1,490 lb/hr coal (as received) and 3,450 lb/hr air (dry).
Citation

APA: R. V. Rahfuse  (1974)  Noncaking Coal Gasified In A Stirred-Bed Producer

MLA: R. V. Rahfuse Noncaking Coal Gasified In A Stirred-Bed Producer. The National Institute for Occupational Safety and Health (NIOSH), 1974.

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