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Title: Desulfurization of coal in a fluidized bed reactor at elevated temperatures. [MS thesis; 53 references]

Technical Report ·
DOI:https://doi.org/10.2172/7337623· OSTI ID:7337623

In a batch, fluidized-bed reactor under essentially isothermal conditions the effectiveness of hydrogen and oxygen in the removal of sulfur from coal was evaluated at temperatures in the range of 220/sup 0/-410/sup 0/C, and compared with the desulfurization achieved due to thermal pyrolysis of coal. A statistical parametric study was done to determine the effects of temperature, type of treatment gas and the ash content on weight loss, volatile matter loss and sulfur removal from coal. The reactions of organic and pyritic sulfur were shown to be very temperature sensitive. The removal of organic sulfur is effected only by the thermal decomposition reactions during pyrolysis. Pyritic sulfur reacts appreciably with oxygen or hydrogen at 400/sup 0/C. After removal of the sulfurous gases and carbon dioxide, the heating value of the fuel gas evolved from coal was estimated to be 400 to 900 Btu/scf. The specific sulfur content (lb. S./MM Btu) of the char residue was not appreciably different from that of the feed coal. However, if the evolved gas is desulfurized and used with the char, the specific sulfur content of the overall product could be significantly reduced.

Research Organization:
Iowa State Univ. of Science and Technology, Ames (USA). Energy and Mineral Resources Research Inst.
DOE Contract Number:
W-7405-ENG-82
OSTI ID:
7337623
Report Number(s):
IS-ICP-31
Country of Publication:
United States
Language:
English