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Desulfurization of hot coal-gas in a high-pressure fluid-bed reactor

Conference · · Preprints of Papers, American Chemical Society, Division of Fuel Chemistry; (USA)
OSTI ID:6798918
;  [1];  [2]
  1. Research Triangle Institute, NC (USA)
  2. Morgantown Energy Technology Center, WV (USA)
Zinc ferrite, a regenerable mixed-metal oxide, is a leading sorbent for removal of H{sub 2}S from hot coal-derived gas streams for integrated gasification combined cycle (IGCC) applications. Due to several potential advantages of fluid-bed operation, a high-temperature high-pressure bench-scale reactor was constructed and commissioned for testing in the fluid-bed mode. Zinc ferrite was tested at a superficial velocity to minimum fluidization velocity ratio of 3.0. Multicycle testing at 15 atm and 600{degree}C with 5,000 ppmv H{sub 2}S in the inlet simulated fluid-bed coal gasifier (KRW) gas showed that zinc ferrite consistently reduced the H{sub 2}s to under 20 ppmv, in a single-stage fluidized bed at a superficial residence time of {approximately}3 seconds. Prior to reaching a bed outlet H{sub 2}S concentration of 100 ppmv, a sulfur pickup of 12 g per 100 g sorbent was achieved.
OSTI ID:
6798918
Report Number(s):
CONF-900402--
Conference Information:
Journal Name: Preprints of Papers, American Chemical Society, Division of Fuel Chemistry; (USA) Journal Volume: 35:1
Country of Publication:
United States
Language:
English