Supercritical water gasification of sewage sludge using bench-scale batch reactor: advantages and drawbacks

被引:44
作者
Sawai, Osamu [1 ]
Nunoura, Teppei [1 ]
Yamamoto, Kazuo [1 ]
机构
[1] Univ Tokyo, Ctr Environm Sci, Bunkyo Ku, Tokyo 1130033, Japan
关键词
Bench-scale batch reactor; Parameter effect; Heavy metal concentration; Gasification efficiency; PRESSURE AQUEOUS ENVIRONMENTS; BIOMASS GASIFICATION; HYDROGEN-PRODUCTION; HEATING RATE; HYDROTHERMAL GASIFICATION; CATALYST; HYDROPYROLYSIS; TEMPERATURE; GLUCOSE;
D O I
10.1007/s10163-013-0144-7
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Sewage sludge, a byproduct of municipal wastewater treatment, was gasified by supercritical water using a bench-scale batch reactor. Configuration of bench-scale batch reactor and operation procedures are discussed in detail. Experience and challenges that arose during the experiment are also shared. Using the bench-scale reactor under the condition of 600 A degrees C, 23 MPa, and a reaction time of 60 min without catalyst presence, a total gas yield of 9.8 mol/(kg-sewage sludge) was obtained. Furthermore, investigations on operational parameters were conducted. Extension of reaction time up to 60 min increased the gasification, reaching a plateau thereafter. Investigation on pressure indicated the superiority of supercritical pressure. The addition of Ni as a catalyst also promoted gasification, although inorganic salts and char seemed to cover the catalyst surface. With regard to the prospect of future operation at a municipal waste water treatment plant, the effect of operational parameters on heavy metal concentration in the liquid phase is also discussed.
引用
收藏
页码:82 / 92
页数:11
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