Air co-gasification of coal and dried sewage sludge in a two-stage gasifier: Effect of blending ratio on the producer gas composition and tar removal

被引:40
|
作者
Jeong, Yong-Seong [1 ]
Choi, Young-Kon [2 ]
Park, Ki-Bum [2 ]
Kim, Joo-Sik [1 ,2 ]
机构
[1] Grad Sch Environm Engn, Seoul, South Korea
[2] Univ Seoul, Grad Sch Energy & Environm Syst Engn, 163 Siripdaero, Seoul 02504, South Korea
关键词
Two-stage gasification; Co-gasification; Hydrogen; Tar; Coal; Dried sewage sludge; FLUIDIZED-BED GASIFICATION; BIOMASS GASIFICATION; BITUMINOUS COAL; FIXED-BED; STEAM GASIFICATION; ACTIVATED CARBON; CHAR; PYROLYSIS; OIL; REACTIVITY;
D O I
10.1016/j.energy.2019.07.093
中图分类号
O414.1 [热力学];
学科分类号
摘要
The co-gasification of coal and dried sewage sludge (DSS) was conducted using a two-stage gasifier consisting of a fluidized bed gasifier and a tar-cracking reactor. In this study, the effect of the blending ratio of coal and DSS was investigated. Producer gases that were obtained from the tar-cracking reactor filled with active carbon contained high levels of hydrogen (maximum H-2: 27.7 vol%) and low tar contents (minimum tar: 0 mg/Nm(3)). Upon gasification of the coal/DSS blends, the hydrogen content decreased and tar content increased with increasing DSS. Blends with coal/DSS ratios of 70/30 and 50/50 showed a synergetic effect on tar reduction, which could be attributed to the high ash content of the DSS. The gasification of the 70% DSS blend increased the condensed tar yield by only 0.1 wt%, compared to coal gasification. Lastly, a hot filter filled with Fe-impregnated active carbon was applied to completely remove tar from producer gas, which led to the production of a tar-free and hydrogen-rich gas (30 vol%). Furthermore, the Fe-impregnated active carbon reduced the H2S content to 229 ppmv. In summary, it was possible to produce a clean gas from coal and DSS blends in the UOS gasification process. (C) 2019 Elsevier Ltd. All rights reserved.
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页码:708 / 716
页数:9
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