Multi-response optimization of sewage sludge-derived hydrochar production and its CO2-assisted gasification performance

被引:11
作者
Guo, Shuai [1 ,2 ]
Xu, DanDan [1 ,2 ]
Li, Xingcan [1 ,2 ]
Zhao, Chenchen [1 ,2 ]
机构
[1] Northeast Elect Power Univ, Sch Energy & Power Engn, Jilin 132012, Jilin, Peoples R China
[2] Harbin Boiler Co Ltd, Harbin 150046, Peoples R China
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2022年 / 10卷 / 01期
关键词
Sewage sludge; Hydrothermal carbonization; Gasification; Response surface methodology; Waste-to-energy; HYDROTHERMAL CARBONIZATION HTC; SOLID-FUEL; ENERGY; WASTE; TEMPERATURE; COMBUSTION; BIOMASS; CARBON; STRAW; LIQUEFACTION;
D O I
10.1016/j.jece.2021.107036
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The harmful effects of improper sewage sludge (SS) treatment on the environment inspire the search for more benign sludge processing techniques such as hydrothermal carbonization (HTC); the abundant organic matter in SS is used for energy recovery. Here, we aimed to optimize the HTC-based preparation of SS hydrochar and its gasification performance by using response surface methodology (RSM). Specifically, the hydrochar yield, higher heating value (HHV), and gasification activity index were selected as optimization goals, whereas carbonization temperature (160-260 degrees C), residence time (30-150 min), and acetic acid concentration (0-1.5 M) were selected as factors influencing the HTC process and CO2-assisted gasification performance. Carbonization temperature was the dominant parameter determining hydrochar yield, HHV, and gasification activity. The hydrochar yield (82.69%) and calorific value (7820.99 kJ kg(-1)) were maximized under comparatively mild conditions (160 degrees C, 30 min, and 0.07 M acetic acid), whereas the gasification activity index (0.288 s(-1)) was maximized under harsher conditions (211.34 degrees C, 88.16 min, and 1.58 M acetic acid). The results help to guide the HTC of SS intended for gasification, thus promoting the development of this promising waste-to-energy technology and may facilitate the design and further optimization of thermochemical SS conversion.
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页数:13
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