Catalytic co-pyrolysis of food waste digestate and corn husk with CaO catalyst for upgrading bio-oil

被引:48
作者
Chen, Minzi [1 ]
Zhang, Shuping [1 ]
Su, Yinhai [2 ]
Niu, Xin [2 ]
Zhu, Shuguang [1 ,2 ]
Liu, Xinzhi [1 ]
机构
[1] Nanjing Univ Sci & Technol, Sch Energy & Power Engn, Nanjing 210094, Jiangsu, Peoples R China
[2] Nanjing Univ Sci & Technol, Sch New Energy, Jiangyin 214443, Jiangsu, Peoples R China
基金
中国国家自然科学基金; 中国博士后科学基金;
关键词
Food waste digestate disposal; CaO catalysts; Bio-oil; Nitrogen-containing compounds; SEWAGE-SLUDGE; FERMENTATION RESIDUES; ANAEROBIC-DIGESTION; ALKALI LIGNIN; RICE HUSK; BIOMASS; MICROALGAE; NITROGEN; BEHAVIOR; SAWDUST;
D O I
10.1016/j.renene.2021.12.139
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Catalytic co-pyrolysis behavior of food waste digestate (FD) and corn husk (CH) with CaO catalysts derived from calcining calcium hydroxide (CH-CaO) and calcium acetate monohydrate (CA-CaO) for upgrading bio-oil was studied. For co-pyrolysis process, the char yield decreased while the bio-oil and non-condensable gas yields increased with the CH/FD mass ratio increased. Compared to co-pyrolysis without catalysts, the relative contents of acids and esters in bio-oil decreased while the phenols increased in the case of catalytic co-pyrolysis. The relative contents of nitrogen-containing compounds (NCCs) increased with the presence of CaO catalysts. When the CH/FD mass ratio was 1/4, the relative content of nitrogen-containing components in bio-oil was 41.42% for co-pyrolysis without CaO catalysts, but increased to 45.10% and 52.03% with CH-CaO and CA-CaO catalysts, respectively. CaO catalysts also reduced the content of CO2 and increased the contents of H-2, CO and CH4 in non-condensable gas. Compared to CH-CaO, CA-CaO exhibited better catalytic performance for upgrading bio-oil for the more developed porous structure and more basic sites. Furthermore, a reaction pathway and mechanism of main NCCs formation during co-pyrolysis of FD and CH with CaO catalysts was proposed. (c) 2022 Elsevier Ltd. All rights reserved.
引用
收藏
页码:105 / 114
页数:10
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