Syngas production from textile dyeing sludge via carbon dioxide-assisted pyrolysis

被引:0
作者
Park, Jonghyun [1 ]
Tsang, Yiu Fai [2 ,3 ]
Lee, Doyeon [4 ]
Cho, Seong-Heon [5 ]
Kwon, Eilhann E. [1 ]
机构
[1] Hanyang Univ, Dept Earth Resources & Environm Engn, Seoul 04763, South Korea
[2] Educ Univ Hong Kong, Dept Sci & Environm Studies, New Terr, Hong Kong 999077, Peoples R China
[3] Educ Univ Hong Kong, State Key Lab Marine Pollut, New Terr, Hong Kong 999077, Peoples R China
[4] Hanbat Natl Univ, Dept Civil & Environm Engn, Daejeon 305719, South Korea
[5] Pusan Natl Univ, Dept Civil & Environm Engn, Busan 46241, South Korea
基金
新加坡国家研究基金会;
关键词
Textile dyeing sludge; Waste-to-energy; Waste valorization; Catalytic pyrolysis; CO; 2; utilization; AROMATIC-HYDROCARBONS PAHS; COAGULATION-FLOCCULATION; HEAVY-METALS; CO2; TEMPERATURE; REMOVAL; WASTEWATERS; SPECIATION; CONVERSION; DYES;
D O I
10.1016/j.jaap.2024.106916
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
The textile dyeing process utilizing synthetic dyes generates by-products known as textile dyeing sludge (TDS), which comprises various harmful chemicals. However, disposal of TDS through conventional methods of waste present significant environmental hazards, leading to the dissemination of hazardous chemicals into the ecosystem. Therefore, this study introduces thermo-chemical platform for the disposal of TDS. Specifically, this study employs CO2 as a reactive feedstock to maximize the production of syngas and minimize formation of toxic chemicals. Prior to pyrolysis, the hazardous potential of TDS was qualitatively evaluated. The pyrolysis of TDS under CO2 environments demonstrated gas-phase reactions between volatile substances and CO2. These reactions led to increased CO production while simultaneously reducing the formation of toxic compounds such as benzene derivatives and polycyclic aromatic hydrocarbons (PAHs) within pyrogenic oil. The reduction in benzene derivatives and PAHs was quantified as -10.31 % under single-step pyrolysis and -25.16 % under multi-step pyrolysis. To expedite kinetics of gas-phase reactions, Ni-based catalyst was employed for catalytic pyrolysis of TDS. Compared to non-catalytic pyrolysis, the Ni catalyst enhanced CO production by expediting gas-phase reactions. Compared to multi-step pyrolysis under the CO2 condition (3.81 mol%), the CO formation from catalytic pyrolysis under CO2 condition exhibited significant enhancement (15.35 mol%). Consequently, all experimental results highlight potential of pyrolysis with CO2 as a promising method for the disposal of TDS, while converting it into valuable energy resources.
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页数:9
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