A platform for research: civil engineering, architecture and urbanism
Auxiliary effect of CO2 on pyrolysis of oily sludge
The efficient recovery and conversion of energy in oily sludge has great prospects. In this article, the main objective is to investigate the impact of the addition of CO2 during the pyrolysis of oily sludge on energy recovery and conversion by thermogravimetric analysis (TGA) and compare the effect with the traditional pyrolysis effect from the perspective of thermal conversion behavior, products composition, and kinetics analysis. The results of the experiment showed that in the CO2 atmosphere, the main weight loss temperature of oily sludge was mainly concentrated in the range of 300–500 °C, which is lower than the reaction temperature range of traditional pyrolysis. The yields of CO and H2 in the products have been greatly improved, and the highest proportion in the gas products can reach 19.29% and 22.38%, respectively. The E a (activation energy) values of oily sludge were determined to be in the range of 40–120 kJ·mol−1 with the conversion between 0.2 and 0.8 via DAEM, KAS, Starink, and FWO methods, respectively, in which the FWO method has shown the strongest adaptability. The results of this study provide reference values for practical engineering applications.
Auxiliary effect of CO2 on pyrolysis of oily sludge
The efficient recovery and conversion of energy in oily sludge has great prospects. In this article, the main objective is to investigate the impact of the addition of CO2 during the pyrolysis of oily sludge on energy recovery and conversion by thermogravimetric analysis (TGA) and compare the effect with the traditional pyrolysis effect from the perspective of thermal conversion behavior, products composition, and kinetics analysis. The results of the experiment showed that in the CO2 atmosphere, the main weight loss temperature of oily sludge was mainly concentrated in the range of 300–500 °C, which is lower than the reaction temperature range of traditional pyrolysis. The yields of CO and H2 in the products have been greatly improved, and the highest proportion in the gas products can reach 19.29% and 22.38%, respectively. The E a (activation energy) values of oily sludge were determined to be in the range of 40–120 kJ·mol−1 with the conversion between 0.2 and 0.8 via DAEM, KAS, Starink, and FWO methods, respectively, in which the FWO method has shown the strongest adaptability. The results of this study provide reference values for practical engineering applications.
Auxiliary effect of CO2 on pyrolysis of oily sludge
Wang, Ziyi (author) / Wang, Zhenbo (author) / Gong, Zhiqiang (author) / Li, Xiaoyu (author) / Chu, Zhiwei (author) / Du, Lianmeng (author) / Wu, Jinhui (author) / Jin, Zhiying (author)
Journal of Environmental Science and Health, Part A ; 57 ; 460-469
2022-05-12
10 pages
Article (Journal)
Electronic Resource
Unknown
Online Contents | 2012
|Continuous Pyrolysis Technology for Oily Sludge Treatment in the Chain-Slap Conveyors
DOAJ | 2019
|Modified asphalt mortar based on oily sludge pyrolysis residues, and preparation method thereof
European Patent Office | 2021
|