Kinetics of the direct reaction between ozone and phenol by high-gravity intensified heterogeneous catalytic ozonation
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Kinetics of the direct reaction between ozone and phenol by high-gravity intensified heterogeneous catalytic ozonation
Chinese Journal of Chemical EngineeringVol. 53, Issue 1, Pages: 317-323(2023)
Affiliations:
Shanxi Province Key Laboratory of Higee-Oriented Chemical Engineering, North University of China,Taiyuan,China,030051
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Published:2023
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Kechang Gao, Shengjuan Shao, Zhixing Li, Jiaxin Jing, Weizhou Jiao, Youzhi Liu. Kinetics of the direct reaction between ozone and phenol by high-gravity intensified heterogeneous catalytic ozonation[J]. Chinese Journal of Chemical Engineering, 2023, 53(1): 317-323.
DOI:
Kechang Gao, Shengjuan Shao, Zhixing Li, Jiaxin Jing, Weizhou Jiao, Youzhi Liu. Kinetics of the direct reaction between ozone and phenol by high-gravity intensified heterogeneous catalytic ozonation[J]. Chinese Journal of Chemical Engineering, 2023, 53(1): 317-323.DOI:
Kinetics of the direct reaction between ozone and phenol by high-gravity intensified heterogeneous catalytic ozonation
high-gravity intensified heterogeneous catalytic ozonation is utilized for treatment of phenol-containing wastewater
and the kinetics of the direct reaction between ozone and phenol in the presence of excess tertiary butanol (TBA) is investigated. It is revealed that the direct reaction between ozone and phenol in the rotating packed bed (RPB) follows the pseudo-first-order kinetics with a reaction rate constant higher than that in the conventional bubbling reactor (BR). Under different conditions of temperature
initial pH
high-gravity factor
and gaseous ozone concentration
the apparent reaction rate constant varies in the range of 0.0160–0.115 min
-1
. An empirical power-exponential model is established to characterize the effects of these parameters on the direct reaction between ozone and phenol by high-gravity intensified heterogeneous catalytic ozonation.
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