The degradation of phenol in aqueous solution by ozone oxidation has been studied in a microporous tube-in-tube microchannel reactor (MTMCR). The results indicated that the removal percentage of phenol decreased with increasing micropore size, annular channel width and initial phenol concentration, and increased with increasing ratio of gas volumetric flow rate to liquid volumetric flow rate and reaction temperature. It was also observed that the removal percentage of phenol initially increased, and subsequently decreased with increasing pH value. A phenol removal percentage of over 99% was achieved under the following reaction conditions: initial phenol concentration of 100mg/L, micropore size of 10μm, annular channel width of 250μm, ratio of gas volumetric flow rate to liquid volumetric flow rate of 13, pH value of 11 and reaction temperature of 25℃.
LI PengFei;LI WenJun;WANG JieXin;FU JiWen;CHEN JianFeng;SHAO Lei.
Degradation of phenol solution by ozone oxidation in a microporous tube-in-tube microchannel reactor[J]. Journal of Beijing University of Chemical Technology, 2011, 38(2): 12-16
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参考文献
1]陈思莉, 汪晓军, 顾晓扬, 等. 高级氧化处理苯酚废水的研究[J]. 环境科学与技术, 2008, 31(1): 96-99. Chen S L, Wang X J, Gu X Y, et al. Advanced oxidation process for phenol wastewater[J]. Environmental Science & Technology, 2008, 31 (1): 96-99. (in Chinese) [2]Amat A M, Arques A, Miranda M A, et al. Use of ozone and/or UV in the treatment of effluents from board paper industry[J]. Chemosphere, 2005, 6 0(8): 1111-1117. [3]Sarasa J, Cortés S, Ormad P, et al. Study of the aromatic byproducts formed from ozonation of anilines in aqueous solution [J]. Water Research, 2002, 36(12): 3035-3044. [4]史惠祥, 徐献文, 汪大翚. US/O3降解对硝基苯酚的影响因素及机理[J]. 化工学报, 2006, 57(2): 390-396. Shi H X, Xu X W, Wang D H. Influencing factors and mechanism of decomposition of 4-nitrophenol by US/O3[J]. Journal of Chemical Industry and Engineerin g (China), 2006, 57(2): 390-396. (in Chinese) [5]何志桥, 宋爽, 周华敏, 等. 臭氧/超声联合降解水中对氨基苯酚的动力学[J]. 化工学报, 2006, 57(12): 2964-2969. He Z Q, Song S, Zhou H M, et al. Kinetics of degradation of 4-aminophenol in aq ueous solution by ozonation combined with sonolysis[J]. Journal of Chemical Industry and Engineering (China), 2006, 57(12): 2964-2969. (in Chinese) [6]乐军, 陈光文, 袁权, 等. 微通道内气-液传质研究[J].化工学报, 2006, 57(6): 1296-1303. Le J, Chen G W, Yuan Q, et al. Mass transfer in gas-liquid flow in microchannels [J]. Journal of Chemical Industry and Engineering (China), 2006, 57(6): 1296 1303. (in Chinese) [7]Chen J F, Chen G Z, Wang J X, et al. High-throughput microporous tube-in-tube microreactor as novel gas-liquid contactor: mass transfer study [J]. AIChE Journal, (in press). [8]Yang Q, Wang J X, Shao L, et al. High Throughput Methodology for Continuous Preparation of Hydroxyapatite Nanoparticles in a Microporous Tube-in-Tube Microchannel Reactor[J]. Industrial & Engineering Chemistry Research, 2010, 49(1): 140-147. [9]沈耀良. 臭氧化水处理中的控制反应[J]. 水处理技术, 1986, 12(5): 297-299. Shen Y L. Control reaction in water treatment with ozone oxidization[J]. Techn ology of Water Treatment, 1986, 12(5): 297-299. (in Chinese) [10]帕特森 J W. 工业废水处理技术手册[M]. 北京: 化学工业出版社, 1993: 402-420. Patterson J W. Manual of Disposal Technology for Industrial Wastewater[M]. Beijing: Chemical Industry Press, 1993: 402-420. (in Chinese) [11]Hoigne J, Bader H. Rateconstants of reactions of ozone with organic and inorganic compounds in water-I. non-dissociating organic compounds[J]. Water Research, 1985, 17(2): 173-183. [12]杨正庆, 杨丽霞, 候一宁, 等. 臭氧氧化法处理实验室苯酚废水[J]. 环境科学与管理, 2006, 31(9): 119-122. Yang Z Q, Yang L X, Hou Y N, et al. Treatment for laboratory phenol wastewater with ozone oxidization method[J]. Environmental Science and Management, 2006, 31(9): 119-122. (in Chinese) [13]石新军. 超声强化臭氧降解高浓度苯酚废水研究[J]. 水科学与工程技术, 2006(4): 33-36. Shi X J. Study of organic wastewater degradation by ultrasound enhancement ozone oxidation [J]. Water Sciences and Engineering Technology, 2006(4): 33-36. (in Chinese)