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通过电化学氧化处理聚合物工艺中的一氯苯。

Treatment of Monochlorobenzene from Polymers Process through Electrochemical Oxidation.

作者信息

Wang Baiqi, Yue Yanmin, Wang Siyi, Fu Yu, Yin Chengri, Jin Mingji, Quan Yue

机构信息

Department of Agricultural Resources and Environment, Yanbian University, Yanji 133002, China.

Department of Chemistry, Yanbian University, Yanji 133002, China.

出版信息

Polymers (Basel). 2024 Jan 26;16(3):340. doi: 10.3390/polym16030340.

DOI:10.3390/polym16030340
PMID:38337229
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC10857403/
Abstract

With the rapid development of the economy and the demands of people's lives, the usage amount of polymer materials is significantly increasing globally. Chlorobenzenes (CB) are widely used in the industrial, agriculture and chemical industries, particularly as important chemical raw materials during polymers processes. CB are difficult to remove due to their properties, such as being hydrophobic, volatile and persistent and biotoxic, and they have caused great harm to the ecological environment and human health. Electrochemical oxidation technology for the treatment of refractory pollutants has been widely used due to its high efficiency and easiness of operation. Thus, the electrochemical oxidation system was established for the efficient treatment of monochlorobenzene (MCB) waste gas. The effect of a single factor, such as anode materials, cathode materials, the electrolyte concentration, current density and electrode distance on the removal efficiency (RE) of MCB gas were first studied. The response-surface methodology (RSM) was used to investigate the relationships between different factors' conditions (current density, electrolyte concentration, electrode distance), and a prediction model was established using the Design-Expert 10.0.1 software to optimize the reaction conditions. The results of the one-factor experiments showed that when treating 2.90 g/m MCB gas with a 0.40 L/min flow rate, Ti/TiO as an anode, stainless steel wire mesh as a cathode, 0.15 mol/L NaCl electrolyte, 10.0 mA/cm current density and 4.0 cm electrode distance, the average removal efficiency (RE), efficiency capacity (EC) and energy consumption (Esp) were 57.99%, 20.18 g/(m·h) and 190.2 (kW·h)/kg, respectively. The results of the RSM showed that the effects of the process parameters on the RE of MBC were as follows: current density > electrode distance > electrolyte concentration; the interactions effects on the RE of MBC were in the order of electrolyte concentration and current density > current density and electrode distance > electrolyte concentration and electrode distance; the optimal experimental conditions were as follows: the concentration of electrolyte was 0.149 mol/L, current density was 18.11 mA, electrode distance was 3.804 cm. Under these conditions, the RE achieved 66.43%. The response-surface variance analysis showed that the regression model reached a significant level, and the validation results were in agreement with the predicted results, which proved the feasibility of the model. The model can be applied to treat the CB waste gas of polymer processes through electrochemical oxidation.

摘要

随着经济的快速发展和人们生活需求的提高,全球高分子材料的使用量显著增加。氯苯(CB)广泛应用于工业、农业和化学工业,尤其是作为聚合物生产过程中的重要化工原料。由于氯苯具有疏水性、挥发性、持久性和生物毒性等特性,难以去除,对生态环境和人类健康造成了极大危害。电化学氧化技术因其高效性和易操作性,已被广泛用于处理难降解污染物。因此,建立了电化学氧化系统用于高效处理一氯苯(MCB)废气。首先研究了阳极材料、阴极材料、电解液浓度、电流密度和电极间距等单因素对MCB气体去除效率(RE)的影响。采用响应面法(RSM)研究了不同因素条件(电流密度、电解液浓度、电极间距)之间的关系,并使用Design-Expert 10.0.1软件建立了预测模型以优化反应条件。单因素实验结果表明,当以0.40 L/min的流量处理2.90 g/m的MCB气体时,以Ti/TiO为阳极,不锈钢丝网为阴极,电解液为0.15 mol/L NaCl,电流密度为10.0 mA/cm²,电极间距为4.0 cm时,平均去除效率(RE)、去除容量(EC)和能耗(Esp)分别为57.99%、20.18 g/(m³·h)和190.2 (kW·h)/kg。RSM结果表明,工艺参数对MBC去除效率的影响顺序为:电流密度>电极间距>电解液浓度;对MBC去除效率的交互作用影响顺序为:电解液浓度和电流密度>电流密度和电极间距>电解液浓度和电极间距;最佳实验条件为:电解液浓度为0.149 mol/L,电流密度为18.11 mA,电极间距为3.804 cm。在此条件下,去除效率达到66.43%。响应面方差分析表明回归模型达到显著水平,验证结果与预测结果一致,证明了模型的可行性。该模型可应用于通过电化学氧化处理聚合物生产过程中的CB废气。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/4d2dd5967f82/polymers-16-00340-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/08caf5233788/polymers-16-00340-g001.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/17566ff7b952/polymers-16-00340-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/ef81621c3987/polymers-16-00340-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/2375c37097ad/polymers-16-00340-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/4d2dd5967f82/polymers-16-00340-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/08caf5233788/polymers-16-00340-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/3a204f33af63/polymers-16-00340-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/914e60813f5c/polymers-16-00340-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/c2fb996e297c/polymers-16-00340-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/2133f3eb24e5/polymers-16-00340-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/e4800c5aabbb/polymers-16-00340-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/17566ff7b952/polymers-16-00340-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/ef81621c3987/polymers-16-00340-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/2375c37097ad/polymers-16-00340-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/14a9/10857403/4d2dd5967f82/polymers-16-00340-g010.jpg

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