提高碱性稳定性的双极膜电渗析法回收石油废水中苯酚的表征与优化

IF 5.5 Q1 ENGINEERING, CHEMICAL
Ahmad Beiranvand , Mohammad Reza Omidkhah , Mahmoud Moharrami , Susan Davari , Hamidreza Mahdavi
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引用次数: 0

摘要

用双极膜(EDBM)系统电渗析从水溶液中提取苯酚的纯度和回收率主要取决于溶液的pH值,可能仅在碱性条件下有效,因为苯酚是一种非常弱的酸,pKa为10。本研究以1,4-重氮杂环[2.2.2]辛烷(DABCO)为季铵基,以双环有机化合物为基料,成功制备了具有高化学稳定性的单片双极膜。利用FTIR、FESEM、膜在碱性溶液中的化学稳定性和电阻对bpm进行了表征。比较DABCO合成的bpm的性能,发现膜的化学稳定性和电阻性都令人满意。将单片复合双极膜用于双极膜电渗析去除合成石油废水模型液中的苯酚。此外,响应面法(RSM)是优化EDBM的简便方法。采用中心复合设计(CCD)实验设计,研究了电流密度、进料流量、进料浓度对工艺完成时间(CT)和回收率(RE)的影响。通过岭型分析和典型分析,确定了最佳操作条件为进料浓度214.0 ppm、电流密度41.89、体积进料流量12.84。在此条件下,CT最小值为85.5 min, RE最大值为75.4%。此外,实验结果与预测结果一致,表明中心复合设计是模拟石油废水中苯酚再生的良好技术。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Characterization and optimization of electrodialysis with bipolar membranes with improved alkaline stability for phenol recovery from petroleum wastewater

Characterization and optimization of electrodialysis with bipolar membranes with improved alkaline stability for phenol recovery from petroleum wastewater
The purity and recovery of phenol from an aqueous solution by electrodialysis with a bipolar membrane (EDBM) system mainly depend on the solution pH, possibly effective only under alkaline conditions because phenol is a very weak acid with a pKa of 10. In this research, mono-sheet bipolar membranes with high chemical stability were successfully prepared using 1,4-diazabicyclo[2.2.2] octane (DABCO) as a quaternary ammonium group with bicyclic organic compounds. The BPMs characterization was studied using FTIR, FESEM, membrane chemical stability in alkaline solution, and electrical resistance. Comparing BPMs' performance synthesized by DABCO illustrated satisfactory results in the membrane's chemical stability and electrical resistance.
The mono-sheet composite bipolar membranes are used in electrodialysis with bipolar membrane (EDBM) to remove phenol from synthetic petroleum wastewater model solution. Moreover, Response Surface Methodology (RSM) was employed as a facile method for optimizing the EDBM. In particular, the effects of current density, feed flow rate, feed concentration on the completion time (CT), and recovery efficiency (RE) of the process were investigated using the Central Composite Design (CCD) experimental design. According to the ridge and canonical analysis, the optimum operating conditions were determined at the feed concentration of 214.0 ppm, current density of 41.89, and volumetric feed flow rate of 12.84. Under these conditions, the minimum CT and maximum RE were found at 85.5 min and 75.4 %, respectively. In addition, the experimental results agreed with the prediction, suggesting that central composite design was a good technique for modeling phenol regeneration from petroleum wastewater.
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来源期刊
Chemical Engineering Journal Advances
Chemical Engineering Journal Advances Engineering-Industrial and Manufacturing Engineering
CiteScore
8.30
自引率
0.00%
发文量
213
审稿时长
26 days
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