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首页> 外文期刊>Research Journal of Chemical Sciences >Extraction of Phenol from Industrial Water Using Different Solvents
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Extraction of Phenol from Industrial Water Using Different Solvents

机译:使用不同溶剂从工业用水中提取苯酚

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The analysis and efficiency of phenol extraction from the industrial water using different solvents, were investigated. To our knowledge, the experimental information available in the literature for liquid-liquid equilibria of ternary mixtures containing the pair phenol-water is limited. Therefore the purpose of the present investigation is to generate the data for the water-phenol with different solvents to aid the correlation of liquid-liquid equilibria, including phase diagrams, distribution coefficients of phenol, tie-lines data and selectivity of the solvents for the aqueous phenol system. The ternary equilibrium diagrams and tie-lines data for systems containing Water-Phenol-Benzene, Water-Phenol-Chloroform, Water-Phenol-iso-Butyl Acetate, Water-Phenol-Butanol, Water-Phenol-Ethyl Methyl Keton and Water-Phenol-Toluene, were determined at 303 K and atmospheric pressure. The capacity and selectivity of these organic solvents in each of these systems were determined from the tie-lines data. The capacity of the isobutyle acetate was found to be the highest among the other solvents, and its selectivity was also the highest. Similar results also were obtained for the ethyl methyl keton but gave less capacity and selectivity as compared to the isobutyle acetate. It can be concluded that both isobutyle acetate and ethyl methyl keton are good solvents for extraction of phenol from industrial water. The liquid-liquid equilibrium data of ternary systems were correlated to the NRTL, UNIQUAC and UNIFAC models of activity coefficient to determine their adjustable parameters. The standard deviations from experimental compositions were calculated. Results show that the correlation may be greatly improved by applying the NRTL model with the regression criteria based on minimizing the experimental and calculating distribution coefficients S_(k) to give an average value of the root mean square deviation about 1.436 % and in terms of the average errors in the distribution ratio for all tie-lines about 10.776%.
机译:研究了使用不同溶剂从工业用水中提取苯酚的分析和效率。据我们所知,在文献中可获得的关于含苯酚-水对的三元混合物的液-液平衡的实验信息是有限的。因此,本研究的目的是生成具有不同溶剂的水酚的数据,以帮助进行液-液平衡的相关性,包括相图,苯酚的分布系数,联系线数据和溶剂对溶剂的选择性。苯酚水溶液。包含水-苯-苯,水-苯酚-氯仿,水-苯酚-异丁酸酯,水-苯酚-丁醇,水-苯酚-乙基甲基酮和水-苯酚的系统的三元平衡图和联系线数据在303 K和大气压下测定甲苯。这些有机溶剂在每个系统中的容量和选择性均由联系数据确定。发现乙酸异丁酯的容量在其他溶剂中最高,并且其选择性也是最高的。对于乙基甲基酮也获得了相似的结果,但是与乙酸异丁酯相比,给出的容量和选择性较小。可以得出结论,乙酸异丁酯和乙基甲基酮都是从工业用水中提取苯酚的良好溶剂。将三元体系的液-液平衡数据与活度系数的NRTL,UNIQUAC和UNIFAC模型相关联,以确定其可调参数。计算与实验组成的标准偏差。结果表明,通过最小化实验和计算分布系数S_(k)以给出均方根偏差的平均值约为1.436%并根据回归系数应用NRTL模型和回归标准可以极大地改善相关性。所有联络线的分配比率的平均误差约为10.776%。

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