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New Method For Acrylic Acid Recovery From Industrial Waste Water Via Esterification With 2-Ethyl Hexanol

机译:2-乙基己醇酯化从工业废水中回收丙烯酸的新方法

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摘要

Acrylic acid (AA) is an important component for the production of acrylate polymer. In a typical acrylic manufacturing unit, waste water contains AA in a range of 4–15wt.% contributes to the high values of chemical oxygen demand. Due to the toxicity of AA to the aquatic organism, this wastewater should be treated before it is discharged to the environment. The waste water could be evaporated before sending to the incineration which was neither economic feasible nor environmental friendly. Esterification of wastewater containing carboxylic acid with alcohol could be a promising method to recover the acid by converting it to ester while purifying the wastewater. In the present study, recovery of AA via esterification with 2-ethyl hexanol (2EH) was investigated. The model industrial wastewater with various concentration of AA (10–100% w/w) was reacted with 2EH to produce 2-ethyl hexyl acrylate (2EHA) in the setups with total reflux and continuouslywater removal. These Amberlyst-15 (ion exchange resin) catalyzed reactions were carried out under the mass transfer resistance free region. The performance of both systems was compared. The yield for the reactions of the AA solutions with the AA concentrations of 30–80% was enhanced significantly when the reactions were carried out using the second setup. The kinetic data of the esterification of dilute AA was well described by the Eley–Rideal (ER) kinetic model incorporated with a correction factor to consider the catalyst fouling effect and pseudo-homogeneous (PH) kineticmodel for the AA polymerization. The findings have shown the potential of recovering AA from the waste water stream via esterification. The concentrated AA solutions or larger amount of inhibitor should be adopted to prevent the catalyst fouling by the deposition of poly-acrylic acid on the catalyst surface.
机译:丙烯酸(AA)是生产丙烯酸酯聚合物的重要组分。在典型的丙烯酸生产单元中,废水中AA含量在4-15wt。%的范围内,导致化学需氧量较高。由于AA对水生生物的毒性,应在将废水排入环境之前对其进行处理。废水在送往焚化炉之前可以蒸发掉,这既不经济,也不环保。用醇对含羧酸的废水进行评价可能是一种有前途的方法,可以在净化废水的同时将其转化为酯来回收酸。在本研究中,研究了通过与2-乙基己醇(2EH)酯化反应回收AA的方法。在总回流和连续除水的装置中,将具有不同浓度的AA(10-100%w / w)的模型工业废水与2EH反应生成丙烯酸2-乙基己酯(2EHA)。这些Amberlyst-15(离子交换树脂)催化的反应在无传质阻力的区域下进行。比较了两个系统的性能。当使用第二种设置进行反应时,AA浓度为30-80%的AA溶液的反应收率显着提高。稀释AA的酯化反应的动力学数据可以通过Eley-Rideal(ER)动力学模型很好地描述,并结合校正因子来考虑AA聚合反应的催化剂结垢效应和拟均相(PH)动力学模型。结果表明,通过酯化可以从废水中回收AA。为了防止由于聚丙烯酸在催化剂表面上沉积而造成的催化剂结垢,应采用浓AA溶液或更大量的抑制剂。

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