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Treatment of Sebacic Acid Industrial Wastewater by Extraction Process Using Castor Oil Acid as Extractant*

机译:以蓖麻油酸为萃取剂萃取工艺处理癸二酸工业废水*

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摘要

Wastewater containing high concentrations of phenol and sodium sulfate is generated in sebacic acid (SA) industry. Castor oil acid, a raw material for producing SA, can be used to extract phenol from wastewater in order to reduce the amount of phenol used in the process and discharge of phenol. The results show that the extrac-tion mechanism is that hydroxyl group of phenol is linked to carboxyl group of castor oil acid by hydrogen bond. The extraction process approaches equilibrium in 30 min. Extraction ratio increases with the increase of sodium sulfate and castor oil acid, and decreases as phenol increases. When the oil-water ratio is 1︰3, the optimal distribu-tion coefficient of 40 is obtained. Phenol saturation concentration in castor oil acid is 1.03 mol·L−1 after extraction for 4 times. The equilibrium constant (Kex) at 25 °C is 8.41 and the endothermic enthalpy (ΔH) is 1.513 kJ·mol−1. The Gibbs free energy (ΔG) is−5.277 kJ·mol−1 and the value ofΔS is calculated to be 22.3 J·mol−1·K−1.
机译:癸二酸(SA)工业中会产生含有高浓度苯酚和硫酸钠的废水。蓖麻油酸是生产SA的原料,可用于从废水中提取苯酚,以减少过程中和苯酚排放中所用的苯酚量。结果表明,其萃取机理是苯酚的羟基通过氢键与蓖麻油酸的羧基相连。提取过程在30分钟内达到平衡。萃取率随硫酸钠和蓖麻油酸的增加而增加,随苯酚的增加而降低。当油水比为1∶3时,最佳分配系数为40。提取4次后,蓖麻油酸中的苯酚饱和浓度为1.03mol·L-1。 25°C时的平衡常数(Kex)为8.41,吸热焓(ΔH)为1.513 kJ·mol-1。吉布斯自由能(ΔG)为-5.277 kJ·mol-1,ΔS的值经计算为22.3 J·mol-1·K-1。

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