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Recovery of nitric and acetic acids from etching waste solutions using a synergistic system consisting of N235 and TRPO in cyclohexane

机译:使用由环己烷的N235和TRPO组成的协同系统,从蚀刻废液中恢复硝酸和乙酸

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摘要

To purify and recover phosphoric acid (H3PO4) from laboratory synthetic etching waste, Alamine 336 (N235) and trialkyl phosphine oxide (TRPO) were used in a mixed extractant to extract nitric (HNO3) and acetic acids (HAc). The effects of the extraction temperature, extractant concentration, and ratio of the organic phase to the liquid phase on the separation process were investigated. Using an organic system containing 3.5% (v/v) N235, 46.5% (v/v) TRPO, and 50% (v/v) cyclohexane, 70% of the HAc and 85% of the HNO3 were extracted, with 8.5% H3PO4 co-extracted through single-stage contact. Furthermore, more than 99% HAc and 99.5% HNO3 were removed after three counter-current extractions, with only similar to 15% of the H3PO4 being co-extracted. A stripping rate of more than 99% was achieved for HNO3, HAc, and H3PO4 using 0.25 mol.L-1 NH3 center dot H2O. UV-vis and FT-IR analyses indicated that the N235 and TRPO mixture had a synergistic effect on HNO3 and HAc extraction. The mechanisms of HNO3 and HAc extraction involve ion-pair association and hydrogen bonding, respectively.
机译:从实验室合成蚀刻废物中纯化和回收磷酸(H3PO4),在混合萃取剂中使用阿拉胺336(N235)和三烷基膦(TRPO)以提取硝酸(HNO3)和乙酸(HAC)。研究了提取温度,萃取剂浓度和有机相与分离过程中液相的影响。使用含有3.5%(v / v)N235,46.5%(v / v)TRPO和50%(v / v)环己烷的有机系统,提取70%HAC和85%的HNO3,8.5% H3PO4通过单级接触共提取。此外,在三次反电流萃取后除去超过99%的HAC和99.5%HNO 3,仅相似于15%的H3PO4共同提取。使用0.25mol.L-1 NH3中央点H2O,对HNO3,HAC和H3PO4实现了超过99%的汽提率超过99%。 UV-Vis和FT-IR分析表明N235和TRPO混合物对HNO3和HAC萃取具有协同作用。 HNO3和HAC萃取的机制分别涉及离子对缔合和氢键。

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