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Development of an electrodialysis-distillation integrated process for separation of hazardous sodium azide to recover valuable DMSO solvent from pharmaceutical effluent

机译:开发一种用于分离危险叠氮化钠以从制药废水中回收有价值的DMSO溶剂的电渗析-蒸馏集成工艺的开发

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Recovery of solvents from aqueous industrial effluents containing hazardous compounds is not directly feasible by conventional methods due to the complex nature of such wastewaters. An effluent from a pharmaceutical industry contains 2-3 wt% explosive sodium azide + corrosive ammonium chloride salts, 15-20% dimethylsulfoxide (DMSO) solvent and water. The focus of this work is to establish a hybrid process to facilitate removal of salts by electrodialysis (ED) followed by distillation to recover DMSO. An indigenously constructed ED system of 1.05 m2 membrane area was used to process 10 L batch size. Pure DMSO was recovered from desalted liquor by vacuum distillation in two stages to obtain DMSO concentration up to 60-70% in the first stage and subsequent recovery of pure DMSO in the second. Effect of operating parameters such as flow rate, limiting current density and voltage was evaluated. Distillation was carried out at 20-30 mmHg at reboiler temperature below 150 °C. Drug prepared using the recycled DMSO (>99.5%) was found to meet desired specifications. Detailed design of the ED-distillation process scheme to treat 7500 L/day of the effluent revealed that it was technically and economically feasible, since 30 Metric Tonnes of solvent has been recovered by the industry.
机译:由于这类废水的复杂性质,采用常规方法无法直接从含有危险化合物的工业废水中回收溶剂。制药行业的废水包含2-3 wt%的易爆叠氮化钠+腐蚀性氯化铵盐,15-20%的二甲基亚砜(DMSO)溶剂和水。这项工作的重点是建立一种混合工艺,以促进通过电渗析(ED)去除盐,然后蒸馏以回收DMSO。膜面积为1.05平方米的本地设计的ED系统用于处理10 L的批量。通过两步真空蒸馏从脱盐液中回收纯DMSO,以在第一步中获得高达60-70%的DMSO浓度,然后在第二步中进行纯DMSO的回收。评估了诸如流量,极限电流密度和电压等操作参数的影响。在低于150℃的再沸器温度下在20-30mmHg下进行蒸馏。发现使用回收的DMSO(> 99.5%)制备的药物符合所需规格。 ED蒸馏工艺方案的详细设计表明,该工艺每天可处理7500升废水,因为该行业已回收了30公吨的溶剂,因此在技术和经济上都是可行的。

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