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Hydrophobic Pervaporation for Environmental Applications: Process Optimization and Integration

机译:用于环境的疏水渗透蒸发:工艺优化和集成

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The focus of this paper is on the design of pervaporation units for wastewater treatment taking into account technical, economic, and environmental aspects. Two different sized industrial wastewater streams of water-chloroform, and of water-methyl-isobutylketone (MIBK) are considered. Based on a wastewater stream of 1,500 kg/d, a semi-batch process combining pervaporation with a decanter recycle loop is developed. Using this process, it is possible to recover over 99% of the organic components at concentrations of more than 98 wt. %. The treatment costs are between 0.11 to 0.16 $/kg wastewater. For the treatment of a wastewater stream of 1,000 kg/h, pervaporation combined with a decanter and recycling loop, as well as integrated in a hybrid process with adsorption, is considered. For MIBK, pervaporation with a decanter is the most attractive option taking economic and environmental aspects into account, while, for chloroform, the hybrid process is the better option. Treatment costs in all cases are about 0.03 $/kg wastewater. The recovery rate of the organic compounds is over 99% at concentrations over 98 wt. %. The authors concluded that pervaporation as a stand-alone unit, or integrated into hybrid processes, offers significant advantages over conventional alternatives.
机译:本文的重点是考虑到技术,经济和环境方面的问题,设计用于废水处理的渗透蒸发装置。考虑了水-氯仿和水-甲基-异丁酮(MIBK)的两种不同大小的工业废水流。基于1,500 kg / d的废水流,开发了将全蒸发与process析器循环回路相结合的半分批工艺。使用此方法,有可能以超过98 wt。%的浓度回收超过99%的有机成分。 %。处理成本为每公斤废水0.11至0.16美元。为了处理1,000 kg / h的废水流,需要考虑将全蒸发与倾析器和循环回路相结合,以及与吸附混合的过程中。对于MIBK,考虑到经济和环境方面的考虑,用倾析器进行全蒸发是最有吸引力的选择,而对于氯仿,混合工艺是更好的选择。在所有情况下,处理成本约为0.03 $ / kg废水。当浓度超过98wt。%时,有机化合物的回收率超过99%。 %。作者得出的结论是,与传统替代品相比,全蒸发作为独立单元或集成到混合工艺中具有明显优势。

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