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Multi-Effect Evaporation Coupled with MVR Heat Pump Thermal Integration Distillation for Separating Salt Containing Methanol Wastewater

机译:用于分离含甲醇废水的MVR热泵热整合蒸馏联耦合多效蒸发

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Due to the high energy consumption for separation of salt containing methanol wastewater, in this work, the multi-effect evaporation coupled with mechanical vapor recompression (MVR) heat pump and thermal integration technologies were raised for the first time. The ELECNRTL thermodynamic model is used to simulate and optimize the evaporation rectification process. Energy consumption and total annual cost (TAC) are taken as objective functions. The results show that multi-effect evaporation coupled with conventional distillation process can save energy consumption and TAC by 44.12% and 39.14%. The multi-effect evaporation coupled with distillation process based on MVR heat pump technology can save energy consumption and TAC by 55.27% and 47.49%, which is super to three-effect evaporation coupled with conventional distillation process. The three-effect evaporation coupled with MVR heat integration process can save energy consumption and TAC by 81.32% and 58.55%, which is more economical than other processes. It can be clearly seen that three-effect evaporation coupled with MVR heat integration process is more competitive to deal with the salt containing methanol wastewater.
机译:由于含甲醇废水的盐分离的高能耗,在这项工作中,首次提高了与机械蒸汽再压缩(MVR)热泵和热集成技术相连的多效蒸发。 ELECNRTL热力学模型用于模拟和优化蒸发整流过程。能源消耗和总年度成本(TAC)被视为客观职能。结果表明,与常规蒸馏工艺相结合的多效蒸发可以节省能耗和TAC的44.12%和39.14%。基于MVR热泵技术的蒸馏过程结合的多效蒸发可以节省能源消耗和TAC 55.27%和47.49%,这是与常规蒸馏过程相连的超级三效蒸发。三效蒸发与MVR热集成过程相结合,可以节省能耗和TAC 81.32%和58.55%,比其他过程更经济。可以清楚地看出,三效蒸发与MVR热整合过程相结合,更具竞争力地处理含甲醇废水的盐。

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