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Environmental Impact Cost Analysis of Multi-Stage Flash, Multi-Effect Distillation, Mechanical Vapor Compression, and Reverse Osmosis Medium-Size Desalination Facilities

机译:多阶段闪光,多效蒸馏,机械蒸汽压缩和反渗透中等大小脱盐设施的环境影响成本分析

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摘要

In response to increasing global water demand, desalination has become an important source of water in many regions of the world. The objective of this research is to compare four different desalination methods operating at a production capacity between 100 and 200 m~3/d: 1) multi-stage flash (MSF), 2) multi-effect distillation (MED), 3) mechanical vapor compression (MVC), and 4) reverse osmosis (RO). Brine disposal and energy consumption for treatment are also discussed in the paper. The source water and brine disposal requirements for each method vary based on system efficiency. As a system's treatment efficiency increased, the source water requirement decreased and the salinity of the brine solution increased. RO was the least energy intensive treatment method, requiring 3-5.5 kWh/m~3. MED and MVC had similar energy requirements at 6.5-12 kWh/m~3. The least efficient treatment method was MSF, requiring 13.5-25.5 kWh/m~3. High salinity and large energy requirements can be mitigated by pairing the desalination facility with a waste water treatment plant. Effluent can be mixed with the brine to reduce salinity and thermal energy can be supplied to reduce energy demand.
机译:为了应对增加全球需水需求,海水淡化已成为世界许多地区的重要水源。本研究的目的是比较四种不同的海水淡化方法在100到200 m〜3 / d:1)多级闪光(MSF),2)多效蒸馏(MED),3)机械下运行蒸汽压缩(MVC)和4)反渗透(RO)。本文还讨论了盐水处理和用于治疗的能耗。每种方法的源水和盐水处理要求都根据系统效率而变化。随着系统的治疗效率增加,源水需求降低,盐水溶液的盐度增加。 RO是最少的能量密集的处理方法,需要3-5.5千瓦时/ m〜3。 MED和MVC在6.5-12 kWh / m〜3时具有相似的能量要求。最低有效的处理方法是MSF,需要13.5-25.5千瓦时/ m〜3。通过将海水淡化设施与废水处理厂配对,可以减轻高盐度和大的能量要求。流出物可以与盐水混合以降低盐度,可以提供热能以降低能量需求。

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