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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Analysis of a new design of a multi-stage flash-mechanical vapor compression desalination process
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Analysis of a new design of a multi-stage flash-mechanical vapor compression desalination process

机译:多级闪速机械蒸汽压缩脱盐工艺的新设计分析

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摘要

A new design for a multi-stage flash-mechanical vapor compression(MSF-MVC)desalination process was investigated.The analysis of the proposed MSF-MVC system was performed based on the energy,exergy and thermoeconomic methodologies.The considered system was investigated under different operating conditions using a developed Design and Simulation(VDS)software.To examine the performance of the proposed process,a comparison with the conventional MSF desalination process was performed.Thermoeconomic results show that the best operating suction pressure for the compressor is 8 kPa and the best top brine temperature is 110°C.The effect of the stages number of the heat recovery section was studied,and the results show that the low unit product cost was obtained at 20 stages.The effect of the temperature difference across the vent chamber was measured,and the results show that the lower unit product cost was 6 °C.Thermoeconomic analysis shows that the last stage(vent chamber)had the highest value of the sum of capital and operation and maintenance costs in addition to the exergy destruction cost.Also,the last stage had a higher relative cost difference and lower exergetic efficiency.This in turn shows that a reduction in the exergy destruction within the vent chamber reduced the unit product cost.The performance ratio of the proposed MSF-MVC system was 2.4 times the performance ratio of the conventional MSF process.The heat transfer area of the MSF-MVC system was 57% higher than that of conventional MSF.The exergetic efficiency of the MSF-MVC system was 67% higher than that of MSF.The thermoeconomic results show that the unit product cost of MSF-MVC,under the specified conditions,was calculated by 2.0 US/m3;this value is 25% less than that of the conventional MSF process.
机译:研究了一种多级闪速机械蒸汽压缩(MSF-MVC)脱盐工艺的新设计。基于能量,火用和热经济方法对所提出的MSF-MVC系统进行了分析,并在考虑了以下因素的情况下对所考虑的系统进行了研究。使用开发的设计和仿真(VDS)软件在不同的运行条件下进行。为检验所提出的过程的性能,与传统的MSF脱盐过程进行了比较。热经济学结果表明,压缩机的最佳运行吸入压力为8 kPa,最佳最高盐水温度为110°C。研究了热回收段的段数影响,结果表明在20个段中获得了较低的单位产品成本。经测量,结果表明较低的单位产品成本为6°C。热经济分析表明,最后一个阶段(通风室)的价值最高除火用破坏成本外,还包括资金,运营和维护成本之和。此外,最后阶段的相对成本差异更大,火用效率更低。这又表明,排气室内的火用破坏减少了降低了单位产品成本。拟议的MSF-MVC系统的性能比是传统MSF工艺的2.4倍; MSF-MVC系统的传热面积比常规MSF高57%。 MSF-MVC系统的效率比MSF高67%。热经济学结果表明,在指定条件下,MSF-MVC的单位产品成本按2.0 US / m3计算;此值比MSF-MVC小25%。常规MSF工艺的性能。

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