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基于嵌套结构的多级负压太阳能蒸馏装置实验研究 被引量:1

Experimental study on a nested multi-effect solar still operating under vacuum
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摘要 文章针对常压运行单级太阳能蒸馏器产水效率较低的问题,提出了嵌套管回热和负压运行的改进方案。改进装置由多层圆管嵌套而成,其内部具有多个独立拱形产水腔室,在负压下运行时具有能耗低、操作维护简便、产水性能好且水质高等特点。分别于成都和西昌两地测试了装置处于95(常压),60,40,20 kPa运行压力时的产水性能,结果表明装置在西昌维持40 kPa运行时具有最优产水性能,对应单日产水量为7.2 kg/m2,性能系数为1.45,较常压运行时性能提升近一倍。此后对装置维持负压的能耗数据及产水经济性进行了评估,数据表明装置产水时维持负压能耗低于4 kJ/kg,综合产水成本约为0.1元/L,与同类太阳能蒸馏器相比具有一定优势。 Single-effect solar still operating under atmospheric pressure commonly suffers from its low yielding efficiency,therefore a modification strategy with nested heat recovery and vacuum operation was proposed.The modified still is composed of multiple nested circular tubes,whereby several independent distillation cavities with arch feature were formed.The still was characterized by low energy consumption,convenient operational maintenance and high freshwater quality.Two group of experiments for yielding performance were then conducted in Chengdu and Xichang,including operation pressures of atmospheric,60,40 and 20 kPa.The results showed that the still obtained the highest performance at 40 kPa in Xichang,corresponding to the highest daily yield of 7.2 kg/m~2 and performance ratio(PR)of 1.45 which is nearly double of PR at atmospheric test.The subsequent work concerned an economic analysis on yielding cost and energy consumption for maintaining vacuum.The results indicated that the energy consumption can be lower than 4 kJ/kg and yielding cost is approximately 0.1 yuan/L,showing certain advantages compared with other similar solar stills.
作者 谢果 魏新宇 孙泽荣 刘莹璋 Xie Guo;Wei Xinyu;Sun Zerong;Liu Yingzhang(State Key Laboratory of Hydraulics and Mountain River Engineering,Sichuan University,Chengdu 610065,China)
出处 《可再生能源》 CAS CSCD 北大核心 2023年第11期1446-1453,共8页 Renewable Energy Resources
基金 国家自然科学基金项目(51606130)。
关键词 太阳能 蒸馏 负压 多级 solar energy distillation vacuum multi-effect
作者简介 谢果(1984-),男,博士,副教授,研究方向为传热传质与太阳能利用技术。E-mail:2008xieguo@scu.edu.cn。
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  • 1He K, Hwang H J, Woo M W, Moon I S. Production of drinking water from saline water by direct contact membrane distillation (DCMD) [J] Journal of Industrial and Engineering Chemistry, 2011, 17 (1): 41-48.
  • 2Chouikh R, Bouguecha S, Dhahbi M. Modelling of a modified air gap distillation membrane for the desalination of seawater [J]. Desalination, 2005, 181:257-265.
  • 3Khayet M, Cojocaru C, Garcla-Payo C. Application of response surface methodology and experimental design in direct contact membrane distillation [J]. Ind. Eng. Chem. Res., 2007, 46 (17): 5673-5685.
  • 4Boubakri A, Hafiane A, Bougnecha S A T. Application of response surface methodology for modeling and optimization of membrane distillation desalination process [J]. Journal of Industrial and Engineering Chemistry, 2014, 20:3163-3169.
  • 5Cojoearu C, Khayet M. Sweeping gas membrane distillation of sucrose aqueous solutions: response surface modeling and optimization [J]. Separation and Puri.fication Technology, 2011, 81:12-24.
  • 6Khayet M, Cojocaru C. Artificial neural network model for desalination by sweeping gas membrane distillation [J]. Desalination, 2013, 308:102-110.
  • 7Onsekizoglu P, Bahceci K S, Acar J. The use of factorial design for modeling membrane distillation [J]. Journal of Membrane Science, 2010, 349:225-230.
  • 8Chang H, Liau J S, Ho C D, Wang W H. Simulation of membrane distillation modules for desalination by developing user's model on Aspen Plus platform [J]. Desalination, 2009, 249:380-387.
  • 9Khayet M, Cojocaru C. Artificial neural network modeling and optimization of desalination by air gap membrane distillation [J]. Separation and Purification Technology, 2012, 86:171-182.
  • 10Khayet M, Cojocaru C. Air gap membrane distillation: desalination, modeling and optimization [J]. Desalination, 2012, 287:138-145.

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