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氨水溶液降膜蒸发实验 被引量:2

Experiment of ammonia water falling film evaporation
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摘要 发生器和吸收器的传热性能是影响制冷机组和双工质发电机组做功效率的关键因素,为了提高中低温地热(余热)在热泵机组和地热双工质发电系统中的利用效率,本文选用50%和60%的氨水溶液作为循环工质,对约6 m长的竖管降膜蒸发器的传热特性进行实验研究,分别讨论喷淋密度和热水温度对垂直降膜蒸发器的传热系数、氨蒸气量和蒸发压力的影响。结果表明,降膜蒸发器的传热系数和氨蒸气量随喷淋密度的增加先增大后减小,传热系数和蒸发压力随着热源温度的增大而增加;50%和60%的氨水溶液喷淋密度最佳值分别在0.2200~0.2500 kg/(m.s)和0.2600~0.2900 kg/(m.s);传热系数和热源温度呈线性关系。氨水溶液的实验传热系数明显高于现有文献中水的实验传热系数,通过两种不同浓度的溶液对比发现,60%的氨水溶液传热性能明显优于50%的氨水溶液。 An experimental investigation of vertical out-tube falling film heat transfer with different inlet spray densities of ammonia water mixture and inlet hot water temperatures was conducted.The falling film evaporator had a total height of 6000mm and the cycling working fluids were high concentration 60% and 50% ammonia water.We mainly studied the influence of spray density and inlet temperature of hot water on heat transfer coefficient,ammonia vapor amount and evaporation pressure.The experiment showed that heat transfer coefficient and ammonia vapor amount increased first and then decreased with increasing inlet spray density.The higher the hot water temperature,the higher the evaporation pressure.Heat transfer coefficient increased lineany with increasing hot water temperature.The experimental heat transfer coefficient of ammonia water solution was significantly higher than that of water reported in literature.For 50% water,optimum spray density was between 0.2200 and 0.2500 kg/(m·s);for 60% ammonia water,optimum spray density was between 0.2600 and 0.2900 kg/(m·s).In this experiment,heat transfer performance of 60% ammonia water was better than 50% ammonia water.
出处 《化工进展》 EI CAS CSCD 北大核心 2011年第9期1889-1893,共5页 Chemical Industry and Engineering Progress
基金 国家高技术研究发展计划(国家863计划 2009AA05Z433) 中国科学院可再生能源与天然气水合物重点实验室基金项目(y107j2)
关键词 氨水溶液 降膜 蒸发 传热性能 中低温地热 余热利用 ammonia water falling film evaporation heat transfer performance mid-low temperature geothermal water waste heat utilization
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  • 1李红梅.管式、扳式降膜蒸发器综合性能比较[C].第卜届全国氧化铝学术会议论文集,2009:280-284.
  • 2Tanf Ali Aciib, Bertrand Heyd, Jean Vasseur. Experimental results and modeling of boiling heat transfer coefficients in falling film evaporator usable for evaporator design[J]. Chemical Engineering and processing: Process Intensification, 2009, 48: 961-968.
  • 3Feddaoui M, Meftah H, Mir A. The numerical computation of the evaporative cooling of falling water film in turbulent mixed convection inside a vertical tube[J]. International Communications in Heat and Mass Transfer, 2006, 33: 917-927.
  • 4Yang Luopeng, Chen Xue, Shen Shengqiang. Heat-transfer characteristics of climbing film evaporation in a vertical tube[J]. Experimental Thermal and Fluid Science, 2010, 34(6): 753-759.
  • 5Felix Weise, Stephan Scholl. Evaporation of pure liquids with increased viscosity in a falling film evaporator[J]. Heat Mass Transfer, 2009, 45: 1037-1046.
  • 6Li Yang, Wen Wang. The heat transfer performance of horizontal tube bundles in large falling film evaporators[J]. International Journal of Refrigeration, 2011, 34: 303-316.
  • 7刘殿宇.多效降膜式蒸发器中各效蒸发面积的调整[J].医药工程设计,2008,29(3):5-6. 被引量:9
  • 8翟玉燕,黄兴华.基于分布参数模型的水平管式降膜蒸发器模拟[J].机械工程学报,2009,45(7):284-290. 被引量:10
  • 9白健美,马虎根,李长生,罗忠.水平管束低压降膜蒸发换热特性研究[J].流体机械,2010,38(2):53-56. 被引量:6
  • 10刘红,马虎根,邹静,罗忠.水平管排低压降膜蒸发传热特性实验研究[J].制冷与空调(四川),2010,24(4):6-9. 被引量:1

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