Theoretical and Experimental Study on the Falling-Film Evaporator Applied to Mechanical Vapor Compression

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Abstract:

Based on a heat pump system of mechanical vapor recompression (MVR) designed and manufactured independently, the heat transfer performance of falling-film evaporator was measured by a combination way of theory analysis and experiment proving as the heat pump operated in practice. After the result of theoretical calculation is worked out, the start thickness and entrance velocity of the liquid film are established by adjusting the flux of raw solution. The result shows there is an optimization that the film thickness at the bottom of the tubes amounts to that of boundary layer of velocity. Additionally, it is a process of falling-film flow with heat and mass transfer between the start and end of falling-film. The last thickness of the falling film is about 0.21~0.44mm. The thickness of falling film when the falling-film flowed and heat exchange was over is compared with each other, and the effect of heat resistance on heat transfer is discussed also. It is showed that an optimal thickness is formed during the process of falling-film flow and evaporation, and disadvantages come up when it is not formed. The falling-film evaporator propelled by the MVR heat pump with low compression ratio carries through a process of strong and high-efficiency heat transfer with phase transition. It is because the states of produced vapor both before compressed and after compressed are saturated. Its heat-transfer coefficient may be as high as 1990 W/ (m2·K). The start and end thickness of falling film become great while the evaporation pressure goes up. It leads to the drop of the heat-transfer efficiency, so there is an optimization to the system in all probability.

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Periodical:

Advanced Materials Research (Volumes 753-755)

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2667-2673

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August 2013

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] Zhu Yufeng, Wang Wei, Cui Haiting. Design of liquid distributors in large falling-film evaporator [J]. Food and Machinery, 2007, 23(1), 104-106.

Google Scholar

[2] Du Qizhong. Film forming reason and handling measures of influence on falling-film evaporator [J]. Report on Aluminum and Magnesium, 2009. 4, 9-10.

Google Scholar

[3] Zhu Lujia, Hao Yunlong, The application study of flash-triple effects falling film evaporator on xylose production [J]. China Food Additive. 2010, 56-59.

Google Scholar

[4] Zhang Liqiang, Yang Chunguang, Xu Lie, Cai Jiang, Zhao Jingli. Experimental study on heat transfer performance of the umbrella-plate falling-film evaporator [J]. Chemical Engineering, 2006, 34(6), 17-20.

Google Scholar

[5] Song Jitian, Liu Wenwu. Perfomance study on the enhanced heat-transfer of the dimple-vertical plate falling-film evaporator [J]. Chemical Engineering, 2010, 37(3), 270-272.

Google Scholar

[6] G. Karimi, M. Kawaji. An experimental study of freely falling films in a vertical tube [J]. Chemical Engineering Science, 1998, 20: 3501-3512.

DOI: 10.1016/s0009-2509(98)00159-6

Google Scholar

[7] J.A. Winchester, C. Marsh. Dynamics and control of falling film evaporators with mechanical vapor recompression [J]. Trans IChemE, 1999, 77: 357-371.

DOI: 10.1205/026387699526340

Google Scholar

[8] Yang Shiming, Tao Wenquan. Heat Transfer(M). Beijing: High Education Press, 1998: 27.

Google Scholar

[9] H. Chen, R.S. Jebson. Factors affecting heat transfer in falling film evaporators [J]. Trans IChemE, 1997, 75: 111-115.

DOI: 10.1205/096030897531423

Google Scholar