入口空气参数分布对薄膜式全热交换器性能影响的数值研究

沈志杰, 闵敬春, 段江菲

清华大学学报(自然科学版) ›› 2020, Vol. 60 ›› Issue (11) : 958-966.

PDF(13636 KB)
PDF(13636 KB)
清华大学学报(自然科学版) ›› 2020, Vol. 60 ›› Issue (11) : 958-966. DOI: 10.16511/j.cnki.qhdxxb.2020.22.010
航空航天与工程力学

入口空气参数分布对薄膜式全热交换器性能影响的数值研究

  • 沈志杰1, 闵敬春1, 段江菲2
作者信息 +

Numerical study on influence of supply inlet air parameter distribution on a membrane-type total heat exchanger

  • SHEN Zhijie1, MIN Jingchun1, DUAN Jiangfei2
Author information +
文章历史 +

摘要

薄膜式全热交换器是一种可同时回收热量和湿份的空气-空气热回收装置,其换热芯由具有良好透湿性的膜材料制成,通常用来减少建筑能耗并改善室内空气品质。由于全热交换器内部通道分布不均或外部干扰,全热交换器入口空气可能存在分布不均的情况。该文采用数值计算研究了薄膜式全热交换器入口空气参数分布对全热交换器传热传质特性的影响,包括入口空气温度、含湿量和速度分别呈线性和抛物线分布的情况。建立了全热交换器传热传质模型,通过数值计算得到了不同入口条件下全热交换器的显热效率、潜热效率和全热效率以及全热交换器薄膜两侧的温、湿差分布云图。结果表明:入口空气参数的线性分布对全热交换器效率影响较为明显,而抛物线分布对效率影响很小,但二者对薄膜两侧的温、湿差分布均有影响;传热传质相互影响并存在耦合,但传热对传质的作用很弱;入口空气温度和含湿量分布越不均匀,越容易出现反向传热传质现象,从而恶化传热传质。

Abstract

Membrane-type total heat exchangers (THX) are air-to-air heat exchangers with a core made of a water vapor permeable membrane that transfers both heat and moisture. These heat exchangers are often used to reduce building energy consumption and improve indoor air quality. However, non-uniform internal channel structures and external disturbances can lead to maldistributions of the supply inlet air parameters into the heat exchanger. This research numerically examines the effects of various supply inlet air parameter variations on the heat and moisture transfer characteristics, including linear and parabolic distributions of the inlet air temperature, moisture ratio and velocity. The model then simulates the heat and mass transfer in the heat exchanger to predict the temperature, moisture and enthalpy effectiveness distributions as well as the temperature difference and humidity ratio difference contours between the two sides of the membrane for the various inlet conditions. The results show that the linear distribution significantly affects the effectiveness while the parabolic distribution has little effect, with both affecting the temperature difference and humidity ratio difference contours between the two sides of the membrane. The heat transfer and the mass transfer affect each other, with the heat transfer having only a weak effect on the mass transfer. More nonuniform supply inlet air temperature and moisture ratio distributions increase the probability that the heat and mass transfer will be in opposite directions, which reduces both the heat and mass transfer.

关键词

入口空气参数 / 线性分布 / 抛物线分布 / 传热传质 / 效能

Key words

supply inlet air parameter / linear distribution / parabolic distribution / heat and mass transfer / effectiveness

引用本文

导出引用
沈志杰, 闵敬春, 段江菲. 入口空气参数分布对薄膜式全热交换器性能影响的数值研究[J]. 清华大学学报(自然科学版). 2020, 60(11): 958-966 https://doi.org/10.16511/j.cnki.qhdxxb.2020.22.010
SHEN Zhijie, MIN Jingchun, DUAN Jiangfei. Numerical study on influence of supply inlet air parameter distribution on a membrane-type total heat exchanger[J]. Journal of Tsinghua University(Science and Technology). 2020, 60(11): 958-966 https://doi.org/10.16511/j.cnki.qhdxxb.2020.22.010

参考文献

[1] ZURAIMI M S, THAM K W. Effects of child care center ventilation strategies on volatile organic compounds of indoor and outdoor origins[J]. Environmental Science & Technology, 2008, 42(6):2054-2059.
[2] XUE L X, LIU B X, CHEN J, et al. Structure and properties of total-heat exchange membranes for energy saving heat exchange ventilation processes[J]. Sustainable Development of Urban Environment and Building Material, 2012, 374-377:568-571.
[3] YE W, GAO J, ZHANG X, et al. Studies of relationship between ventilation, pollution exposure and environmental health of buildings[J]. Indoor and Built Environment, 2017, 26(2):147-151.
[4] HU T, MIN J C, SONG Y Z. Analysis of the effects of mass transfer on heat transfer in the process of moisture exchange across a membrane[J]. Chinese Science Bulletin, 2010, 55(12):1221-1225.
[5] HU T, MIN J C, SONG Y Z. Analysis of the effects of the heat of sorption on the process of heat transfer in moisture exchange across a membrane[J]. Science in China Series E:Technological Sciences, 2008, 51(12):2120-2127.
[6] ZHANG L Z, NIU J L. Effectiveness correlations for heat and moisture transfer processes in an enthalpy exchanger with membrane cores[J]. Journal of Heat Transfer, 2002, 124(5):922-929.
[7] ZHANG L Z, JIANG Y. Heat and mass transfer in a membrane-based energy recovery ventilator[J]. Journal of Membrane Science, 1999, 163(1):29-38.
[8] NIU J L, ZHANG L Z. Membrane-based enthalpy exchanger:Material considerations and clarification of moisture resistance[J]. Journal of Membrane Science, 2001, 189(2):179-191.
[9] MIN J C, SU M. Performance analysis of a membrane-based energy recovery ventilator:Effects of outdoor air state[J]. Applied Thermal Engineering, 2011, 31(17-18):4036-4043.
[10] MIN J C, SU M. Performance analysis of a membrane-based enthalpy exchanger:Effects of the membrane properties on the exchanger performance[J]. Journal of Membrane Science, 2010, 348(1-2):376-382.
[11] MIN J C, SU M. Performance analysis of a membrane-based energy recovery ventilator:Effects of membrane spacing and thickness on the ventilator performance[J]. Applied Thermal Engineering, 2010, 30(8-9):991-997.
[12] MIN J C, DUAN J F. Comparison of various methods for evaluating the membrane-type total heat exchanger performance[J]. International Journal of Heat and Mass Transfer, 2016, 100:758-766.
[13] MIN J C, DUAN J F. Membrane-type total heat exchanger performance with heat and moisture transferring in different directions across membranes[J]. Applied Thermal Engineering, 2015, 91:1040-1047.
[14] GUO J F, HUAI X L, CHENG K Y, et al. The effects of nonuniform inlet fluid conditions on crossflow heat exchanger[J]. International Journal of Heat and Mass Transfer, 2018, 120:807-817.
[15] WANG L N, MIN J C. Thermodynamic analysis of adsorption process at a non-equilibrium steady state[J]. Chinese Science Bulletin, 2010, 55(31):3619-3625.
[16] ZHENG W, WOREK W M. Numerical simulation of combined heat and mass transfer processes in a rotary dehumidifier[J]. Numerical Heat Transfer, Part A:Applications, 1993, 23(2):211-232.
[17] INCROPERA F P, DEWITT D P. Fundamentals of heat and mass transfer[M]. New York, USA:Wiley, 1985.
[18] SHAH R K, LONDON A L, WHITE F M. Laminar flow forced convection in ducts[J]. Journal of Fluids Engineering, 1980, 102(2):256-257.
[19] KUEHN T H, RAMSEY J W, THRELKELD J L. Thermal environmental engineering[M]. 3rd ed. Upper Saddle River, USA:Prentice Hall, 1998.
[20] SIMONSON C J, BESANT R W. Energy wheel effectiveness, Part I:Development of dimensionless groups[J]. International Journal of Heat and Mass Transfer, 1999, 42(12):2161-2170.
[21] SIMONSON C J, BESANT R W. Energy wheel effectiveness, Part Ⅱ:Correlations[J]. International Journal of Heat and Mass Transfer, 1999, 42(12):2171-2185.
[22] STRUCHTRUP H. Psychrometrics[M]//STRUCHTRUP H.Thermodynamics and energy conversion. Berlin, Germany:Springer, 2014.
[23] YANNIOTIS S. Solving problems in food engineering[M]. New York, USA:Springer, 2008.
[24] GUO Z Y, ZHOU S Q, LI Z X, et al. Theoretical analysis and experimental confirmation of the uniformity principle of temperature difference field in heat exchanger[J]. International Journal of Heat and Mass Transfer, 2002, 45(10):2119-2127.

基金

闵敬春,副教授,E-mail:minjc@tsinghua.edu.cn

PDF(13636 KB)

Accesses

Citation

Detail

段落导航
相关文章

/