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Modeling the performance of water-zeolite 13X adsorption heat pump

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The dynamic performance of cylindrical double-tube adsorption heat pump is numerically analysed using a non-equilibrium model, which takes into account both heat and mass transfer processes. The model includes conservation equations for: heat transfer in heating/cooling fluids, heat transfer in the metal tube, and heat and mass transfer in the adsorbent. The mathematical model is numerically solved using the method of lines. Numerical simulations are performed for the system water-zeolite 13X, chosen as the working pair. The effect of the evaporator and condenser temperatures on the adsorption and desorption kinetics is examined. The results of the numerical investigation show that both of these parameters have a significant effect on the adsorption heat pump performance. Based on computer simulation results, the values of the coefficients of performance for heating and cooling are calculated. The results show that adsorption heat pumps have relatively low efficiency compared to other heat pumps. The value of the coefficient of performance for heating is higher than for cooling
Rocznik
Strony
191–--207
Opis fizyczny
Bibliogr. 23 poz., rys., tab., wz.
Twórcy
autor
  • West Pomeranian University of Technology, Szczecin, Institute of Chemical Engineering and Environmental Protection Processes, al. Piastów 42, 71-065 Szczecin, Poland
autor
  • West Pomeranian University of Technology, Szczecin, Institute of Chemical Engineering and Environmental Protection Processes, al. Piastów 42, 71-065 Szczecin, Poland
Bibliografia
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  • [4] Ambrożek B., Zwarycz-Makles K., Szaflik W.: Equilibrium and heat of ad-sorption for selected adsorbent-adsorbate pairs used in adsorption heat pumps. Polska Energetyka Słoneczna 5(2012), 1-4, 1-11.
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  • [6] Yong L., Sumathy K.: Review of mathematical investigation on the closed adsorption heat pump and cooling system. Renew. Sust. Energ. Rev. 6(2002), 305-337.
  • [7] Pesaran A., Lee H., Hwang Y., Radermacher R., Chun H.H.: Review article: Numerical simulation of adsorption heat pumps. Energy 100(2016), 310-320.
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  • [14] Ko D., Kim M., Moon I., Choi D.: Analysis of purge gas temperature in cyclic TSA process. Chem. Eng. Sci. 57(2002), 179-195.
  • [15] Ruthven D.M., Farooq S., Knaebel K.S.: Pressure swing adsorption. VCH, New York 1994.
  • [16] Schiesser W.: The numerical method of lines: integration of partial differential equations. Academic Press, San Diego 1991.
  • [17] Kane A., Giraudet S., Vilmain J.B., Le Cloirec P.: Intensification of the temperature-swing adsorption process with a heat pump for the recovery of dichloromethane. J. Environ. Chem. Eng. 3(2015), 734-743.
  • [18] Chuaa H.T., Nga K.C., Maleka A., Kashiwagib T., Akisawab A., Sahab B.B.: Modeling the performance of two-bed, sillica gel-water adsorption chillers. Int. J. Refrig. 22(1999), 194-204.
  • [19] Sakoda A., Suzuki M.: Fundamental study on solar powered adsorption cooling system. J. Chem. Eng. Jpn. 17(1984), 52-57.
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  • [21] Saha B.B, Boelman E.C., Kashiwagi T.: Computer simulation of a silica gel-water adsorption refrigeration cycle – the influence of operating conditions on cooling output and COP. ASHRAE Trans. Res. 101(1995), 348-357.
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Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-6183c277-11e8-4c7a-8a0d-e76cf56925f0
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