Dynamic Analysis of Single-Effect/Double-Lift Libr-Water Absorption System using Low-Temperature Hot Water

저온수를 이용하는 일중효용/이단승온 리튬브로마이드-물 흡수식 시스템의 동적 해석

  • Kim, Byong-Joo (Department of Mechanical and System Design Eng., Hongik University)
  • 김병주 (홍익대학교 기계.시스템디자인공학과)
  • Published : 2009.12.10

Abstract

Dynamic behavior of Libr-water absorption system using low-temperature hot water was investigated numerically. Thermal-hydraulic model of single-effect/double-lift 100 RT chiller was developed by applying transient conservation equations of total mass, Libr mass, energy and momentum to each component. Transient variations of system properties and transport variables were analysed during start-up operation. Numerical analysis were performed to quantify the effects of bulk concentration and part-load operation on the system performance in terms of cooling capacity, coefficient of performance, and time constant of system. For an absorption chiller considered in the present study, optimum bulk concentration was found to exist, which resulted in the minimum time constant with stable cooling capacity. COP and time constant increased as the load decreased down to 40%, below which the time constant increased abruptly and COP decreased as the load decreased further.

Keywords

References

  1. Schweigler, C., Hellmann H., Preissner, M., Demmel, S. and Ziegler, F. F., 1998, Operation and performance of a 350 kW(100 RT) singleeffect/double-lift absorption chiller in a district heating network, ASHRAE Trans. Vol. 104, No. 1, pp. 1420-1426
  2. Kim, Y., Ha, S., Ryu, J., Kim, C. and Kim, I., 2007, Commercialization of single effect/ double lift absorption chiller for a district heating network, Proc. of Summer Conf. of SAREK, pp. 903-910
  3. Yattara, A., Zhu, Y., and Ali, M. M., 2003, Comparison between solar single-effect and single-effect double-lift absorption machines (Part I), Applied Thermal Engineering, Vol. 23, pp. 1981–1992 https://doi.org/10.1016/S1359-4311(03)00132-7
  4. Rademacher, B. J., Moran, R., 2005, Transient simulation of an absorption chiller in a CHP system, Proc. Int. Absorption Heat Pump Conf., June 22-24, CO, USA
  5. Kohlenbach, P., and Ziegler, F., 2008, A dynamic simulation model for transient absorption chiller performance. Part I:The model, Int. J. Refrigeration, Vol. 31, No. 2, pp. 217-225 https://doi.org/10.1016/j.ijrefrig.2007.06.009
  6. Butterworth, D., 1974, A comparison of some void fraction relationships for co-current gasliquid flow, Int. J. Multiphase Flow, Vol. 1, pp. 845-8508 https://doi.org/10.1016/0301-9322(75)90038-5
  7. McNeely, L. A., 1979, "Thermodynamic properties of aqueous solutions of lithium bromide," ASHRAE Trans., PH-79-3, No. 3, pp. 413-434
  8. Beattie, D. R. H., 1973, A note on the calculation of two-phase pressure losses, Nuc. Eng. Des., Vol. 25, pp. 395-402 https://doi.org/10.1016/0029-5493(73)90034-4
  9. Schnabel, G. and Schlubder, E. U., Verfahrenstechnik, 14:79, 1980 referred' modelling heat and mass transport in falling liquid films,' Yih, S. M., pp. 11-210, edited by Cheremisinoff, N. P., Handbook of Heat and Mass Transfer, Vol. 2:Mass Transfer and reactor Design, 1986, Gulf Publishing Company
  10. Nusselt, W., 1916, The condensation of steam on cooled surface, Z. Ver. Dtsch. Ing., Vol. 60, pp. 541-546
  11. Kumar, H., 1984, "The plate heat exchanger:construction and design,” 1st UK National COnference on Heat Transfer, University of Leeds, 3-5 July, Inst. Chem. Eng. Symp., Series No. 86, p. 1275
  12. Lance, G. N., 1960, Numerical methods for high speed computer, Iliffe and Sons, pp. 54-57