Heat pump air conditioning system's (HPAC'S) performance enhancement was analyzed by means of simulation for 10 m pure electrical bus. The steady-state simulation model of HPAC was constructed, which was corrected and verified by the experimental data. The heat transfer coefficient increased because of the decrease of heat exchanger's diameter of the tube. Tube-fin heat exchanger with φ 5 mm diameter tube was designed to the new HPAC and new design's effect on system performance was simulated by verified simulation model. The cooling (heating) capacity was 23.2 kW (20.9 kW), and cooling EER (heating COP) was 3.14 (2.75). New HPAC's performance was improved, but couldn't meet improvement target. The simulation results showed that system's mass flow rate was lower than design value, and the compressor capacity was smaller than system requirement. The high efficiency scroll compressor not only increased the displacement, but also the cooling COP of the compressor was 3.45. The combination of the two factors improved the HPAC's energy efficiency. A high efficiency R410a scroll compressor was selected and applied to the same HPAC with the small diameter tube heat exchanger. The simulation results showed that cooling (heating) capacity reached to 26.4 kW (23.4 kW), while cooling EER (heating COP) reached to 3.64(3.16), which generally met design requirement that cooling (heating) capacity reached to 26 kW (22 kW), while cooling EER (heating COP) reached to 3.2(2.8).
HAN Lian-jin, WU Jiang-hong, XUE Zhi-qiang. Simulation and improvement of heat pump air conditioning system for electric bus. JOURNAL OF ZHEJIANG UNIVERSITY (ENGINEERING SCIENCE), 2018, 52(4): 641-648.
[1] MOUKALLED F, VERMA S, DARWISH M. The use of CFD for predicting and optimizing the performance of air conditioning equipment[J]. International Journal of Heat and Mass Transfer, 2011, 54(1-3):549-563.
[2] 张春路. 制冷空调系统仿真原理与技术[M]. 北京:化学工业出版社, 2012:87.
[3] 丁国良. 制冷空调装置的计算机仿真技术[J]. 科学通报, 2006, 51(9):998-1010. DING Guo-liang. The computer simulation technology of the refrigeration air conditioning equipment[J]. Chinese Science Bulletin, 2006, 51(9):998-1010.
[4] DABIRI A E, RICE C K. Compressor-simulation model with corrections for the level of suction gas superheat[J]. Ashrae Transactions, 1981, 87(pt2):771-782.
[5] GNIELINSKI V. New equations for heat and mass transfer in turbulent pipe and channel flows[J]. International Chemical Engineering, 1976, 16(2):359-368.
[6] DOBSON M K, CHATO J C. Condensation in smooth horizontal tubes[J]. Journal of Heat Transfer, 1998, 120(1):193-213.
[7] CHURCHILL S W. Comprehensive correlating equations for heat, mass and momentum transfer in fully developed flow in smooth tubes[J]. Industrial and Engineering Chemistry Fundamentals, 1977, 16(1):109-116.
[8] LIN Y T, HWANG Y M, WANG C C. Performance of the herringbone wavy fin under dehumidifying conditions[J]. International Journal of Heat and Mass Transfer, 2002, 45(25):5035-5044.
[9] SHEN B.Improvement and validation of unitary air conditioner and heat pump simulation models at off-design conditions[M].[S. l.]:ProQuest, 2006.