To obtain a breakthrough in selecting high-efficient working pairs for absorption refrigeration
the energy diversion along with the working pair circulation in a single-stage absorption refrigeration system is investigated. By regarding solution enthalpy as the sum of excess enthalpy
solute enthalpy and solvent enthalpy
it is found that the excess enthalpy exerts either positive or negative effect on the performance coefficient. Moreover
comparison between the systems with a 100% or 0% efficiency heat recovery exchanger implies that the excess enthalpy effect is related with the heat recovery exchanger efficiency. Subsequently
system simulations forH
2
O/LiBr
R134a/[HMIM
]
[Tf
2
N
]
andR1234yf/[HMIM
]
[BF
4
]
show that the higher efficiency of heat recovery exchanger and the excess enthalpy effect together leadR1234yf/[HMIM
]
[BF
4
]
to acquire a higher coefficient of performance thanH
2
O/LiBr.
关键词
Keywords
references
AMASYALI K, EL-GOHARY N M. A review of data-driven building energy consumption prediction studies [J]. Renewable and Sustainable Energy Reviews, 2018, 81: 1192-1205.
ZEYGHAMI M, YOGI GOSWAMI D, STEFANAKOS E. A review of solar thermo-mechanical refrigeration and cooling methods [J]. Renewable and Sustainable Energy Reviews, 2015, 51: 1428-1445.
ERICKSON D C, ANAND G, KYUNG I. Heat-activated dual-function absorption cycle [J]. ASHRAE Transactions, 2004, 110(1): 515-524.
ABU-EIN S Q, FAYYAD S M, MOMANI W, et al. Performance analysis of solar powered absorption refrigeration system [J]. Heat and Mass Transfer, 2009, 46(2): 137-145.
HONG D L, TANG L, HE Y J, et al. A novel absorption refrigeration cycle [J]. Applied Thermal Engineering, 2010, 30(14): 2045-2050.
YOKOZEKI A. Theoretical performances of various refrigerant-absorbent pairs in a vapor-absorption refrigeration cycle by the use of equations of state [J]. Applied Energy, 2005, 80(4): 383-399.
KIM S, PATEL N, KOHL P A. Performance simulation of ionic liquid and hydrofluorocarbon working fluids for an absorption refrigeration system [J]. Industrial Engineering Chemistry Research, 2013, 52(19): 6329-6335.
HE L J, TANG L M, CHEN G M. Performance prediction of refrigerant-DMF solutions in a single-stage solar-powered absorption refrigeration system at low generating temperatures [J]. Solar Energy, 2009, 83(11): 2029-2038.
LIANG Shiqiang, ZHAO Jie, WANG Li, et al. Absorption refrigeration cycle utilizing a new working pair of ionic liquid type [J]. Journal of Engineering Thermophysics, 2010, 31(10): 1627-1630.
BAI L H, LIU X Y, HE M G. A new thermodynamic cycle of heat pump relying on excess enthalpy changing [J]. Applied Thermal Engineering, 2019, 150: 605-611.
KOUREMENOS D, ROGDAKIS E D. Thermodynamic cycles for refrigeration and heat transformer units H2O/LiBr [J]. Forschung Im Ingenieurwesen: A, 1988, 54(2): 39-47.
BAI Lihang, LIU Siqi, YE Zheng, et al. Investigation on the performance of R1234ze(E)in absorption refrigeration and ejection refrigeration systems [J]. Applied Thermal Engineering, 2019, 161: 114120.
SOUACˇUKOVÁ M, KLOMFAR J, PÁTEK J. Measurements and group contribution analysis of 0.1 MPa densities for still poorly studied ionic liquids with the[PF6] and [NTf2]anions [J]. The Journal of Chemical Thermodynamics, 2014, 77: 31-39.
KLOMFAR J, SOUCKOVA M, PATEK J. Temperature dependence measurements of the density at 0.1 MPa for 1-alkyl-3-methylimidazolium-based ionic liquids with the trifluoromethanesulfonate and tetrafluoroborate anion [J]. Journal of Chemical Engineering Data, 2010, 55(9): 4054-4057.
BLOKHIN A V, PAULECHKA A Y U, KABO G J. Thermodynamic properties of[C6 mim][NTf2]in the condensed state [J]. Journal of Chemical Engineering Data, 2006, 51(4): 1377-1388.
WALISZEWSKI D. Heat capacities of the mixtures of ionic liquids with methanol at temperatures from 283.15 K to 323.15 K [J]. The Journal of Chemical Thermodynamics, 2008, 40(2): 203-207.
LIU Xiangyang, BAI Lihang, LIU Siqi, et al. Vapor-liquid equilibrium of r1234yf/[HMIM][Tf2N]and r1234ze(E)/[HMIM][Tf2N]working pairs for the absorption refrigeration cycle [J]. Journal of Chemical Engineering Data, 2016, 61(11): 3952-3957.
REN W, SCURTO A M. Phase equilibria of imidazolium ionic liquids and the refrigerant gas, 1,1,1,2-tetrafluoroethane(R-134a)[J]. Fluid Phase Equilibria, 2009, 286(1): 1-7.
LEMMON E W, HUBER M L, MCLINDEN M O. NIST reference fluid thermodynamic and transport properties—REFPROP [EB/OL]. [2020-04-01]. https: ∥data.nist.gov/od/id/ECBCC1C130222ED9E04 306570681B10740.