Energy and exergy analyses of a novel hybrid system consisting of a phosphoric acid fuel cell and a triple-effect compression-absorption refrigerator with [mmim]DMP/CH3OH as working fluid

被引:24
作者
Chen, Wei [1 ]
Xu, Chenbin [1 ]
Wu, Haibo [1 ,2 ]
Bai, Yang [1 ]
Li, Zoulu [1 ]
Zhang, Bin [1 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Electromech Engn, Qingdao 266061, Peoples R China
[2] Songling Rd 99, Qingdao, Peoples R China
基金
中国国家自然科学基金;
关键词
Phosphoric acid fuel cell; Compression-absorption refrigerator; Hybrid system; mmim]DMP/CH3OH; Energy and exergy analyses; VAPOR-LIQUID-EQUILIBRIA; THERMODYNAMIC ANALYSIS; IONIC-LIQUID; HEAT-PUMP; WASTE-HEAT; PERFORMANCE; CYCLES; DRIVEN; WATER; OPTIMIZATION;
D O I
10.1016/j.energy.2020.116951
中图分类号
O414.1 [热力学];
学科分类号
摘要
Energy and exergy analyses were conducted on a proposed hybrid system consisting of a phosphoric acid fuel cell (PAFC) and a triple-effect compression-absorption refrigerator with [mmim]DMP/CH3OH as working fluid (HFCAR). The HFCAR system was modeled and simulated based on the current density model of PAFC, isentropic efficiency model of assisted compressor, and mass and energy conservation model of the compression-absorption refrigerator. For the basic design condition, the detailed operating parameters of each status point, energy conservation, temperature difference, and total thermal conductance of each component were simulated and discussed. For the variable conditions, the effects of electrical current density, PAFC temperature, and compression ratios on 16 key operating parameters were simulated and analyzed. A critical electrical current density was proposed. Under condition of critical current density, HFCAR system works as a cooling system with the largest cooling capacity. The variation characteristics of the critical electrical current density were studied. The exergy losses of each component were simulated and analyzed. The PAFC efficiency and heat transfer characteristic of certain components should be optimized to improve the thermal performance of the HFCAR system. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页数:17
相关论文
共 57 条
[1]   Isobaric vapor-liquid equilibria of 1,1-dimethylethoxy-butane plus methanol or ethanol plus water at 101.32 kPa [J].
Arce, Alberto ;
Arce, Alberto, Jr. ;
Manuel Martinez-Ageitos, Jose ;
Soto, Ana .
FLUID PHASE EQUILIBRIA, 2007, 259 (01) :57-65
[2]   Thermodynamic analysis of an ammonia/water absorption-resorption refrigeration system [J].
Berdasco, M. ;
Valles, M. ;
Coronas, A. .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2019, 103 :51-60
[3]   THERMODYNAMIC DESIGN-DATA FOR ABSORPTION HEAT-PUMP SYSTEMS OPERATING ON AMMONIA LITHIUM-NITRATE .3. SIMULTANEOUS COOLING AND HEATING [J].
BEST, R ;
RIVERA, W ;
PILATOWSKY, I ;
HOLLAND, FA .
HEAT RECOVERY SYSTEMS & CHP, 1991, 11 (04) :199-212
[4]   Performance of double effect absorption compression cycles for air-conditioning using methanol - TEGDME and TFE-TEGDME systems as working pairs [J].
Boer, D ;
Valles, M ;
Coronas, A .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 1998, 21 (07) :542-555
[5]   Exergy analysis of a novel air-cooled non-adiabatic absorption refrigeration cycle with NH3-NaSCN and NH3-LiNO3 refrigerant solutions [J].
Cai, Dehua ;
He, Guogeng ;
Tian, Qiqi ;
Tang, Weier .
ENERGY CONVERSION AND MANAGEMENT, 2014, 88 :66-78
[6]   Thermodynamic analysis of a novel air-cooled non-adiabatic absorption refrigeration cycle driven by low grade energy [J].
Cai, Dehua ;
He, Guogeng ;
Tian, Qiqi ;
Tang, Weier .
ENERGY CONVERSION AND MANAGEMENT, 2014, 86 :537-547
[7]  
Cal WH, 2007, P IMECE 2007 WASH, V6, P227
[8]   Vapour pressure measurements of ammonia/ionic liquids mixtures as suitable alternative working fluids for absorption refrigeration technology [J].
Cera-Manjarres, Andry ;
Salavera, Daniel ;
Coronas, Alberto .
FLUID PHASE EQUILIBRIA, 2018, 476 :48-60
[10]   Numerical investigation of the thermal performance of compressor-assisted double-effect absorption refrigeration using [mmim] DMP/CH3OH as working fluid [J].
Chen, Wei ;
Sun, Qiang ;
Bai, Yang ;
Zhang, Bin .
ENERGY CONVERSION AND MANAGEMENT, 2018, 166 :433-444