Dynamic Performance Investigation of Single-Effect NH3 + LiNO3 and NH3 + NaSCN Solar Cooling Cycles: A Case Study for Western Indian Climate

被引:2
作者
Modi, Nishant [1 ]
Pandya, Bhargav [2 ]
Kumar, Vinay [3 ]
Patel, Jatin [4 ]
机构
[1] Heatex Ind Ltd, Dept Design, Surat 394315, Gujarat, India
[2] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
[3] Griffith Univ, Sch Engn & Built Environm, Southport, Qld 4215, Australia
[4] Pandit Deendayal Petr Univ, Sch Technol, Gandhinagar 382007, Gujarat, India
来源
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME | 2020年 / 142卷 / 05期
关键词
dynamic analysis; absorption cooling; NH3 + NaSCN; NH3 + LiNO3; evaporator temperature; clean energy; renewable; solar; sustainability; ABSORPTION COOLING SYSTEM; OPTIMIZATION; SIMULATION;
D O I
10.1115/1.4046604
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This article compares the dynamic behavior of solar-assisted novel salt-based ammonia/sodium thiocyanate (NH3 + NaSCN) and ammonia/lithium nitrate (NH3 + LiNO3) single-effect absorption refrigeration cycles. An evacuated tube collector (ETC) is attached with fully mixed hot water storage tank to power the absorption system. Variations in ambient conditions are determined for Gujarat Region of India and their effects on absorption cycles are quantified throughout the days for the months of April to September. System performance is investigated and compared on terms of coefficient of performance (COP), refrigeration capacity, efficiency and solar COP (SCOP). At same operating conditions, it is found that the NH3 + LiNO3 cycle can achieve much lower evaporator temperature (-13.1 degrees C) then NH3 + NaSCN cycle (-7.5 degrees C) and maximum possible COP for NH3 + NaSCN cycle is 0.73 and 0.68 for NH3 + LiNO3 cycle. The working limit of NH3 + LiNO3 cycle is wide ranging and narrow for NH3 + NaSCN cycle due to high crystallization possibility. SCOP varies from 0.18 to 0.43 for NH3 + NaSCN cycle and 0.17 to 0.39 for NH3 + LiNO3 cycle over the period of 6 months. Based on these findings, the suitable working cycle is justified.
引用
收藏
页数:8
相关论文
共 14 条
[1]  
Abdulateef J.M., 2008, International Journal of Mechanical and Materials Engineering, V3, P17
[2]   Simulation and optimization of a LiBr solar absorption cooling system with evacuated tube collectors [J].
Assilzadeh, F ;
Kalogirou, SA ;
Ali, Y ;
Sopian, K .
RENEWABLE ENERGY, 2005, 30 (08) :1143-1159
[3]   Energetic, exergetic and financial evaluation of a solar driven absorption chiller - A dynamic approach [J].
Bellos, Evangelos ;
Tzivanidis, Christos ;
Symeou, Christoforos ;
Antonopoulos, Kimon A. .
ENERGY CONVERSION AND MANAGEMENT, 2017, 137 :34-48
[4]   First law analysis of a novel double effect air-cooled non-adiabatic ammonia/salt absorption refrigeration cycle [J].
Cai, Dehua ;
He, Guogeng ;
Tian, Qiqi ;
Bian, Yifeng ;
Xiao, Ruxi ;
Zhang, Aoni .
ENERGY CONVERSION AND MANAGEMENT, 2015, 98 :1-14
[5]  
Duffie WABJA., 2013, SOLAR ENG THERMAL PR
[6]   Economical comparison between a solar-powered vapour absorption air-conditioning system and a vapour compression system in the Middle East [J].
Elsafty, A ;
Al-Daini, AJ .
RENEWABLE ENERGY, 2002, 25 (04) :569-583
[7]   First and second law analysis of ammonia/salt absorption refrigeration systems [J].
Farshi, L. Garousi ;
Ferreira, C. A. Infante ;
Mahmoudi, S. M. S. ;
Rosen, M. A. .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2014, 40 :111-121
[8]  
Klein F., 2007, ENG EQUATION SOLVER
[9]  
Modi N., 2019, INT J ENERG RES, V43, P1
[10]  
National Fire Protection Association, 2017, 704 NFPA