ANALYSIS OF HEAT-DRIVEN COMBINED COOLING AND DESALINATION

被引:0
作者
Alelyani, Sami M. [1 ]
Fette, Nicholas W. [1 ]
Stechel, Ellen B. [2 ]
Doron, Pinchas [3 ]
Phelan, Patrick E. [1 ]
机构
[1] Arizona State Univ, Sch Engn Matter Transport & Energy, Tempe, AZ 85287 USA
[2] Arizona State Univ, LightWorks, Tempe, AZ 85287 USA
[3] AORA Solar Ltd, Rehovot, Central Distric, Israel
来源
PROCEEDINGS OF THE ASME INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION, 2016, VOL. 6B | 2017年
关键词
Ammonia-water absorption refrigeration; multi-effect distillation; integrated refrigeration and desalination system; water desalination; EFFICIENCY COMBINED DESALINATION; REFRIGERATION; SEAWATER; ENERGY; SYSTEM; WATER; DISTILLATION; FEASIBILITY; ENVIRONMENT; PROPOSAL;
D O I
暂无
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
This paper investigates the opportunities for integrating thermally driven cooling systems with thermally driven desalination systems via cascade of reject heat. Single- and double-stage ammonia-water (NH3-H2O) absorption refrigeration systems with multi-effect distillation (MED) are selected for this study based on technical limitations and practical considerations. Cooling capacity and hourly water production are calculated from thermodynamic properties of the working fluids at different operating conditions using simple models for each of the constituent systems. Additionally, the second law of thermodynamics is applied with the aim of examining the entropy generation of each component as well as the total exergy destruction of the entire system. The results indicate that the total exergy destruction of the combined systems, which consist of an MED unit driven by either a single- or double-stage NH3-H2O refrigeration system, decreases by an average of 55% compared to stand-alone NH3-H2O and MED systems. Relative to stand-alone systems, although water production decreases by 30% and 9% when an MED unit is integrated with single- and double-stage NH3-H2O absorption systems, respectively, cooling capacity remains unchanged for the double-stage NH3-H2O MED system, and only decreases by 16% for the single-stage NH3-H2O MED system.
引用
收藏
页数:14
相关论文
共 26 条
[1]   Second law based thermodynamic analysis of ammonia-water absorption systems [J].
Adewusi, SA ;
Zubair, SM .
ENERGY CONVERSION AND MANAGEMENT, 2004, 45 (15-16) :2355-2369
[2]   Energy consumption and water production cost of conventional and renewable-energy-powered desalination processes [J].
Al-Karaghouli, Ali ;
Kazmerski, Lawrence L. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 24 :343-356
[3]   Application of absorption heat pumps to multi-effect distillation:: a case study of solar desalination [J].
Alarcon-Padilla, Diego-Cesar ;
Garcia-Rodriguez, Lourdes .
DESALINATION, 2007, 212 (1-3) :294-302
[4]   The feasibility of integrating ME-TVC plus MEE with Azzour South Power Plant: Economic evaluation [J].
Alasfour, F. N. ;
Bin Amer, A. O. .
DESALINATION, 2006, 197 (1-3) :33-49
[5]   A study of a new thermal vapor compression multi-effect stack (TVC/MES) low temperature distillation system [J].
Aly, SE .
DESALINATION, 1995, 103 (03) :257-263
[6]  
Amelia Elson A.H., 2015, Waste heat to power market assessment
[7]  
Cengel Y., 1989, Thermodynamics and Engineering Approach,"
[8]  
Dai AG, 2013, NAT CLIM CHANGE, V3, P52, DOI [10.1038/nclimate1633, 10.1038/NCLIMATE1633]
[9]   A review of thermally activated cooling technologies for combined cooling, heating and power systems [J].
Deng, J. ;
Wang, R. Z. ;
Han, G. Y. .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2011, 37 (02) :172-203
[10]  
DOE U., 2008, WAST HEAT REC TECHN