PERFORMANCE OF WORKING FLUIDS FOR POWER GENERATION IN A SUPERCRITICAL ORGANIC RANKINE CYCLE
被引:0
作者:
Vidhi, Rachana
论文数: 0引用数: 0
h-index: 0
机构:
Univ S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USAUniv S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
Vidhi, Rachana
[1
]
Kuravi, Sarada
论文数: 0引用数: 0
h-index: 0
机构:
Univ S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USAUniv S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
Kuravi, Sarada
[1
]
Besarati, Saeb
论文数: 0引用数: 0
h-index: 0
机构:
Univ S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USAUniv S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
Besarati, Saeb
[1
]
Stefanakos, E. K.
论文数: 0引用数: 0
h-index: 0
机构:
Univ S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USAUniv S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
Stefanakos, E. K.
[1
]
Goswami, D. Yogi
论文数: 0引用数: 0
h-index: 0
机构:
Univ S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USAUniv S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
Goswami, D. Yogi
[1
]
Sabau, Adrian S.
论文数: 0引用数: 0
h-index: 0
机构:
Oak Ridge Natl Lab, Mat Sci & Technol Div, Oak Ridge, TN USAUniv S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
Sabau, Adrian S.
[2
]
机构:
[1] Univ S Florida, Clean Energy Res Ctr, Tampa, FL 33620 USA
[2] Oak Ridge Natl Lab, Mat Sci & Technol Div, Oak Ridge, TN USA
来源:
PROCEEDINGS OF THE ASME 6TH INTERNATIONAL CONFERENCE ON ENERGY SUSTAINABILITY - 2012, PTS A AND B
|
2012年
关键词:
THERMODYNAMIC CYCLE;
D O I:
暂无
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 paper reports on the performance of various organic refrigerants and their mixtures as working fluids for power generation in a supercritical Rankine cycle (SRC) from geothermal sources. Organic fluids that have zero or very low ozone depletion potential and are environmentally safe are selected for this study. Geothermal source temperature is varied from 125-200 degrees C, and the cooling water temperature is changed from 10-20 degrees C. The effect of varying operating conditions on the performance of the thermodynamic cycle has been analyzed. Operating pressure of the cycle has been optimized for thermal efficiency for each fluid at each source temperature. The condensation pressure is determined by the cooling condition and is kept fixed for each condensation temperature. Energy and exergy efficiencies of the cycle have been obtained for the pure fluids as a function of heat source temperature. Mixtures of organic fluids have been analyzed and effect of composition on performance of the thermodynamic cycle has been studied. It is observed that thermal efficiency over 20% can be achieved for 200 degrees C heat source temperature and the lowest cooling temperature. When mixtures are considered as working fluids, the thermal efficiency of the cycle is observed to remain between the thermal efficiencies of the constituent fluids.