TY - GEN
T1 - Optimized Mass Velocity for Evaporator of Organic Rankine Cycle Using R1234ze(E) for 373.15-423.15 K Geothermal Water
AU - Ge, Zhong
AU - Liu, Qiang
AU - Yang, Zhen
AU - Li, Jian
AU - Duan, Yuanyuan
N1 - Publisher Copyright:
© 2018 IEEE.
PY - 2018/5/8
Y1 - 2018/5/8
N2 - Organic Rankine cycle (ORC) is a promising technology for medium and low temperature geothermal water power generation due to its simple structure, good applicability, and user-friendliness. The evaporator absorbs heat from heat source and facilitates the evaporation of working fluid, the performance of it has an important influence on ORC system. The working fluid mass velocity is the important parameter for evaporator, the increment of mass velocity can enhance heat transfer coefficient and decrease heat transfer temperature, but it also increases pressure drop and heat transfer area, the selection of working fluid mass velocity is important for ORC system. There has been few studies on the working fluid mass velocity for ORC evaporator. The thermodynamic and economic performance of geothermal water ORC system using R1234ze(E) are analyzed, the working fluid mass velocity influences of evaporator on geothermal water outlet temperature, net power output, thermal efficiency, exergy efficiency and electricity generation cost (EGC) are studied, the optimal mass velocities for maximizing net power output and minimizing EGC are obtained for 373.15-423.15 K geothermal water respectively. The results show increasing mass velocity can increase net power output and exergy efficiency, EGC initially decreases and then increases with increasing mass velocity; optimal mass velocities increase with increasing geothermal water inlet temperature; when geothermal water inlet temperature is 418.15K, the EGC of case 2 can decreases by 22.73% compared with case 1.
AB - Organic Rankine cycle (ORC) is a promising technology for medium and low temperature geothermal water power generation due to its simple structure, good applicability, and user-friendliness. The evaporator absorbs heat from heat source and facilitates the evaporation of working fluid, the performance of it has an important influence on ORC system. The working fluid mass velocity is the important parameter for evaporator, the increment of mass velocity can enhance heat transfer coefficient and decrease heat transfer temperature, but it also increases pressure drop and heat transfer area, the selection of working fluid mass velocity is important for ORC system. There has been few studies on the working fluid mass velocity for ORC evaporator. The thermodynamic and economic performance of geothermal water ORC system using R1234ze(E) are analyzed, the working fluid mass velocity influences of evaporator on geothermal water outlet temperature, net power output, thermal efficiency, exergy efficiency and electricity generation cost (EGC) are studied, the optimal mass velocities for maximizing net power output and minimizing EGC are obtained for 373.15-423.15 K geothermal water respectively. The results show increasing mass velocity can increase net power output and exergy efficiency, EGC initially decreases and then increases with increasing mass velocity; optimal mass velocities increase with increasing geothermal water inlet temperature; when geothermal water inlet temperature is 418.15K, the EGC of case 2 can decreases by 22.73% compared with case 1.
KW - R1234ze(E)
KW - mass velocity
KW - optimization
KW - organic Rankine cycle
KW - thermodynamic and economic analysis
UR - http://www.scopus.com/inward/record.url?scp=85048362465&partnerID=8YFLogxK
U2 - 10.1109/ICGEA.2018.8356274
DO - 10.1109/ICGEA.2018.8356274
M3 - Conference contribution
AN - SCOPUS:85048362465
T3 - Proceedings - 2018 2nd International Conference on Green Energy and Applications, ICGEA 2018
SP - 28
EP - 35
BT - Proceedings - 2018 2nd International Conference on Green Energy and Applications, ICGEA 2018
PB - Institute of Electrical and Electronics Engineers Inc.
T2 - 2nd International Conference on Green Energy and Applications, ICGEA 2018
Y2 - 24 March 2018 through 26 March 2018
ER -