کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
5013246 | 1462831 | 2017 | 14 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Operation characteristic of a R123-based organic Rankine cycle depending on working fluid mass flow rates and heat source temperatures
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی انرژی
انرژی (عمومی)
پیش نمایش صفحه اول مقاله
چکیده انگلیسی
The test and operation characteristic of an organic Rankine cycle using R123 and a scroll expander have been investigated. The steady-state operation characteristic is addressed with the varying working fluid mass flow rates ranging of 0.124-0.222Â kg/s and heat source temperatures ranging of 383.15-413.15Â K. The behaviors and detailed discussion for those four major components (pump, evaporator, expander and condenser) are examined. The experimental results show that the environmental temperature presents a higher influence on the pump behaviors. The range of pump power consumption, isentropic efficiency and back work ratio are 0.21-0.32Â kW, 26.76-53.96%, and 14-32%, respectively. The expander isentropic efficiency presents a slight decrease first and then a sharp increase with mass flow rate, while a degree of superheating more than 3Â K is necessary to avoid expander cavitation. The expander isentropic and generator efficiencies are in range of 69.10-85.17% and 60-73%, respectively, while the respective heat transfer coefficients for evaporator and condenser are ranging of 200-400 and 450-2000Â W/m2Â K. The maximum expander shaft power and electrical power are 2.78Â kW and 2.01Â kW, respectively, while the maximum system generating efficiency is 3.25%. Moreover, the tested thermal efficiency presents a slight decrease trend with mass flow rate.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Energy Conversion and Management - Volume 131, 1 January 2017, Pages 55-68
Journal: Energy Conversion and Management - Volume 131, 1 January 2017, Pages 55-68
نویسندگان
Yong-Qiang Feng, Tzu-Chen Hung, Shang-Lun Wu, Chih-Hung Lin, Bing-Xi Li, Kuo-Chen Huang, Jiang Qin,