|Table of Contents|

[1] Liu Yulan, Cao Zheng, Chen Jiufa, Xiong Jian, et al. Simulation and performance analysis of organic Rankine cyclecombined heat and power system [J]. Journal of Southeast University (English Edition), 2015, 31 (4): 489-495. [doi:10.3969/j.issn.1003-7985.2015.04.010]
Copy

Simulation and performance analysis of organic Rankine cyclecombined heat and power system()
Share:

Journal of Southeast University (English Edition)[ISSN:1003-7985/CN:32-1325/N]

Volumn:
31
Issue:
2015 4
Page:
489-495
Research Field:
Energy and Power Engineering
Publishing date:
2015-12-30

Info

Title:
Simulation and performance analysis of organic Rankine cyclecombined heat and power system
Author(s):
Liu Yulan1 Cao Zheng1 Chen Jiufa1 Xiong Jian2
1School of Energy and Environment, Southeast University, Nanjing 210096, China
2Lotusland Renewable Energy Holdings Limited, Shanghai 200233, China
Keywords:
organic Rankine cycle combined heat and power cycle efficiency exergy efficiency thermal efficiency
PACS:
TK21
DOI:
10.3969/j.issn.1003-7985.2015.04.010
Abstract:
To improve the overall thermal efficiency of the organic Rankine cycle(ORC), a simulation study was carried out for a combined heat and power(CHP)system, using the Redlich-Kuang-Soave(RKS)equation of state. In the system, R245fa was selected as the working fluid. A scroll expander was modeled with empirical isentropic expansion efficiency. Plate heat exchangers were selected as the evaporator and the condenser, and detailed heat transfer models were programmed for both one-phase and two-phase regions. Simulations were carried out at seven different heat source temperatures(80, 90, 100, 110, 120, 130, 140 ℃)in combination with eight different heat sink temperatures(20, 25, 30, 35, 40, 45, 50, 55 ℃). Results show that in the ORC without an internal heat exchanger(IHE), the optimum cycle efficiencies are in the range of 7.0% to 7.3% when the temperature differences between the heat source and heat sink are in the range of 70 to 90 ℃. Simulations on CHP reveal that domestic hot water can be produced when the heat sink inlet temperature is higher than 40 ℃, and the corresponding exergy efficiency and overall thermal efficiency are 29% to 56% and 87% to 90% higher than those in the non-CHP ORC, respectively. It is found that the IHE has little effect on the improvement of work output and efficiencies for the CHP ORC.

References:

[1] Manolakos D, Kosmadakis G, Kyritsis S. On site experimental evaluation of a low temperature solar organic Rankine cycle system for RO desalination[J]. Solar Energy, 2009, 83(5): 646-656.
[2] Madhawa H H D, Golubovic M, Worek W M, et al. Optimum design criteria for an organic Rankine cycle using low-temperature geothermal heat sources[J]. Energy, 2007, 32(9): 1698-1706.
[3] Liu H, Shao Y J, Li J X. A biomass-fired micro-scale CHP system with organic Rankine cycle(ORC)-thermodynamic modeling studies[J]. Biomass and Bioenergy, 2011, 35(9): 3985-3994.
[4] Wei D H, Lu X S, Lu Z, et al. Performance analysis and optimization of organic Rankine cycle(ORC)for waste heat recovery[J]. Energy Conversion and Management, 2007, 48(4): 1113-1119.
[5] Li M Q, Wang J F, He W F, et al. Construction and preliminary test of a low-temperature regenerative organic Rankine cycle(ORC)using R123[J]. Renewable Energy, 2013, 57(3): 216-222.
[6] Jradi M, Li J X, Liu H, et al. Micro-scale ORC-based combined heat and power system using a novel scroll expander[J]. International Journal of Low-Carbon Technologies, 2014, 9(2): 91-99.
[7] Zheng N, Zhao L, Wang X D, et al. Experimental verification of a rolling-piston expander that applied for low-temperature organic Rankine cycle[J]. Applied Energy, 2013, 112(16): 1265-1274.
[8] Pei G, Li J, Li Y Z, et al. Construction and dynamic test of a small-scale organic Rankine cycle[J]. Energy, 2011, 36(5): 3215-3223.
[9] Qiu G Q. Selection of working fluids for micro-CHP systems with ORC[J]. Renewable Energy, 2012, 48(6): 565-570.
[10] Aghahosseini S, Dincer I. Comparative performance analysis of low-temperature organic Rankine cycle(ORC)using pure and zeotropic working fluids[J]. Applied Thermal Engineering, 2013, 54(1): 35-42.
[11] Saleh B, Koglbauer G, Wendland M, et al. Working fluids for low-temperature organic Rankine cycles[J]. Energy, 2007, 32(7): 1210-1221.
[12] Onkar Singh. Applied thermodynamics[M]. New Delhi, India: Mechanical Engineering Department, Harcourt Butler Technological Institute, 2009.
[13] García-Cascales J R, Vera-García F, Corberán-Salvador J M, et al. Assessment of boiling and condensation heat transfer correlations in the modelling of plate heat exchangers[J]. International Journal of Refrigeration, 2007, 30(6): 1029-1041.
[14] Quoilin S. Sustainable energy conversion through the use of organic Rankine cycles for waste heat recovery and solar applications[D]. Liège, Belgium: University of Liège, 2011.

Memo

Memo:
Biographies: Liu Yulan(1990—), female, graduate; Chen Jiufa(corresponding author), male, doctor, professor, chen.jiufa@126.com.
Foundation item: Special Fund for Industry, University and Research Cooperation(No.2011DFR61130).
Citation: Liu Yulan, Cao Zheng, Chen Jiufa, et al.Simulation and performance analysis of organic Rankine cycle combined heat and power system[J].Journal of Southeast University(English Edition), 2015, 31(4):489-495.[doi:10.3969/j.issn.1003-7985.2015.04.010]
Last Update: 2015-12-20