Performance analysis and improvement of geothermal binary cycle power plant in oilfield

In order to improve the efficiency of a geothermal power plant, oil wells in the high water cut stage were used as geothermal wells, thereby improving the recovery ratio and economic benefit. A new function that reflects both the technical and economic performances was put forward and used as the objective function. An organic Rankine cycle (ORC) was analyzed through the energetic and exergetic analyses, and the reasons for low efficiency were pinpointed. Results indicate that geothermal water directly transferring heat to the working fluid reduces energy dissipation and increases cycle efficiencies. The net power output with an internal heat exchanger (IHE) is averagely 5.3% higher than that without an IHE. R601a and R601 can be used to replace R123 for geothermal water below 110 °C. Moreover, the modified ORC dramatically outperforms the actual one.

[1]  D. Brüggemann,et al.  Exergy based fluid selection for a geothermal Organic Rankine Cycle for combined heat and power generation , 2010 .

[2]  Mehmet Kanoglu,et al.  Performance and parametric investigation of a binary geothermal power plant by exergy , 2008 .

[3]  Mortaza Yari,et al.  Performance analysis of the different Organic Rankine Cycles (ORCs) using dry fluids , 2009 .

[4]  N. Lai,et al.  Working fluids for high-temperature organic Rankine cycles , 2007 .

[5]  W. Worek,et al.  Optimum design criteria for an Organic Rankine cycle using low-temperature geothermal heat sources , 2007 .

[6]  H. Miyamoto,et al.  A Thermodynamic Property Model for Fluid-Phase Propane , 2000 .

[7]  Ulli Drescher,et al.  Optimierungspotenzial des Organic Rankine Cycle für biomassebefeuerte und geothermische Wärmequellen , 2008 .

[8]  Santanu Bandyopadhyay,et al.  Process integration of organic Rankine cycle , 2009 .

[9]  Wang Xiao-yuan Parametric optimization of low-temperature waste heat power generation system by simulated annealing algorithm , 2012 .

[10]  H. Martin A theoretical approach to predict the performance of chevron-type plate heat exchangers , 1996 .

[11]  Tong Dao-hui Comparison of thermodynamic performance for waste heat power generation system with different low temperature working fluids , 2010 .

[12]  Z. Ayub,et al.  Experimental investigation of single phase convective heat transfer coefficient in a corrugated plate heat exchanger for multiple plate configurations , 2010 .

[13]  Mehmet Kanoglu,et al.  Exergy analysis of a dual-level binary geothermal power plant , 2002 .

[14]  Ronald DiPippo,et al.  Second Law assessment of binary plants generating power from low-temperature geothermal fluids , 2004 .

[15]  Ramazan Köse,et al.  Exergoeconomic optimization of integrated geothermal system in Simav, Kutahya , 2010 .

[16]  Junye Hua,et al.  Thermodynamic analysis of simplified dual-pressure ammonia-water absorption power cycle , 2012 .

[17]  Yiping Dai,et al.  Exergy analyses and parametric optimizations for different cogeneration power plants in cement industry , 2009 .

[18]  Tao Guo,et al.  Comparative analysis of natural and conventional working fluids for use in transcritical Rankine cycle using low‐temperature geothermal source , 2011 .

[19]  Axel Polt,et al.  Thermophysical Properties of Refrigerants , 1990 .

[20]  Mortaza Yari,et al.  Exergetic analysis of various types of geothermal power plants , 2010 .

[21]  Enrico Barbier,et al.  Geothermal energy technology and current status: an overview , 2002 .

[22]  Björn Palm,et al.  Plate Heat Exchangers: Calculation Methods for Singleand Two-Phase Flow , 2006 .

[23]  A. Borsukiewicz-Gozdur,et al.  Maximising the working fluid flow as a way of increasing power output of geothermal power plant , 2007 .