An Investigation on the Exergo-Economic Performance of an Evaporator in Orc Recovering Low-Grade Waste Heat

Based on the perspective of exergy recovery (profit), an exergo-economic performance evaluation model of evaporator in ORC recovering low-grade waste heat is established. Selecting dry fluid R600a as a working fluid, an exergo-economic criterion was defined to estimate the effects of operating parameters and tube length on the performance of evaporator when the boiling temperature of evaporator is fixed. The optimal flow rate of organic working fluid Gt (flow rate of exhaust flue gas Gs), the flow rate ratio of exhaust flue gas to organic working fluid y, and tube length l have been discovered to maximize the annual net profit value NPV. Furthermore, there exists the critical values of Gt (Gs), y, and l which make NPV = 0. The results also show that, with the increase of the flow rate ratio of exhaust flue gas to organic working fluid, the maximum annual net profit value first increases sharply, and then decreases slowly, while the optimal tube length of evaporator reduces monotonously. Furthermore, the evaluation method from purely thermodynamic viewpoint is imperfect, and the economic considerations change the results obtained with only the maximization of recovered exergy.

[1]  P. Mago,et al.  Performance analysis of different working fluids for use in organic Rankine cycles , 2007 .

[2]  Ashok Misra,et al.  Performance analysis of an Organic Rankine Cycle with superheating under different heat source temperature conditions , 2011 .

[3]  J. M. Coulson,et al.  Heat Transfer , 2018, A Concise Manual of Engineering Thermodynamics.

[4]  Zhen Lu,et al.  Performance analysis and optimization of organic Rankine cycle (ORC) for waste heat recovery , 2007 .

[5]  Alessandro Franco,et al.  Combined cycle plant efficiency increase based on the optimization of the heat recovery steam generator operating parameters , 2002 .

[6]  Jung-Yang San,et al.  Second-law performance of heat exchangers for waste heat recovery , 2010 .

[7]  A. M. Al Taweel,et al.  Modeling of heat recovery steam generator performance , 1997 .

[8]  Alessandro Franco,et al.  A general method for the optimum design of heat recovery steam generators , 2006 .

[9]  Vincent Lemort,et al.  Thermo-economic optimization of waste heat recovery Organic Rankine Cycles , 2011 .

[10]  E. Stefanakos,et al.  A REVIEW OF THERMODYNAMIC CYCLES AND WORKING FLUIDS FOR THE CONVERSION OF LOW-GRADE HEAT , 2010 .

[11]  Jiangfeng Wang,et al.  Parametric optimization and comparative study of organic Rankine cycle (ORC) for low grade waste heat recovery , 2009 .

[12]  V. Gnielinski New equations for heat and mass transfer in turbulent pipe and channel flow , 1976 .

[13]  M. K. Mishra,et al.  Parametric Optimization and Performance Analysis of a Regenerative Organic Rankine Cycle Using Low–Grade Waste Heat for Power Generation , 2011 .

[14]  B. Reddy,et al.  Second law analysis of a waste heat recovery based power generation system , 2007 .

[15]  W. Gu,et al.  Theoretical and experimental investigation of an organic Rankine cycle for a waste heat recovery system , 2009 .

[16]  S. M. Zubair,et al.  Second-law-based thermoeconomic optimization of two-phase heat exchangers , 1987 .

[17]  A. Franco,et al.  Thermodynamic optimisation of the operative parameters for the heat recovery in combined plants , 2000 .

[18]  Pedro J. Mago,et al.  An examination of exergy destruction in organic Rankine cycles , 2008 .

[19]  R. Bahrampoury,et al.  Optimization of fire tube heat recovery steam generators for cogeneration plants through genetic algorithm , 2010 .

[20]  Ramesh K. Shah,et al.  Costs of Irreversibilities in Heat Exchanger Design , 1983 .

[21]  Mehmet Kanoglu,et al.  Exergoeconomic analysis and optimization of combined heat and power production: A review , 2009 .

[22]  R. Radermacher,et al.  A study of flow boiling heat transfer with refrigerant mixtures , 1989 .

[23]  Ibrahim Dincer,et al.  An Exergy-Based Multi-Objective Optimization Of A Heat Recovery Steam Generator (HRSG) In A Combined Cycle Power Plant (CCPP) Using Evolutionary Algorithm , 2011 .

[24]  Alessandro Franco,et al.  Optimum thermal design of modular compact heat exchangers structure for heat recovery steam generators , 2005 .

[25]  T. Hung Waste heat recovery of organic Rankine cycle using dry fluids , 2001 .

[26]  K. Ashok Kumar,et al.  Second law analysis of a waste heat recovery steam generator , 2002 .

[27]  Sudipta De,et al.  Design and operation of a heat recovery steam generator with minimum irreversibility , 1997 .

[28]  Ahmed Z. Al-Garni,et al.  Effect of fouling on operational cost in pipe flow due to entropy generation , 2000 .

[29]  K. Gungor,et al.  A general correlation for flow boiling in tubes and annuli , 1986 .

[30]  Alessandro Franco,et al.  THERMOECONOMIC OPTIMIZATION OF HEAT RECOVERY STEAM GENERATORS OPERATING PARAMETERS FOR COMBINED PLANTS , 2004 .

[31]  Alessandro Franco,et al.  Thermodynamic Optimization of the Operative Parameters for the Heat Recovery in Combined Power Plants , 2001 .