OPTIMAL DESIGN OF COMPACT ORGANIC RANKINE CYCLE UNITS FOR DOMESTIC SOLAR APPLICATIONS

Organic Rankine cycle turbogenerators are a promising technology to transform the solar radiation harvested by solar collectors into electric power. The present work aims at sizing a small-scale organic Rankine cycle unit by tailoring its design for domestic solar applications. Stringent design criteria, i. e., compactness, high performance and safe operation, are targeted by adopting a multi-objective optimization approach modeled with the genetic algorithm. Design-point thermodynamic variables, e. g., evaporating pressure, the working fluid, minimum allowable temperature differences, and the equipment geometry, are the decision variables. Flat plate heat exchangers with herringbone corrugations are selected as heat transfer equipment for the preheater, the evaporator and the condenser. The results unveil the hyperbolic trend binding the net power output to the heat exchanger compactness. Findings also suggest that the evaporator and condenser minimum allowable temperature differences have the largest impact on the system volume and on the cycle performances. Among the fluids considered, the results indicate that R1234yf and R1234ze are the best working fluid candidates. Using flat plate solar collectors (hot water temperature equal to 75 °C), R1234yf is the optimal solution. The heat exchanger volume ranges between 6.0 and 23.0 dm3, whereas the thermal efficiency is around 4.5%. R1234ze is the best working fluid employing parabolic solar collectors (hot water temperature equal to 120 °C). In such case the thermal efficiency is around 6.9%, and the heat exchanger volume varies from 6.0 to 18.0 dm3.

[1]  M. McLinden,et al.  NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 8.0 , 2007 .

[2]  K. S. Lee,et al.  Experiments on the characteristics of evaporation of R410A in brazed plate heat exchangers with different geometric configurations , 2003 .

[3]  R. K. Ursem Multi-objective Optimization using Evolutionary Algorithms , 2009 .

[4]  Yiping Dai,et al.  Multi-objective optimization of an organic Rankine cycle (ORC) for low grade waste heat recovery using evolutionary algorithm , 2013 .

[5]  Kuppan Thulukkanam Heat Exchanger Design Handbook , 2013 .

[6]  Giovanni Antonio Longo Heat transfer and pressure drop during HFC refrigerant saturated vapour condensation inside a brazed plate heat exchanger , 2010 .

[7]  E. Schlunder Heat exchanger design handbook , 1983 .

[8]  Brian Elmegaard,et al.  Multi-objective optimization of organic Rankine cycles for waste heat recovery: Application in an offshore platform , 2013 .

[9]  Vincent Lemort,et al.  Techno-economic survey of Organic Rankine Cycle (ORC) systems , 2013 .

[10]  Sarah Rothstein Fundamentals Of Heat Exchanger Design , 2016 .

[11]  Fredrik Haglind,et al.  Design and optimisation of organic Rankine cycles for waste heat recovery in marine applications using the principles of natural selection , 2013 .

[12]  S. Quoilin,et al.  Performance and design optimization of a low-cost solar organic Rankine cycle for remote power generation , 2011 .

[13]  Olav Bolland,et al.  Working fluids for low-temperature heat source , 2010 .

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

[15]  Bertrand F. Tchanche,et al.  Fluid selection for a low-temperature solar organic Rankine cycle , 2009 .

[16]  Piero Colonna,et al.  Efficiency Improvement in Precombustion CO2 Removal Units With a Waste–Heat Recovery ORC Power Plant , 2013 .