Investigation of new mechanical heat pump systems for heat upgrading applications

In this study, two novel high‐temperature heat pump systems based on vapor compression cycles are introduced and examined. Three fluids (water, cyclohexane, and biphenyl) are selected and analyzed thermodynamically as prospective working fluids for the high‐temperature heat pumps. These working fluids are used in cascaded cycles to upgrade the heat to a temperature of 600°C. The equations of state used in performance analysis are Peng‐Robinson, non‐random two‐liquid model, and International Association for the Properties of Water and Steam 95. A parametric analysis is carried out to study the effects of isentropic efficiency, sink temperature, source temperature, and ambient temperature on the system performance. Both energetic and exergetic coefficients of performance (COPs) of the overall and individual cycles are determined. The COP values obtained are found to range from 2.3 to 3.8, depending upon the cycle and temperature levels. The high COP values in some instances make these systems promising alternatives to fossil fuel and electrical heating. As a possible sustainable scenario, these pumps can utilize low‐grade heat from geothermal, nuclear, or thermal power plants and derive work from clean energy sources (solar, wind, nuclear) to deliver high‐grade heat. The high delivery temperatures make these heat pumps suitable for processes with corresponding needs, like high‐temperature endothermic reactions, metallurgical processes, distillation, and thermochemical water splitting.

[1]  Clemens Forman,et al.  Estimating the global waste heat potential , 2016 .

[2]  Riccardo Brignoli,et al.  Parametric investigation of working fluids for organic Rankine cycle applications , 2015 .

[3]  Dianfeng Li,et al.  Selection of organic Rankine cycle working fluids in the low-temperature waste heat utilization , 2015 .

[4]  Gequn Shu,et al.  Alkanes as working fluids for high-temperature exhaust heat recovery of diesel engine using organic Rankine cycle , 2014 .

[5]  C. W. Chan,et al.  A review of chemical heat pumps, thermodynamic cycles and thermal energy storage technologies for low grade heat utilisation , 2013 .

[6]  I. Dincer Green methods for hydrogen production , 2012 .

[7]  J. Greet,et al.  Trends in global CO2 emissions: 2012 report , 2012 .

[8]  M. M. Prieto,et al.  Thermodynamic analysis of high-temperature regenerative organic Rankine cycles using siloxanes as working fluids , 2011 .

[9]  Wenming Yang,et al.  Advances in heat pump systems: A review , 2010 .

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

[11]  G. Naterer,et al.  Upgrading of Waste Heat for Combined Power and Hydrogen Production With Nuclear Reactors , 2010 .

[12]  G. Naterer,et al.  Performance evaluation of organic and titanium based working fluids for high-temperature heat pumps , 2009 .

[13]  George Papadakis,et al.  Comparative thermodynamic study of refrigerants to select the best for use in the high-temperature stage of a two-stage organic Rankine cycle for RO desalination , 2009 .

[14]  Ibrahim Dincer,et al.  Performance investigation of high-temperature heat pumps with various BZT working fluids , 2009 .

[15]  Vincent Lemort,et al.  Technological and Economical Survey of Organic Rankine Cycle Systems , 2009 .

[16]  I. Dincer,et al.  Thermodynamic analysis of the copper production step in a copper-chlorine cycle for hydrogen production , 2008 .

[17]  Lieve Helsen,et al.  Influence of massive heat-pump introduction on the electricity-generation mix and the GHG effect: Comparison between Belgium, France, Germany and The Netherlands , 2008 .

[18]  Cletus Chukwu,et al.  PROCESS ANALYSIS AND ASPEN PLUS SIMULATION OF NUCLEAR-BASED HYDROGEN PRODUCTION WITH A COPPER-CHLORINE CYCLE , 2008 .

[19]  Marc A. Rosen,et al.  TOWARDS ENERGY SUSTAINABILITY: A QUEST OF GLOBAL PROPORTIONS , 2008 .

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

[21]  Ibrahim Dincer,et al.  Exergy: Energy, Environment and Sustainable Development , 2007 .

[22]  Gilles Flamant,et al.  Screening of water-splitting thermochemical cycles potentially attractive for hydrogen production by concentrated solar energy , 2006 .

[23]  Zhao Li,et al.  Investigation on incomplete condensation of non-azeotropic working fluids in high temperature heat pumps , 2006 .

[24]  Calin Zamfirescu,et al.  Twin screw oil-free wet compressor for compression–absorption cycle , 2006 .

[25]  Cesare Marchetti,et al.  Long-term global vision of nuclear-produced hydrogen , 2006 .

[26]  Jahar Sarkar,et al.  Transcritical CO2 heat pump systems: exergy analysis including heat transfer and fluid flow effects , 2005 .

[27]  Michele A. Lewis,et al.  Hydrogen Production at <550°C Using a Low Temperature Thermochemical Cycle , 2004 .

[28]  Jostein Pettersen,et al.  Fundamental process and system design issues in CO2 vapor compression systems , 2004 .

[29]  J.B.J. Veldhuis,et al.  Determination of structural, thermodynamic and phase properties in the Na2S–H2O system for application in a chemical heat pump , 2002 .

[30]  Yoshio Yoshizawa,et al.  Application of a chemical heat pump to a cogeneration system , 2001 .

[31]  Eckhard A. Groll,et al.  Efficiencies of transcritical CO2 cycles with and without an expansion turbine , 1998 .

[32]  H. Auracher Thermal design and optimization , 1996 .

[33]  Costante Mario Invernizzi,et al.  Potential performance of real gas Stirling cycle heat pumps , 1996 .

[34]  L.C.M Itard Wet compression versus dry compression in heat pumps working with pure refrigerants or non-azeotropic mixtures , 1995 .

[35]  Selahatti̇n Göktun Selection of working fluids for high-temperature heat pumps , 1995 .

[36]  G. Angelino,et al.  Cyclic Methylsiloxanes as Working Fluids for Space Power Cycles , 1993 .

[37]  Judith Gurney BP Statistical Review of World Energy , 1985 .

[38]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .