4.7 Article

Performance prediction of HFC, HC, HFO and HCFO working fluids for high temperature water source heat pumps

Journal

APPLIED THERMAL ENGINEERING
Volume 185, Issue -, Pages -

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.applthermaleng.2020.116324

Keywords

High temperature heat pump; Working fluids screening; Critical parameters; Performance prediction; COP

Funding

  1. Beijing Nova Program [Z181100006218022]
  2. National Natural Sciences Foundation of China [51806229]

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A new performance prediction model for heat pump working fluids was proposed in this paper, aiming to provide a quick and easy way to screen a large number of working fluids for HTWSHP. The model showed good agreement with calculated values for specific volumetric heating capacity and coefficient of performance, and could be applied to different conditions such as varying compressor isentropic efficiencies and temperatures.
High temperature water source heat pumps (HTWSHP) plays an increasingly important role in drying and building heating due to its remarkable energy-saving effect. However, traditional heat pump working fluids such as R134a are not applicable for HTWSHP and the research on alternative working fluids is limited by the complex process of working fluids screening. This paper is aimed to quickly and easily obtain the performance of a large amount of working fluids for screening. A new simple performance predicted model was proposed in a simple vapor compression cycle at condensation temperatures from 70 to 110 degrees C. By knowing only a working fluid's critical temperature and pressure, the specific volumetric heating capacity (VHC) and coefficient of performance (COP) can be predicted. Based on the model, the performance prediction for the newer working fluids involving R1336mzz(Z) and R1224yd(Z) was conducted. The results produced by the model were compared with the values calculated by Peng-Robinson equation of state (PR EoS) and the default, high-accuracy equations implemented in REFPROP 10.0. The predicted values in this work show good agreement. Besides, the model can also be applied varying compressor isentropic efficiencies from 60% to 80%, superheats from 0 to 10 degrees C and subcoolings from 0 to 8 degrees C.

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