Boiling heat-transfer coefficient variation for R407C inside horizontal tubes of a refrigerating vapour-compression plant's shell-and-tube evaporator

Enrique Torrella, Joaquín Navarro-Esbrí and Ramón Cabello

Applied Energy, 2006, vol. 83, issue 3, 239-252

Abstract: The present paper presents experimental results obtained from a refrigerating vapour-compression plant's shell-and-tube (1-2) evaporator working with R407C. Several tests have been carried out to study the influence of the evaporating pressure and the refrigerant's mass flow rate on the refrigerant's boiling heat-transfer coefficient inside horizontal tubes. This work has been performed by analyzing the variations of the evaporator's overall thermal-resistance, computed using the effectiveness-NTU method, considering the influence of pressure drops and glide at the evaporator, and finally transferring the results and conclusions to the boiling heat-transfer coefficient. It has been observed that the variations of the boiling heat-transfer coefficient show a dependence on the evaporating temperature and the refrigerant's mass-flow rate, which has been analyzed in the test range.

Keywords: Shell-and-tube; heat-exchanger; R407C; Boiling; heat-transfer; coefficient; Overall; heat-transfer; coefficient; Refrigeration; vapour-compression; plant (search for similar items in EconPapers)
Date: 2006
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