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Heat transfer coefficients under dry- and wet-surface conditions for a spirally coiled finned tube heat exchanger
Affiliation:1. ExxonMobil Upstream Research Company, Gas & Facilities Division, Houston, TX, USA;2. Texas A&M University-Kingsville, Kingsville, TX 78363, USA;3. Sustainable Thermal Systems Laboratory, George W. Woodruff School of Mechanical Engineering, Georgia Institute of Technology, Atlanta, GA 30332, USA;1. IEE – Institute of Energy and Environment, University of São Paulo, São Paulo, SP, Brazil;2. SISEA- Alternative Energy Systems Lab., Escola Politécnica, University of São Paulo, SP, Brazil
Abstract:In the present study, the average tube-side and air-side heat transfer coefficients in a spirally coiled finned tube heat exchanger under dry- and wet-surface conditions are experimentally investigated. The test section is a spiral-coil heat exchanger, which consists of six layers of concentric spirally coiled tube. Each tube is fabricated by bending a 9.6-mm outside diameter straight copper tube into a spiral coil of four turns. Aluminium fins with thickness 0.6 mm and outside diameter 28.4 mm are placed helically around the tube. The chilled water and the hot air are used as working fluids. The test runs are done at the air and water mass flow rates ranging between 0.02 and 0.2 kg/s and between 0.04 and 0.25 kg/s, respectively. The inlet-air and -water temperatures are between 35 and 60 °C and between 10 and 35 °C, respectively. The effects of the inlet conditions of both working fluids flowing through the heat exchanger on the heat transfer coefficients are discussed. New correlations based on the data gathered during this work for predicting the tube-side and air-side heat transfer coefficients for the spirally coiled finned tube heat exchanger are proposed.
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