Abstract
The purpose of this study was to experimentally investigate the viscosity for carbon dioxide with nitrogen and methane impurities under supercritical conditions. The experimental setup was comprised of a test section, a condensation section for the liquefaction of carbon dioxide before entering the pump, and a heating section for controlling the temperature of the entrance of the test section. The test section was comprised of a capillary tube with a length of 300 mm and a ⅛ inch diameter. The experiment was performed under a mass flux of 200~400 kg/(m²s) at a impurities concentration of 1.0~5.0 mol%. The viscosity of nitrogen mixture was lower by 0.5% for 1% mole fraction, 4.9% for 3% mole fraction, and 23.5% for 5% mole fraction compared with that of pure CO₂. The viscosity of methane mixture was lower by 7.3% for 1% mole fraction, 11.2% for 3% mole fraction, and 24.4% for 5% mole fraction compared with that of pure CO₂. A model for predicting the viscosity of CO₂ mixtures under the supercritical condition was developed by the multi-variable regression analysis. The model included the non-dimensional parameters for temperature, pressure, and density.
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More From: Korean Journal of Air-Conditioning and Refrigeration Engineering
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