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- W2046543452 abstract "Experimental work was carried out on a single tube natural circulation reboiler. One copper and one stainless steel tube each equipped with a single steam jacket, and one stainless steel tube equipped with a six-compartment-steam jacket were used. All the tubes had nominal dimensions: 0.5 in. diameter and 48 in. height. Length-mean and local point coefficients of heat transfer and heat fluxes were obtained by three investigators, working independently, for water, isopropanol, n-propanol and their azeotropes. Two phase heat transfer coefficients for all five liquids were correlated by a single equation hTPhL = 0.065 (1Xtt) TsatΔTf) (σH2OσL)0.9 All the length-mean coefficients from runs with a two-phase mixture quality of between 0.02 and 0.68 at the tube exit are well within the ±20% accuracy limits. Point coefficients, from the sections of the tube in which no bubbly and liquid deficient flow regimes were suspected to occur, are correlated by the same equation within the accuracy limits of ±30%. The dimensionless groups (σH2O/σL) and (Tsat/ΔT) are powerful correlating factors. The first of them accounts for the differences in the nucleating properties of the various single component liquids. Flow fluctuations inherent in natural circulation loops, their intensity depending on heat flux and apparatus geometry, occurred and these are implicit at least in the constant of the correlating equation." @default.
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- W2046543452 date "1973-12-01" @default.
- W2046543452 modified "2023-09-26" @default.
- W2046543452 title "Heat transfer in a natural circulation single tube reboiler" @default.
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- W2046543452 doi "https://doi.org/10.1016/0300-9467(73)85048-8" @default.
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