Advances in Cryogenic Engineering 1995
DOI: 10.1007/978-1-4757-0513-3_27
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Survey of Heat Transfer to Near-Critical Fluids

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Cited by 14 publications
(15 citation statements)
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“…Data in region 1 were correlated based on the expression of Nu cRe a Pr b / f = / w d , which has been used in many previous studies [8,[13][14][15][16][17]. In this expression, the power in the Reynolds number represents the effect of the flowfield on heat convection, whereas the power in the Prandtl number denotes the effect of fuel properties.…”
Section: Heat Transfer Correlationsmentioning
confidence: 99%
See 1 more Smart Citation
“…Data in region 1 were correlated based on the expression of Nu cRe a Pr b / f = / w d , which has been used in many previous studies [8,[13][14][15][16][17]. In this expression, the power in the Reynolds number represents the effect of the flowfield on heat convection, whereas the power in the Prandtl number denotes the effect of fuel properties.…”
Section: Heat Transfer Correlationsmentioning
confidence: 99%
“…It is known [6,7] that supercritical fuel exhibits a liquidlike density and a gaslike diffusivity. In addition, the variations of many of the fuel thermodynamic and transport properties, such as density, specific heats, viscosity, and thermal conductivity, with temperature are complex, depending on the thermophysical conditions [8,9]. Taking China no.…”
Section: Introductionmentioning
confidence: 99%
“…It has been known that the working pressure of fuel is usually higher than its critical value (P c ) and along the cooling path, fuel temperature would increase and exceed its critical temperature (T c ) so that hydrocarbon fuel becomes supercritical without going through a two-phase dome region. Compared to gaseous or liquid state, supercritical fluid presents many of unique features [3][4][5]. It has gas-like transport property, relatively large density similar to liquid and very high solubility.…”
Section: Introductionmentioning
confidence: 99%
“…The ordinary Dittus-Boelter equation (Equation 4.16) cannot be used to correlate near-critical forced convection phenomena. Correlations for free convection are not consistent with pool boiling data, standard boiling equations exhibit discontinuities, and oscillations are commonplace [1] (see Section 4.3).…”
Section: Convective Heat Transfer In Tubes Laminar Flowmentioning
confidence: 82%
“…The discussion of heat transfer is divided into four parts: gas and part of the compressible liquid (Region I), liquid (Region II), the two-phase region (Region III), and the near-critical region (Region IV) [1]. The regions are illustrated in Figure 4.1.…”
Section: Overview On Heat Transfer Regionsmentioning
confidence: 99%