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HEAT TRANSFER ANALYSES

Dimensionless Mumbers used in Convection Heat-Transfer Analysis. [Pg.483]

Gliick B. Room model for heat transfer analysis (in German Wdrmctechnisches Raummodeli]. Heidelberg C. F. Muller V erlag, 1997. [Pg.1082]

We defer to Chapter 5 (and Appendix A) a description of how the required cooling fraction i// (and the heat transferred) can be obtained from heat transfer analysis, following the work of Holland and Thake [12. ... [Pg.60]

But it app>ears that thermal efficiency does tend towards a maximum level with increasing combustion temperature. More realistic calculations of highly cooled turbines are given in the next chapter, after a brief description of the heat transfer analysis involved in the determination of cooling flow quantities. [Pg.68]

In Chapter 4 calculations were made on the overall efficiency of CBT plants with turbine cooling, the fraction of cooling air (tp) being assumed arbitrarily. In this chapter, we outline more realistic calculations, with the cooling air fraction i/r being estimated from heat transfer analysis and experiments. [Pg.71]

Gilmour, C. H., Performance of Vaporizers, Heat Transfer Analysis of Plant Data presented at Second National Heat Transfer Conference, Aug. 1958, Chicago, IL. Preprint No. 33, AIChE, New York 36, N.Y, pub. Chem Eng. Prog, Sym. Series No. 29, V. 55 (1959). [Pg.280]

Brutin B, Tadrist L (2004) Pressure drop and heat transfer analysis of flow boUing in micro-channel influence of the inlet condition on two-phase flow stability. Int J Heat Mass Transfer 47 2367-2377... [Pg.320]

The calculations for the experimental reaction rates are based on an unsteady state heat transfer analysis. We computed the overall heat transfer coefficient of the system and estimated the experimental rates as follows dT... [Pg.353]

Adams, J. A. and Rogers, D. F. (1973) Computer-Aided Heat Transfer Analysis. McGraw-Hill. [Pg.273]

Zalba B., J.M. Mann, L.F. Cabeza, and H. Mehling, 2003. Review on thermal energy storage with phase change Materials, heat transfer analysis and apphcations, Appl. Thermal Eng., 23, 251-283. [Pg.277]

From that same section, we know that the steady state gain and the time constant are dependent on the values of flow rate, liquid density, heat capacity, heat transfer coefficient, and so on. For the sake of illustration, we are skipping the heat transfer analysis. Let s presume that we have done our homework, substituted in numerical values, and we found Kp = 0.85 °C/°C, and xp = 20 min. [Pg.91]

The second term on the right-hand side of Eq. (3-95) represents the effect of the wall-drop heat transfer. The heat transfer analysis of dispersed-flow film boiling is discussed in Section 4.4.3. [Pg.212]

Rod bundle heat transfer analysis (Anklam, 1981a) A 64-rod bundle was used with an axially and radially uniform power profile. Bundle dimensions are typical of a 17 X 17 fuel assembly in a PWR. Experiments were carried out in a steady-state mode with the inlet flow equal to the steaming rate. Generally, about 20-30% of the heated bundle was uncovered. Data were taken during periods of time when the two-phase mixture level was stationary and with parameters in the following ranges ... [Pg.325]

Anklam, T. M., 1981a, ORNL Small-Break LOCA Heat Transfer Test Series 1 Rod Bundle Heat Transfer Analysis, NUREG/CR 2052, ORNL/NUREG/TM-445, Oak Ridge Natl. Lab., Oak Ridge, TN. (4)... [Pg.520]

Convection heat transfer, 13 245-248 correlations for, 13 247-248 Convection heat-transfer analysis, dimensionless numbers used in,... [Pg.215]

Dimensionless numbers in mixing, 16 685 used in convection heat-transfer analysis, 73 246-247 Dimensionless parameter, external mass transfer resistance and, 25 290-292 Dimensionless reactor design formulation, 21 350... [Pg.272]

GlLMOUR, C. H. Chem. Eng. Prog. Symp. Ser. No. 29, 55 (1959) 67-78. Performance of vaporizers Heat transfer analysis of plant data. [Pg.823]

The first part of the analysis is focused on the energy transfer to the solid bed and what assumptions might be reasonable regarding the temperature profile in the solid bed. For this analysis the barrel and solid interface will be addressed. It is desired that an infinite bed assumption can be justified. Once this assumption is justified, the heat transfer analysis for the melting is quite straightforward. [Pg.722]

In Chapter 3, the reactor models have been presented along with the hydraulic and mass/heat transfer analysis. In the following sections, the solutions of the reactor models are presented along with several examples. [Pg.384]

Heat-Transfer Analysis Thermal-Capillary Models. Numerous analyses of various aspects of heat transfer in the CZ system have been reported many of these are cited by either Kobayashi (143) or Derby and Brown (144). The analyses vary in complexity and purpose, from the simple one-dimensional or fin approximations designed to give order-of-magni-tude estimates for the axial temperature gradient in the crystal (98) to complex system-oriented calculations designed to optimize heater design and power requirements (145,146). The system-oriented, large-scale calculations include radiation between components of the heater and the crucible assemblies, as well as conduction and convection. [Pg.95]

Billig (98) realized this point and used a one-dimensional heat-transfer analysis for the crystal with assumptions about the temperature field in the melt to derive the the following relationship that has been used heavily in qualitative discussions of crystal growth dynamics ... [Pg.96]

SiH4 — epitaxial Si 225 Two-dimensional, axisymmetric flow and heat transfer analysis of detailed chemistry model with 17 species and 27 elementary reactions combined with similarity solution for flow problem. [Pg.252]

Ga(CH3)3 + AsH3 —> GaAs 195, 198 Two-dimensional, axisymmetric flow, mass- and heat-transfer analysis, reactor geometry effects, flow transitions, and mass-transport-limited growth. [Pg.252]

Murthy S., Fedorov G, 2003. Radiation heat transfer analysis of the monolith type solid oxide fuel cell. Journal of Power Sources 124(2), 453—458. [Pg.92]

Damm D.L. and Fedorov A.G., 2004. Spectral radiative heat transfer analysis of the planar SOFC. In Proceedings of the ASMEIMECE, Anaheim, CA, November 13-19, 2004. Paper No. IMECE2004-60142. [Pg.121]

M 4] [P 3] Temperature differences of 5-10 °C result by the action of the AC field owing to Joule heating for the 3 s duration of the pulse [25], The data were gathered from both thermocouple measurements and capacitance-based heat transfer analysis. [Pg.22]

E. Mitsoulis and J. Vlachopoulos, The Finite Element Method for Flow and Heat Transfer Analysis, Adv. Polym. Technol., 4, 107-121 (1984). [Pg.818]

Lee, )-)., et al. (2007), Numerical Treatment of Pebble Contact in the Flow and Heat Transfer Analysis of a Pebble Bed Reactor Core , Nucl. Eng. and Design, 237, 2183-2196. [Pg.65]

Russell, Robinson and Wagner, Mass and Heat Transfer Analysis of Mass Contactors and Heat Exchangers Slattery, Advanced Transport Phenomena... [Pg.261]

The medium in between does not participate in the heat transfer. Analysis ... [Pg.24]


See other pages where HEAT TRANSFER ANALYSES is mentioned: [Pg.59]    [Pg.62]    [Pg.65]    [Pg.295]    [Pg.341]    [Pg.215]    [Pg.234]    [Pg.121]    [Pg.240]    [Pg.253]    [Pg.2]    [Pg.4]    [Pg.6]    [Pg.8]    [Pg.10]    [Pg.12]   


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