Spelling suggestions: "subject:"heat - atransmission."" "subject:"heat - cotransmission.""
161 |
Heat transfer around a bubble in a fluidized bed.Tuot, James. January 1972 (has links)
No description available.
|
162 |
Local heat transfer to spheres in a plasma jet.Katta, Satyanarayana January 1972 (has links)
No description available.
|
163 |
The Effect of free-stream turbulence on heat transfer from cylinders in cross-flow.Mujumdar, A. S. January 1971 (has links)
No description available.
|
164 |
Impingement heat transfer on a rotating cylinder : an experimental study of calender coolingPelletier, Lorraine. January 1984 (has links)
No description available.
|
165 |
Convective and radiative heat transfer of gases flowing in a vertical tube.Biggs, Ronald Clarke. January 1968 (has links)
No description available.
|
166 |
Heat transfer to tubes in the freeboard region of a fluidized bedGeorge, Safa Edward January 1980 (has links)
No description available.
|
167 |
Heat transfer under an impinging slot jetVan Heiningen, Adriaan R.P. January 1982 (has links)
No description available.
|
168 |
Immersed surface heat transfer in a vibrated fluidized bedMalhotra, Karun. January 1984 (has links)
No description available.
|
169 |
Convective Heat Transfer from a Cylinder Rotating in AirPasamehmetoglu, O. Kemal 01 April 1983 (has links) (PDF)
This study had a two-fold purpose. The initial emphasis was placed upon the analysis of heat transfer to ambient air from a rotating cylinder. Three distinct heat transfer regimes can be identified. For low rotational speeds corresponding to a Reynolds number less than the critical value for initiation of turbulence, the flow is laminar and the rotation has no effect on the average heat transfer coefficient. In the transition region, the heat transfer coefficient depends upon both natural convection and rotational effects. For higher rotational velocities, the flow is fully turbulent and rotational effects dominate. Previous analytical and experimental studies have been conducted for all three regions. These studies are summarized in this thesis and it is seen that there are gaps and limitations in the existing state of knowledge. Therefore, further study is required especially for high rotational speeds. In the second phase of study, an experimental program was designed to determine heat transfer coefficients at various rotational speeds and heat transfer rates. The rotating cylinder is designed in such a way that it can be inclined by 30┬░, 45┬░, 60┬░, or 90┬░ with horizontal. High rotational speeds are possible yielding Reynolds numbers of 2 x 105. The maximum power is approximately 400 W.
|
170 |
Transient critical heat fluxPasamehmetoglu, Kemal O. 01 January 1986 (has links) (PDF)
The term Critical Heat Flux (CHF) is used in boiling heat transfer to describe the local value of the heat flux at which a characteristic reduction in heat transfer coefficient first occurs. In today’s technology, the CHF is a phenomenon related to the design and safety of various important devices.
A major limitation on the thermal design of a light-water reactor (LWR) is the necessity to maintain an adequate safety margin between the CHF and the local heat flux. Extended operations at local power levels in excess of the CHF can lead to high temperature oxidation and embrittlement or melting of the zircaloy cladding, thus jeopardizing the fuel rod’s integrity. In the nuclear industry, there have been many empirical CHF correlations developed over the years. These correlations are mostly based on steady-state (or quasi-steady) data obtained from various experiments covering different ranges of CHF parameters. Therefore, the application of such correlations is not only restricted by their parametric ranges, but is also limited to steady (or quasi-steady) operating conditions. In nuclear reactors, however, the CHF level is more likely to be reached during abnormal (transient) operating conditions, rather than during normal (steady) operations. Depending upon the type of accident, a wide range of thermal-hydraulic conditions may arise. For accurate nuclear reactor modeling, the accurate prediction of CHF as a function of time-dependent, thermal-hydraulic conditions is essential. This was the motivation of the subject study.
This research was a two-fold study. In the first part, the quasi-steady approach in predicting the CHF is defined and analyzed. In this part, data from blowdown experiments are compared to commonly used steady-state correlations on a local-instantaneous basis. This is done as a continuation of the previous studies conducted at Argonne National Laboratory. In all these studies, including the present study, a simple computer program Coolant Dynamic Analysis (CODA), is used. The results are discussed in terms of the limitations of the quasi-steady approach.
In the second part of this study, faster transients, where the quasi-steady approach is unable to predict the CHF, are considered. A new theory is developed to predict the CHF in power transients, which are typical of Reactivity Initiated Accidents (RIA) in LWRs. The proposed theory is purely analytical. It incorporates the effect of the hydrodynamic instability on the surface dryout in addition to evaporation, which was studied as the unique mechanism by previous researchers. The presented theory compares quite favorable with the available data from electrical heaters.
Two other types of transients which are of interest to the nuclear industry are rapid flow reduction. These are typical of Loss-of-Coolant Accidents (LOCA) and Loss-of-Flow Accidents (LOFA). The effects of these transients on CHF are also discussed from first principles. Finally, the important parameters of a generalized transient CHF correlation are identified and are grouped into dimensionless numbers. The physical significance of each group is discussed. Based on experimental and theoretical observations, a general mathematical model is developed to correlate transient CHF.
|
Page generated in 0.0739 seconds