scholarly journals Measurements of Heat Transfer Characteristics of Gap Leakage Around a Misaligned Component Interface

Author(s):  
M. K. Chyu ◽  
Y. C. Hsing ◽  
R. S. Bunker

In an attempt to understand the effects of leakage through a component-to-component interface on the turbine end wall heat transfer, this paper describes an experimental efforts on examining the detailed heat transfer characteristics near a leaking gap. Geometric misalignment around the gap is modeled by either a forward-facing step or a backward-facing step. Heat transfer measurement here uses a temperature-sensitive fluorescent imaging of a thermographic phosphor (TGP). The TGP technique reveals detailed distribution of local heat transfer coefficient and adiabatic wall temperature in the vicinity of the leakage. The results suggest that, for a given leakage-to-mainstream mass flow ratio, the adiabatic wall temperature closes to the level of leakage temperature and is relatively insensitive to the nature of misalignment. On the outer hand, however, the value of heat transfer coefficient varies strongly with misalignment and streamwise location relative to the gap. Overall, the leakage thickens the approaching boundary layer and significantly extends the length of reattachment downstream compared to the corresponding cases without leakage. To further qualify the TGP technique, which is relatively new for transient measurement of local heat transfer, an analysis toward its efficacy in resolving complex convective system is developed in this study. One of the main advantages that TGP inherits is its capability of determining both heat transfer coefficient and reference temperature based on a single test. Other methods, such as the transient liquid crystal technique, generally require separate tests each with different thermal conditions.

Author(s):  
Kenneth W. Van Treuren ◽  
Zuolan Wang ◽  
Peter T. Ireland ◽  
Terry V. Jones

A transient method of measuring the local heat transfer under an array of impinging jets has been developed. The use of a temperature sensitive coating consisting of three encapsulated thermochromic liquid crystal materials has allowed the calculation of both the local adiabatic wall temperature and the local heat transfer coefficient over the complete surface of the target plate. The influence of the temperature of the plate through which the impingement gas flows on the target plate heat transfer has been quantified. Results are presented for a single inline array configuration over a range of jet Reynolds numbers.


1994 ◽  
Vol 116 (3) ◽  
pp. 369-374 ◽  
Author(s):  
K. W. Van Treuren ◽  
Z. Wang ◽  
P. T. Ireland ◽  
T. V. Jones

A transient method of measuring the local heat transfer under an array of impinging jets has been developed. The use of a temperature-sensitive coating consisting of three encapsulated thermochromic liquid crystal materials has allowed the calculation of both the local adiabatic wall temperature and the local heat transfer coefficient over the complete surface of the target plate. The influence of the temperature of the plate through which the impingement gas flows on the target plate heat transfer has been quantified. Results are presented for a single in-line array configuration over a range of jet Reynolds numbers.


1998 ◽  
Vol 120 (2) ◽  
pp. 348-356 ◽  
Author(s):  
V. Narayanan ◽  
J. Seyed-Yagoobi ◽  
R. H. Page

A two-dimensional reattachment nozzle called the Slot Jet Reattachment (SJR) nozzle was designed and built with a zero degree exit angle. The heat transfer characteristics of this submerged nozzle were investigated by varying the Reynolds number, nozzle exit opening, and nozzle to surface spacing. The pressure distribution on the impingement surface for different Reynolds numbers and exit openings were measured. Correlations for location of the maximum local Nusselt number and local Nusselt number distribution along the minor axis of the SJR nozzle were determined. A nondimensional scheme for generalized representation of heat transfer data for two-dimensional separated/reattaching flows was developed. The local and average heat transfer characteristics along the minor axis of the SJR nozzle were compared to a conventional slot jet nozzle under identical flow power condition. The comparison showed that the peak local heat transfer coefficient for the SJR nozzle was 9 percent higher than that for a standard slot jet nozzle, while its average heat transfer coefficient was lower or at best comparable to the slot jet nozzle based on the same averaged area. The net force exerted per unit width by the SJR nozzle flow was 13 times lower than the slot jet nozzle flow under this criterion. Additional experiments were conducted to compare the SJR and slot jet nozzles under matching local peak pressures exerted by the jet flow on the impingement surface. The results indicated 52 percent increase in the peak local heat transfer coefficient, and a maximum enhancement of 35 percent in average heat transfer coefficient for the SJR nozzle over the slot jet nozzle based on the same averaged area under this criterion.


Author(s):  
Jingzhi Zhang ◽  
Naixiang Zhou ◽  
Jinpin Lin ◽  
Han Lin ◽  
Wei Li

Heat transfer characteristics of aviation kerosene were investigated numerically using a three-dimensional model. The influence of the ratio of longer axis to short axis of elliptical tubes (r), inlet Reynolds number (Re), and pressure (P) of kerosene on local heat transfer characteristics were discussed in detail. The results indicate that the heat transfer coefficient (h), wall temperature (Tw), and bulk fluid temperature (Tb) increase along Z axis direction from inlet to outlet when P=4Mpa. h increases with increasing r and Re, while Tw decreases with increasing Re and r. Tb decreases with increasing Re and remains stable for a varying r. For P=3Mpa, the deterioration of heat transfer occurs near the outlet of computational geometry, where the temperature of near wall region fluid exceeds the critical point and specific heat decrease dramatically. A correlation for heat transfer coefficient of aviation kerosene at supercritical pressure inside elliptical tubes is proposed and compared with the present simulation data. It is shown that this correlation can predict the simulation data within an ±15% error band. Compared with circular tubes, elliptical tubes can enhance the heat transfer effect and decrease the wall temperature, thus enhance the security of the operating system.


2019 ◽  
Vol 27 (03) ◽  
pp. 1950024
Author(s):  
Zahraa Kareem Yasser ◽  
Ahmed J. Hamad

The heat transfer characteristics of R134a flow boiling in a horizontal tube of an evaporator section for a refrigeration system of 310-W capacity are investigated experimentally and numerically. The experimental work was conducted using an evaporator tube test section of inner diameter 5.8[Formula: see text]mm and length 600[Formula: see text]mm. The ranges of investigated experimental data for heat flux, mass flux, saturation temperature and vapor quality were 13.8–36.6[Formula: see text]kW/m2, 52–105[Formula: see text]kg/m2[Formula: see text][Formula: see text][Formula: see text]s, [Formula: see text]–[Formula: see text]C and 0.2–1, respectively. Numerical analysis was based on two-phase flow turbulent model and this model was solved using the Ansys-18 code. The results showed that the effects of heat flux, mass velocity and saturation temperature on local heat transfer coefficient and pressure drop were greater compared to that of the refrigerant vapor quality. The enhancements in local heat transfer coefficient due to the increase in heat flux, mass and saturation temperature were 38%, 57% and 64%, respectively, within the prescribed test conditions. The influence of mass flux variation on pressure drop along the evaporator channel was higher in the range of 27% compared to the heat flux effect. The average deviations between experimental and numerical results of heat transfer coefficient and pressure gradient were 14% and 17%, respectively, while the same between the experimental and predicted results were 16% and 33%, respectively.


2021 ◽  
Vol 11 (2) ◽  
pp. 751
Author(s):  
Xuefeng Gao ◽  
Yanjun Zhang ◽  
Zhongjun Hu ◽  
Yibin Huang

As fluid passes through the fracture of an enhanced geothermal system, the flow direction exhibits distinct angular relationships with the geometric profile of the rough fracture. This will inevitably affect the heat transfer characteristics in the fracture. Therefore, we established a hydro-thermal coupling model to study the influence of the fluid flow direction on the heat transfer characteristics of granite single fractures and the accuracy of the numerical model was verified by experiments. Results demonstrate a strong correlation between the distribution of the local heat transfer coefficient and the fracture morphology. A change in the flow direction is likely to alter the transfer coefficient value and does not affect the distribution characteristics along the flow path. Increasing injection flow rate has an enhanced effect. Although the heat transfer capacity in the fractured increases with the flow rate, a sharp decline in the heat extraction rate and the total heat transfer coefficient is also observed. Furthermore, the model with the smooth fracture surface in the flow direction exhibits a higher heat transfer capacity compared to that of the fracture model with varying roughness. This is attributed to the presence of fluid deflection and dominant channels.


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