Heat Transfer Enhancement Using Miniaturized Channel Sections With Surface Modifications

2016 ◽  
Author(s):  
Mohammed S. Mayeed ◽  
Soumya S. Patnaik ◽  
Ricky Mitchell

The objective of this study is to enhance heat transfer process using micro/nano scale channels with surface modifications. An application focus of this study is to design an extremely compact heat-exchanger using single/multi component fluid in miniaturized channels along with surface modifications to achieve higher heat exchange per unit surface area. For the last couple of decades significant progress has been made in characterizing flows in micro channels because of its high surface to volume ratio enhancing heat transfer process. However a centerline question still remains — what should be an optimized size of a miniaturized channel to achieve maximum heat transfer? A lack of theoretical characterization of single or multi component flows in micro to nano scale channels is partially responsible for this setback. Lattice Boltzmann (LB) method, a mesoscopic thermo fluid flow modeling technique, has grown significantly over the last couple of years mainly because of the promise of incorporating mesoscale molecular interaction and also the ability to solve Navier-Stokes equation at the hydrodynamic limit. Moreover, LB method which is based on microscopic models and mesoscopic equations, is considered an attractive numerical alternative for solving multiphase phenomena in a multiscale setup. Also fluid-solid interactions can be implemented conveniently in the LB method without introducing additional complex kernels. At first to address thermo-fluid phenomena over a heated surface Rayleigh-Benard (RB) convection was modeled, and to observe forced flow cavity flow was simulated based on LB method. Some of these results had been compared with literature and documented to have good comparison which showed verification of the current in-house LB simulation codes. After this, effects of surface interaction (hydrophobic and hydrophilic) and miniature cross sections (micro-scale) were calculated using single-component RB convection model. Several results were generated e.g. effects of surface interaction and Knudsen number (Kn) on the average Nusselt number (Nu) in a Rayleigh Benard (RB) convection with hot bottom and cold top surfaces. Results showed higher average heat transfer (Nu) when the bottom surface is hydrophobic and top surface is hydrophilic compared to neutral surface condition in a typical single component RB convection flow over a range of Rayleigh numbers (Ra). Knudsen number (Kn) effect was incorporated to observe the effect of miniature cross section. The average Nu decreased with the increase of Kn i.e. the miniaturization of the channel section from macro-scale to micro-scale also over a range of Rayleigh numbers. However, the number of micro-channels that could be placed in the cross section of a macro-channel increased considerably with increasing Kn. Effect of Kn on the velocity profiles, slip velocities, and maximum velocities were also calculated in a flow between parallel plates. Maximum velocities decreased and slip velocities increased with increasing Kn. Many of these results are in good qualitative comparison with results in literature.

2020 ◽  
Vol 42 (1) ◽  
pp. 12-18
Author(s):  
A.A. Avramenko ◽  
N.P. Dmitrenko ◽  
Yu.Yu. Kovetska ◽  
E.A. Kondratieva

A steady heat transfer process of mixed convection in a flat vertical porous microchannel is considered. The results of simulation showed that Knudsen number effects are more significant in the neighborhood of the wall where growth of Knudsen numbers is accompanied with the velocity and temperature jumps on wall. With increasing parameter of porosity M (decreasing permeability), the flow velocity decreases and the velocity jump decrease as well. For all combinations of the criteria Ra, Kn and M increasing Knudsen number reduces heat transfer intensity. This can be attributed to increasing temperature jump on wall which causes deterioration of thermal interaction between the fluid and the wall. For low Rayleigh numbers increasing parameter M leads to increasing heat transfer since the temperature jump decrease on walls. For large Rayleigh numbers the trend becomes reversed, since for larger parameters M, the near-wall velocity decreases. For low Rayleigh numbers increasing the Knudsen number leads to decreasing hydraulic resistance coefficient, but with increasing parameter M leads to increasing this coefficient. At high Ra numbers increasing Knudsen number leads to growth of hydraulic resistance, which is due to increasing velocity gradient on the wall.


2020 ◽  
Vol 786 (11) ◽  
pp. 30-34
Author(s):  
A.M. IBRAGIMOV ◽  
◽  
L.Yu. GNEDINA ◽  

This work is part of a series of articles under the general title The structural design of the blast furnace wall from efficient materials [1–3]. In part 1, Problem statement and calculation prerequisites, typical multilayer enclosing structures of a blast furnace are considered. The layers that make up these structures are described. The main attention is paid to the lining layer. The process of iron smelting and temperature conditions in the characteristic layers of the internal environment of the furnace is briefly described. Based on the theory of A.V. Lykov, the initial equations describing the interrelated transfer of heat and mass in a solid are analyzed in relation to the task – an adequate description of the processes for the purpose of further rational design of the multilayer enclosing structure of the blast furnace. A priori the enclosing structure is considered from a mathematical point of view as the unlimited plate. In part 2, Solving boundary value problems of heat transfer, boundary value problems of heat transfer in individual layers of a structure with different boundary conditions are considered, their solutions, which are basic when developing a mathematical model of a non-stationary heat transfer process in a multi-layer enclosing structure, are given. Part 3 presents a mathematical model of the heat transfer process in the enclosing structure and an algorithm for its implementation. The proposed mathematical model makes it possible to solve a large number of problems. Part 4 presents a number of examples of calculating the heat transfer process in a multilayer blast furnace enclosing structure. The results obtained correlate with the results obtained by other authors, this makes it possible to conclude that the new mathematical model is suitable for solving the problem of rational design of the enclosing structure, as well as to simulate situations that occur at any time interval of operation of the blast furnace enclosure.


2003 ◽  
Author(s):  
B. X. Wang ◽  
H. Li ◽  
X. F. Peng ◽  
L. X. Yang

The development of a numerical model for analyzing the effect of the nano-particles’ Brownian motion on the heat transfer is described. By using the Maxwell velocity distribution relations to calculate the most possible velocity of fluid molecules at certain temperature gradient location around the nano-particle, the interaction between fluid molecules and one single nano-particle is analyzed and calculated. Based on this, a syntonic system is proposed and the coupled effect that Brownian motion of nano-particles has on fluid molecules is simulated. This is used to formulate a reasonable analytic method, facilitating laboratory study. The results provide the essential features of the heat transfer process, contributed by micro-convection to be considered.


2011 ◽  
Vol 393-395 ◽  
pp. 412-415
Author(s):  
Jian Hua Zhong ◽  
Li Ming Jiang ◽  
Kai Feng

In this article, finned copper tube used in the central air conditioning was acted as the discussed object. According to the combination with actual processing and theoretical calculations, Five finned tube was selected with typical structural parameters, and established their entity model using Pro/E, then the heat transfer process of finned tube was simulated through the ANSYS, the effect of the fin height, fin thickness and other structure parameters to the heat transfer enhancement of finned tube was researched. Meantime the efficiency of the heat transfer under different convection heat transfer coefficient was also studied.


2011 ◽  
Vol 228-229 ◽  
pp. 676-680 ◽  
Author(s):  
Ye Tian ◽  
Xun Liang Liu ◽  
Zhi Wen

A three-dimensional mathematic model is developed for a 100kw single-end recuperative radiant tube and the simulation is performed with the CFD software FLUENT. Also it is used to investigate the effect of distance between combustion chamber exit and inner tube on heat transfer process. The results suggest that the peak value of combustion flame temperature drops along with the increasing of distance, which leads to low NOX discharging. Also radiant tube surface bulk temperature decreases, which causes radiant tube heating performance losses.


Author(s):  
Weigang Ma ◽  
Haidong Wang ◽  
Xing Zhang ◽  
Wei Wang

How the energy transfers during electron-phonon nonequilibrium in thin metal films is still an open question, and how to measure the intrinsic thermal transport properties of the material under the covering layer is another challenge. In this paper, the heat transfer process from electron-phonon nonequilibrium in thin gold film to borosilicate glass substrate has been studied by resorting to different segments of the transient thermoreflectance signal, which is obtained from the rear-pump front-probe transient thermoreflectance technique. The gold film, which has a thickness of 23.1 nm, is deposited on the borosilicate glass substrate using using a physical vapor deposition (PVD) approach. Within the framework of the two-temperature model (TTM), the electron-phonon (e-ph) coupling factors of the gold film, which reflect the strength of heat flow from hot electrons to cold phonons, are derived from the signal taken after the first several picoseconds with different pump fluences, and the measured value is (1.95–2.05)×1016 W m−3 K−1. The electron-phonon coupling factor does not significantly change in response to the pump pulse fluence variation and exhibits little change compared to the bulk gold value 2.4×1016 W m−3 K−1. Furthermore, the thermal conductivity of the glass substrate is obtained through the thermoreflectance signal between 20 to 140 picoseconds and the value is W m−1 K−1.


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