Review
Optimization of thermal design of heat sinks: A review

https://doi.org/10.1016/j.ijheatmasstransfer.2017.10.099Get rights and content

Highlights

  • Publications in hydrothermal performance of the heat sinks are reviewed.

  • New techniques used for optimizing the thermal design of heat sinks are discussed.

  • The gaps, unsolved problems and uncovered methods are summarized.

  • Limitations in some proposed techniques are explained.

  • Further works and topics are suggested.

Abstract

Heat sinks are a kind of heat exchangers used for cooling the electronic devices due to the simplicity of fabrication, low cost, and reliability of heat dissipation. The extended surfaces from the heat sinks are either flat-plate fins or pins fins shapes. In the last decades, intensive attentions were spent on miniaturizing the electronic devices because of the high sophisticated micro- and nano-technology development. But the heat dissipation is still the major problem of enhancing the thermal performance the heat sink. In this article, a comprehensive review is carried out on the methods used for optimizing the hydrothermal design of heat sinks. Therefore, available investigations regarding the passive and active techniques utilized for enhancing the heat removal from heat sinks by modifying either the solid domain or fluid domain are covered. The purpose of this study is to summarize the investigational efforts spent for developing the thermal performance of the heat sinks, limitations, and unsolved proposed solutions.

Introduction

With the continuous development of electronic devices towards high performance and miniaturization size, heat dissipation problem has become a major obstacle to their development. Besides, the traditional air cooling method has been unable to meet the high-density heat dissipation requirement. Computer users prefer computers that having high-speed processors. The thermal design optimization of the heat sinks leads to minimize the size and weight of the heat sink, and then improve the heat removal in consequently increasing the speed of electronic devices. Electronic devices are increasingly miniaturized and the operating power of CPU increases. Besides, a larger amount of data processed by the CPU at a time causes greater heat generation. This development in the computer manufacturing makes the transfer of generated heat to the ambient becomes more difficult [1]. Generally, the heat generated by the processors is typically transferred to a heat sink (HS) by heat conduction, and then to the ambient by natural, mixed or forced convection. Low efficiency of heat removal of the heat sink possibly causing damage to the electronic component as the temperature rises [2]. This problem has motivated the computer manufacturers to employ sophisticated technology to improve the speed of electronic elements with increasing the heat removal. In contrary, the smallest size of the computers increases the overall flow resistance for the system and eventually suppresses the fluid flow between fins of the heat sink. This significantly influences the fan performance and affects its heat removal capability. Therefore, the heat sink must be designed properly to promote heat transfer and to avoid overheating of the electronic element. The effective thermal management of heat sinks is of priority concern of researchers. It is necessary to be mentioned that the common popular coolant of electronic systems is air due to the ease of obtaining the coolant and the simplicity, high reliability and low cost of the required equipment [3].

With rapid developments in microelectronic techniques, the electronic devices are going to be more miniaturized having high power, high performance, and higher temperature. The traditional heat transfer method of forced air convection is reached to its thermal limit. Therefore, the challenge is how to develop effective methods for cooling high flux devices. Generally, the working limit temperature of electronic devices is ranged from 85 to 100 °C. The literature has shown that the reliability of chip reduces 5% and the life span significantly reduces when the temperature raises every 1 °C above the limit temperature. Therefore, a huge threatens to chip reliability and service lifetime if the high heat generated by the electronic element cannot be removed in time. Thus, it is necessary to investigate and develop an effective cooling technology to meet the demand of high heat generated by electronic components [4]. Due to the development of the micro-technology, highly integrated electronic circuits led to increased heat generation rates in electronic chips. In other words, the speed of chips is increasing, the heat generated by the chip is going up, and the temperature of the chip is rising while the volume of the chip is miniaturized. The average heat flux of the chip was about 50 W/cm2 in 2010 and rose to be around 250 W/cm2 in 2012. Porous metal has been demonstrated that it can enhance the forced convection heat transfer strongly [5], [6]. Heat sink with a porous medium can increase both the surface contact area between the fins and coolant and the local mixing velocity of the coolant, which ensures better heat removal. The thermal performance of a porous heat sink can be enhanced if porosity conditions and the geometric parameters of the channel are properly designed. High-pressure drop is carrying out between the inlet and outlet of a porous microchannel heat sink (MCHS) having low porosity and permeability which needs more pumping power. Therefore, the high-pressure drop associated with using porous medium plays a vital role in the design of a porous MCHS [7], [8].

The advantages of micro-channel compact heat exchangers have gotten plenty of attention of investigators since the last two decades. The ratio between the contact surface area with the refrigerant and the heat exchanger volume increases with decreasing the channel hydraulic diameter. This characteristic permits minimizing the heat exchanger size, low amount of material used in the heat exchanger manufacture, and reducing the refrigerant amount. These aspects not only impact the fabrication cost but also environmental aspects. Flow boiling in mini- and microchannels can be used for cooling many high power density devices such as Micro Electro Mechanical Systems (MEMS), microprocessors, laser diode arrays and Light Emitting Diodes (LEDs) [9]. Flow boiling in microchannels is very effective in the thermal management of high-flux modern electronics. To avoid electric hazards of electronic equipment or integrated circuit component, the dielectric fluids such as fluorocarbon fluids featuring excellent electrical and chemical properties, are the leading candidates for such applications [10].

The past two decades have witnessed intense interest among researchers in the use of MCHS, which has been spurred by such unique attributes as compactness, high power dissipation to volume ratio, and small coolant inventory. Due to their high area-to-volume ratios, the use of MCHS has been introduced, first by Tuckerman and Pease in 1981, as an alternative solution for removing high heat fluxes from small areas. The mode of flow in microchannels mostly remains under laminar flow regime due to the small hydraulic diameter of the microchannel and eventually the pumping power at the micro-scale is still a limiting factor. One of the most common means for cooling electronic modules is a finned heat sink. There are a variety of heat sink types, depending on the fin geometry, configuration and orientation (flat-plate fin, pin fin, interrupting fin, slotted fins, inline or staggered, same or different height and width, etc.).

The lower thermal resistance, uniform temperature distribution, and lower maximum temperature on the base surface, lower pumping power, higher compactness and lower fabrication cost are still the essential requirements in MCHS. In recent years, the single-layered microchannel heat sink (SLMCHS) has been widely used in various electronic devices as a cooling system. With miniaturizing the electronic chips, the optimization of the geometric parameters of SLMCHS is still a hot and attractive research topic to improve the overall performance [11].

The SLMCHS, firstly introduced by Tuckerman and Pease [1] in 1981. The relatively high and non-uniform temperature distribution along the channel is still the disadvantage of SLMCHS. This disadvantage produces thermal stresses in the chips and then reduces the electrical performance and eventually their lifetime. The high pressure drop between the inlet and outlet (due to the small hydraulic diameter of the channel), and the high temperature variation (due to the large amount of heat generated by chips cannot be removed by the relatively small amount of coolant) restrict the SLMCHS to be applied in all engineering applications particularly with the development of microtechnology. However, increasing the coolant flow rate for enhancing the heat removal requires more pumping power which means higher noise associated [12], [13]. Therefore, in 1999, Vafai and Zhu [6] proposed a double-layered microchannel heat sink (DLMCHS) design (top and bottom layers), as an alternative method for reducing the temperature variation along the heat sink. The proposed heat sink provides larger hydraulic diameter can promise more uniform temperature profile on the heated surface compared to the traditional one. Therefore, further studies on the hydrothermal performance of multi-layer MCHS design are necessary.

Section snippets

Optimization of heat sinks in natural convection

Tari and Mehrtash [14], [15] derived a set of correlations of Nu number (Nu) for both upward and downward natural convection from PFHS by using large sets of experimental data from the literature. At small inclinations, it was noted that convection heat transfer rate remained almost the same. Their correlations covered all possible inclination angles with accuracy less than 20%.

Hassan [16] studied the natural convection heat transfer inside a horizontal and vertical enclosure HS having

Optimization of heat sinks in unsteady flow

Xu et al. [20] carried out a CFD and experimental study on heat transfer performance of a symmetrical fractal silicon microchannel network under a pulsation flow. The results illustrated that the heat transfer rate at pulsation frequency (2–10 and 30–40 Hz) increased by 25–40% and it was higher than that for (10–20 Hz) when Re number was kept constant. By increasing Re number, a decrease in the enhancement factors was recorded from 40% to 5% for the above frequency range, unlike the

Optimization of heat sink shape

Costa and Lopes [22] improved the thermal performance of the HS for a light emitting diodes (LED) lamp operating under natural convection conditions as shown in Fig. 3. The effect of the number, thickness, length and height of fins was examined. Their results obtained by using the commercial code ANSYS-CFX illustrated the remarkable importance of the geometric parameters on the heat removal for keeping the heat source maximum temperature maintained below the critical temperature. They reported

Location of inlet and outlet arrangement of heat sink

Hung et al. [8] examined numerically the effect of enlarging the channel outlet (the channel outlet width and height) on the hydrothermal performance of a porous MCHS. Their simulation data indicated that the pressure drop across the MCHS was reduced when the width or height enlargement ratio increased. It was observed that the thermal performance was enhanced and the Rth was reduced with an enlarged channel outlet. Therefore, they stated that the increase of the width or height enlargement

Rotating heat sinks

Yang et al. [42] examined an air jet impingement rotating and stationary HS under turbulent flow regime as illustrated in Fig. 13. They found that Nu number increased with Re number for a stationary heat sink. The effect of Re number on the average Nu number of a rotating HS with jet impingement was higher than that for stationary HS for small Re, but it decreased with increasing Re. They reported that by varying the fins geometry the hydrothermal performance of the HS can be optimized. From

Optimization of the substrate material

Shkarah et al. [43] simulated a set of cases to show the superiority of three types of the substrate; silicon, aluminum, and graphene to provide the better thermal performance of MCHS. They found that graphene effectively reduced the thermal resistance. Mohammed et al. [44] investigated the laminar flow and heat transfer characteristics of trapezoidal MCHS using various types of substrate materials; copper, aluminum, steel, and titanium. Their major findings confirmed that the substrate

Optimization of heat sinks with boiling

Nascimento et al. [10] evaluated experimentally the flow boiling of R134a inside a MCHS. It was noticed that by keeping the average vapor quality over the HS constant, the average heat transfer coefficient increased when the mass velocity increased. The HS performance improved with decreasing the mass velocity and the liquid sub-cooling at the microchannel inlet.

McNeil et al. [9] studied the boiling of deionized water and R113 in a pin-fins HS (in-line arrangement) at atmospheric pressure

Optimization of flat-plate fin heat sink (FPFHS)

Li et al. [2] tested experimentally the effects of the width, height and number of fins on the thermal performance of vapor chamber of FPFHS. The results displayed that the maximum temperature was effectively reduced and heat transfer was more uniformly on the base substrate by using the vapor chamber HS than that by aluminum HS. The overall Rth of their new proposed HS reduced with Re number, but this reduction became small as Re increased. At low Re number, the fin dimensions had a greater

Optimization of pin-fin heat sink (PFHS)

Huang et al. [50] optimized the thermal design of the rectangular PFHS with non-uniform fin widths. They reduced numerically the Rth up to 12.98% compared to the original HS. Besides, Nu number increased by 14.92% compared to the original one. Their experimental results demonstrated that Rth decreased by 12.49% and Nu increased by 14.21% compared to the original fin array. While Huang and Chen [51], [52] optimized the HS design by varying the fin widths and heights. The observed numerically and

Optimization of heat sink by using porous media

Hung et al. [8] concluded that for a certain width or height of channel outlet enlargement ratios, the Rth of a porous MCHS is not necessarily to be less than that of plain MCHS if the pumping power is not large enough to overcome the frictional loss.

Liu et al. [6] investigated a Lotus-type porous copper which is used for cooling of high-power electronic devices numerically and experimentally. Their experimental results illustrated that this type of HS has an excellent heat transfer rate. The

Optimization of heat sinks by using turbulators

Ahmed et al. [67] optimized the thermal design of FPFHS by inserting ribs in between channels in different sizes, locations, numbers and orientations as shown in Fig. 25. They examined the effect of inserting the ribs in the channels by keeping the number of fins constant and reducing them. They reduced the amount of substrate material by reducing the number of fins and adding tiny ribs simultaneously and reduced the pumping power by keeping the number of fins and inserting ribs with reducing

Optimization of the shape of single-channel

Wang et al. [77] studied an inverse geometric optimization for Al2O3-water nanofluid-cooled MCHS. They tested the parameters of the number, aspect ratio (AR), and the width ratio of the channel. They concluded that the cooling performance was enhanced by increasing the pumping power; however, this enhancement was reduced when the pumping power increased highly.

Kim et al. [78] derived correlations for optimal fin thickness and optimal channel width which reduce the Rth for given width, height

Optimization of heat sinks by working fluid

The experiments of Ho et al. [96] on using nanofluids in copper MCHS proved the remarkable increase in the dynamic viscosity due to dispersing the alumina nanoparticles in water base fluid (0–2 vol%), while a slight increase in the friction factor was recorded. Besides, a significant heat transfer enhancement was registered and thereby lower Rth and wall temperature was observed. Continuously, the experiments of Ho and Chen [97] were focused on the effect of alumina oxide-water nanofluid

Optimization of single- and double-layer heat sink

Hung et al. [13] explored numerically the heat transfer characteristics of a DLMCHS as shown in Fig. 37. Their predictions displayed that the substrate materials having a higher thermal conductivity ratio provided the higher thermal performance of the HS. Better heat transfer was observed with a coolant having high thermal conductivity and low dynamic viscosity. They recorded a decrease in the pressure loss when the channel AR and channel width ratio increased. They stated that the Rth of the

Mini-channel heat sink (MiCHS)

Fan et al. [119] examined a novel cylindrical oblique fin MiCHS in order to optimize the thermal performance of the HS for laminar flow regime as shown in Fig. 38. The oblique angle was varied from 20° to 45° with Re number range from 200 to 900. They found that Nu number depended on the geometric parameters of the oblique fins, Re number and Pr number. The secondary flows were strengthened when the length of the secondary channels increased. They monitored a re-developing boundary layer at

Temperature jump

Bushehri et al. [125] explored the effect of temperature jump boundary condition (TJBC) on heat transfer and temperature distribution in FFHS. They proposed a new method for coupling equations between solid and fluid domains with TJBC in the open-source CFD package, Open FOAM. They considered boundary conditions, constant wall temperature and constant heat flux. They observed a significant effect for the temperature jump on temperature field and heat transfer in HS. For uniform heat flux

Conclusion

In the present paper, the techniques which are used for improving the hydrothermal performance of heat sinks are reviewed. The review includes the optimization of the thermal design of the heat sinks by examining the pulsating flow and agitation, shapes and orientations of fins, the inlet/outlet of the heat sinks, static and rotating heat sinks, substrate material of the heat sinks, channel configurations, adding of foams and porous media, using of turbulators, additives to the conventional

Recommendations for future works

A few numbers of investigations published in using active methods for thermal performance augmenting of the heat sinks. Zhang et al. [64] suggested taking the pore length and penetrative porosity into the account during fabricating the lotus-type porous copper HS. Further investigations are needed for enhancing the thermal design of MCHS by using more than two layers. Making grooves in the flat-plate fins or using slotted fins in order to improve the heat transfer, reducing the frictional

Conflict of interest

The authors declared that there is no conflict of interest.

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