Jing Wang,
Haihong Ma,
Fengmei Ren,
Zhengfa Zhou* and
Weibing Xu
School of Chemistry and Chemical Engineering, Hefei University of Technology, Hefei, 230009, People's Republic of China. E-mail: zhengfazhou@hfut.edu.cn; Tel: +86-551-62901455
First published on 30th March 2022
Heat dissipation has become a key problem for highly integrated and miniaturized electronic components. High thermal conductivity, good flowability and low coefficient of linear thermal expansion (CLTE) are indispensable performance parameters in the field of electronic potting composite materials. In this study, spherical alumina (Al2O3) was surface modified by γ-(2,3-epoxypropoxy) propyltrimethoxy silane (KH560) and γ-aminopropyltriethoxy silane (KH550) and labelled as Al2O3-epoxy and Al2O3–NH2, respectively. Al2O3-epoxy and Al2O3–NH2 powders were equally filled in vinyl silicone oil to prepare a high Al2O3 loading (89 wt%) precursor of silicone potting adhesive. The viscosity of the precursor rapidly decreased with increasing reaction time of Al2O3-epoxy and Al2O3–NH2 at 140 °C. The viscosity reduction mechanism may be due to the formation of some Al2O3 clusters by the reaction of Al2O3-epoxy with Al2O3–NH2, which results in some vinyl silicone oil segments being held in the channel of particles through capillary phenomenon, leading to the friction among Al2O3 clusters decreasing considerably. Laser particle size analysis and scanning electron microscopy (SEM) results confirmed the existence of Al2O3 clusters. Energy dispersive spectroscopy (EDS) and dynamic viscoelasticity experiments revealed that some segments of vinyl silicone oils were held by Al2O3 clusters. When Al2O3-epoxy and Al2O3–NH2 reacted for 4 h, the thermal conductivity, CLTE and volume electrical resistivity of the silicone potting adhesive reached 2.73 W m−1 k−1, 75.8 ppm/°C and 4.6 × 1013 Ω cm, respectively. A new strategy for preparing electronic potting materials with high thermal conductivity, good flowability and low CLTE is presented.
In recent years, electronic devices are developing towards high integration and miniaturization. The heat generated by devices needs to be diffused in time to improve the operation reliability and service life of devices.9,10 The thermal conductivity of silicone is low (∼0.2 W m−1 k−1),11,12 which cannot meet the working requirements of potting materials. Thermally conductive but insulating fillers such as boron nitride (BN),13,14 Al2O3,15 aluminum nitride (AlN),16 and silicon carbide (SiC)17 are often filled to improve the thermal conductivity of silicone potting adhesive. However, the thermal conductivity of polymer-based composites with fillers is relatively low. Preparation of 3D fillers, filler assembling and orientation can effectively improve the thermal conductivity of polymer composites.18–21 Li et al.22 used the ice template method to assemble BN nanosheets (BNNSs) and silver nanowires (AgNWs), and the thermal conductivity of the composites reached 1.10 W m−1 k−1 when the filler addition was only 5.0 vol%. Yang et al.23 prepared a thermally conductive filler with BN bridging carbon fiber (CF), and a special three-dimensional oriented BN/CF/EP composite material was obtained by the vacuum impregnation method, improving the thermal conductivity to 3.1 W m−1 k−1. Song et al.24 prepared 3D-Al2O3/silicone rubber (SR) frame by a foaming and vacuum infiltration process, and the thermal conductivity of the composite reached 0.747 W m−1 k−1 when the loading amount of Al2O3 was 32.6 wt%. Liu et al.25 obtained 35 wt% BN/30 wt% Al2O3/polydimethylsiloxane (PDMS) composite materials through a 3-D printing assisted orientation technology, in which the orientation rate and thermal conductivity reached 90.65% and 3.64 W m−1 k−1, respectively. The CLTE of silicone is usually higher than 200 ppm/°C.26 Although 3D fillers, filler orientation and self-assembling can improve the thermal conductivity of silicone composites to a certain extent, the CLTE of these composites are often too large to satisfy the potting requirements of specific electronic devices. Thermally conductive but insulating fillers such as Al2O3 have low CLTE (∼6.6 ppm/°C),27 which can meet the performance requirements of high thermal conductivity and low CLTE of silicone potting adhesive under the condition of large amount of filling. For example, Fu et al.28 prepared a series of dense boric acid modified BNNSs/EP composites by mechanical ball milling and pressure forming processes; the EP composites with 90 wt% BNNSs achieved the maximum thermal conductivity (6.7 W m−1 k−1) and the minimum CLTE (4.5 ppm/°C) at a temperature of 25 °C. Unfortunately, high filler loading will inevitably cause a sharp increase in the viscosity of silicone potting adhesive, which makes it impossible to achieve potting under mechanical or artificial conditions.29
In this study, Al2O3-epoxy and Al2O3–NH2 powders were equally filled in vinyl silicone oil to prepare a high Al2O3 loading (89 wt%) precursor of silicone potting adhesive. The viscosity of the precursor was greatly reduced through the reaction of Al2O3-epoxy and Al2O3–NH2 powders, and a mechanism of viscosity reduction was proposed. The experimental results of laser particle size analysis, SEM, EDS, and dynamic viscoelasticity analysis supported the proposed viscosity reducing mechanism. This study presents a new strategy for preparing electronic potting materials with high thermal conductivity, low viscosity and low CLTE.
Thermogravimetric analysis (TG) was carried out on a TGA8000 analyzer (PerkinElmer, USA) at a heating rate of 10 °C min−1 under a nitrogen atmosphere from 25 °C to 700 °C.
Shear viscosity was obtained using the NDJ-97 type rotary viscometer (Shanghai Changji, China) at 25 °C. The experiment was repeated three times.
Mastersizer 2000 laser particle size analyzer (Malvern Instruments, UK) was used to detect the particle size distribution. 10 g precursor was added in 100 mL toluene under stirring for 10 min, and allowed to settle naturally; the sediments were then collected. This operation was repeated three times to obtain particle sediments. The particle sediments were dispersed in absolute ethanol for testing, and the concentration of the sediments was 0.09%.
Dynamic viscoelasticity analysis of the precursor was performed using small amplitude oscillatory shear (SAOS) at 25 °C, on a Malvern Rheometer (HRnano 200, UK) equipped with cone-and-plate fixture. The diameter of the cone-and-plate was 20 mm, the inclination angle was 2°, and the fixed strain was 1%. Pre-shearing was performed before each dynamic viscoelasticity experiment to eliminate the shear history of the samples.
Gemini 500 field emission scanning electron microscope (Carl Zeiss, German) was utilized to observe the morphology of Al2O3 clusters. The washing operation of the precursor was the same as the laser particle size analysis, where the sediments were fully dispersed in 50 mL THF, then a drop was taken and dripped on the copper mesh, and dried at 80 °C for 2 h. Before testing, the samples were treated with gold spraying. The distribution of elements was obtained by a high-resolution field emission scanning electron microscope equipped with energy dispersive spectroscopy (Regulus 8230, Japan), and testing pattern was selected to use high-end plane insertion energy spectrum, to eliminate shooting shadow.
TPS 2500S thermal analyzer (Hot Disk, Sweden) was used to characterize the thermal conductivity of silicone potting composite materials, in which the double helix probe of 4 mm diameter was sandwiched between two lamella samples of 2 mm thickness. The CLTE was measured on a TMA402F3 thermo-mechanical analyzer (NETZSCH, German) from 25 °C to 250 °C at a heating rate of 10 °C min−1. ZST-121 volume surface resistivity tester (Beijing Zhonghang Times Instrument Equipment, China) was utilized to determine the volume resistivity, and the diameter and thickness of the sample was 8 mm and 2 mm, respectively. The components A and B of silicone potting adhesive were mixed under equal mass. After complete stirring, the mixture was injected into the mold, and vacuumed to eliminate air bubbles. The mixture was cured at 90 °C for 3 h, and then demolded to obtain thermal and insulating test samples.
Sample | Si 2p (%) | C 1s (%) | N 1s (%) | O 1s (%) |
---|---|---|---|---|
Pristine Al2O3 | 1.85 | 17.70 | 0.80 | 79.65 |
Al2O3-epoxy | 8.08 | 42.64 | 0 | 49.28 |
Al2O3–NH2 | 11.46 | 40.08 | 10.50 | 37.96 |
Fig. 2 shows the TG curves of pristine and modified Al2O3. The mass retention rate (at 700 °C) of pristine Al2O3, Al2O3-epoxy, Al2O3–NH2 was 99.99%, 99.69%, and 99.64%, respectively. The mass loss of pristine Al2O3 came from the decomposition of the surface free hydroxyl group at high temperature, whereas the weight loss of Al2O3-epoxy and Al2O3–NH2 came from the decomposition of not only the free hydroxyl group but also the organic residues of KH560 or KH550 on the surface of Al2O3-epoxy and Al2O3–NH2 powders. The amount of residual silane agent grafted on the surface of inorganic powders can be obtained by comparing the mass retention rate difference between pristine and modified inorganic powders.32 A drop in the thermogram of Al2O3-epoxy at 100 °C (0.05%) might be coming from extraneous water, which should be eliminated while calculating the amount of residual KH560 grafted on the surface of Al2O3-epoxy. As a result, the amount of residual KH560 and KH550 grafted on the surface of Al2O3-epoxy and Al2O3–NH2 was 0.25% and 0.35%, respectively.
It is well known that Richard summarized the effect of particle interaction coefficient (σ) on the viscosity of the particle filling system.34 When σ = 0, the suspension viscosity equation was simplified as In(η/η0) = [η]φ, where η is suspension viscosity, η0 and [η] are viscosity and intrinsic viscosity of suspending medium, respectively, and φ is suspension particle volume fraction. For the case σ = 2, the suspension viscosity equation is In(η/η0) = [η]{φ/(1 − φ/φn)}, where, φn is the maximum particle packing fraction. He concluded that the viscosity of the particle filling mixture increased rapidly with increasing σ. In this work, the φ of Al2O3 was 0.68. Assuming φn was 0.95, when the σ increased from 0 to 2, η would increase e1.71[η] times by the above formula. However, the experimental results showed that the viscosity in this work decreased significantly with increasing particle interaction. This abnormal phenomenon may be due to the micro aggregation of Al2O3 particles, which will be discussed later.
Fig. 4 Diagrams of (a) formation of Al2O3 clusters, (b) some vinyl silicone oil segments fixing in the interval of particles. |
Fig. 5 The particle size distribution curves of Al2O3 with different reaction time (a) 0 h, (b) 0.5 h, (c) 1 h, (d) 2 h, (e) 3 h, (f) 4 h. |
Reaction time/h | D10/μm | D50/μm | D90/μm |
---|---|---|---|
0 | 5.79 | 12.55 | 25.21 |
0.5 | 6.18 | 13.07 | 26.10 |
1 | 6.67 | 14.39 | 28.31 |
2 | 9.53 | 18.36 | 33.85 |
3 | 8.97 | 18.35 | 33.69 |
4 | 10.11 | 19.30 | 34.71 |
Fig. 6 The SEM images of Al2O3 with different reaction time (a) 0 h, (b) 0.5 h, (c) 1 h, (d) 2 h, (e) 3 h, (f) 4 h. |
Fig. 6 shows the SEM images of Al2O3 with Al2O3-epoxy and Al2O3–NH2 reacting for different reaction times at 140 °C. It can be seen that the particle distribution was relatively loose when the reaction time was 0 h (Fig. 6(a)). When epoxy groups reacted with amino for 0.5 h to 1 h, the modified Al2O3 particles showed slight aggregation and the size of the Al2O3 clusters was small (Fig. 6(c)). The Al2O3 clusters became larger at 2 h reaction time, which was consistent with the results of particle size distribution shown in Fig. 5, and the Al2O3 particles were in close contact with each other (Fig. 6(d)). The size of Al2O3 clusters was getting larger and larger when the reaction time exceeded 3 h (Fig. 6(e and f)).
Fig. 7 shows the visual element distribution observed by EDS of Al2O3 with Al2O3-epoxy and Al2O3–NH2 reacting for different reaction times. From Fig. 7(a), when the reaction time was 0 h, the images of Al and O elements revealed that the Al2O3 particles were discrete from each other, and the image of Si element was unclear. Fig. 7(b) and (c) display the Al, O and Si images of Al2O3 with Al2O3-epoxy and Al2O3–NH2 reacting for 1 h and 4 h, respectively. It was found that some Al2O3 particles contacted tightly, and some Si elements appeared on the surface and interval of Al2O3 particles. Furthermore, the Si element in Fig. 7(c) was higher and more significant than that in Fig. 7(b) as the reaction time of Al2O3-epoxy and Al2O3–NH2 was prolonged. This phenomenon indicates that some vinyl silicone oil segments are fixed in the intervals of Al2O3 particles as described in Fig. 4(b).
Fig. 7 The Al, O and Si element images of Al2O3 with different reaction time (a) 0 h, (b) 1 h, (c) 4 h. |
Fig. 8 shows the dynamic viscoelasticity curves of precursors in which Al2O3-epoxy reacts with Al2O3–NH2 for different reaction times. Fig. 8(a) shows the curve of the complex viscosity η* versus angular frequency ω. When the reaction time was 0 h, the precursor exhibited significantly low-frequency shear thinning,35 while the precursor with powders reacting for 4 h exhibited weak shear thinning at low frequency, and both samples showed shear thickening behavior at high frequency. The change in viscosity is related to a certain structural change inside the liquid. Giuntoli et al.36 studied the α relaxation kinetic model of a coarse-grained polymer melt under steady-state shear. They found that the shear thinning was due to the action of shearing, the instantaneous combination of macromolecules was “deaggregated” or the fixed particle clusters were destroyed. In this study, when the epoxy and amino groups grafted on the Al2O3 surface did not undergo a chemical reaction, the Al2O3 powders were evenly dispersed in the vinyl silicone oil. Only electrostatic interaction, van der Waals forces and solvation exist among modified Al2O3 powders, and between powders and vinyl silicone oil. Under shear force, the electrostatic attraction, van der Waals forces and solvation were destroyed, and at this moment, the chain of vinyl silicone oil was untangled, resulting in remarkable shear thinning. On the contrary, when the two groups reacted, a chemical bonding interaction was generated among Al2O3 powders to form Al2O3 clusters. A part of the vinyl silicone oil was fixed in the tiny intervals due to capillary phenomenon, which has a lubricating effect resulting in reduced interaction among the Al2O3 clusters. Hence, the shear thinning phenomenon was weakened.
Fig. 8 The dynamic viscoelasticity curves of precursors with different reaction time, (a) η* versus ω, (b) and (c) G′ and G′′ versus ω, and (d) tanδ versus ω. |
Fig. 8 (b) and (c) are the curves of the elastic modulus (G′) and viscous modulus (G′′) versus the angular frequency ω of precursor with the reaction time of 0 h and 4 h, respectively. It could be clearly seen from the figure that when ω was low, the G′ and G′′ of the precursor were basically the same at 0 h reaction time. Whereas the G′′ was higher than G′ when the reaction time was 4 h. It was because that Al2O3-epoxy and Al2O3–NH2 took reaction to build a Al2O3 cluster structure as shown in Fig. 6. Some segments of vinyl silicone oil were fixed in the particle intervals, which deeply limited the movement ability of the vinyl silicone oil, resulting in its prolonged relaxation time. The relationship between loss factor tanδ and ω in Fig. 8(d) further showed that the mechanical loss of the Al2O3-epoxy and Al2O3–NH2 reacting system was higher than that of the non-reacting system at lower frequency. As the frequency increased, both G′ and G′′ showed an increasing trend, but the increasing speed of G′ exceeded that of G′′. For the non-reacting system, the intersection of G′ and G′′ appeared at 99.58 rad s−1, while for the 4 h reaction system, the intersection appeared at 39.64 rad s−1, indicating that the elastic modulus of the 4 h reaction system is greatly improved. The results may be due to the formation of Al2O3 clusters in the 4 h reaction system, and Al2O3 clusters are of a bigger size, which increases the rigidity of the precursor at higher frequency. Zheng et al.37 found that higher G′ depended on larger size and the interaction between aggregations, which is conducive to flocculating a stable 3D network structure.
Reaction time (h) | 0 | 0.5 | 1 | 2 | 3 | 4 |
---|---|---|---|---|---|---|
Thermal conductivity (W m−1 k−1) | 2.67 | 2.69 | 2.70 | 2.67 | 2.71 | 2.73 |
CLTE (ppm/°C) | 74.0 | 73.1 | 72.4 | 75.5 | 74.9 | 75.8 |
Volume electrical resistivity (X 1013 Ω cm) | 5.7 | 4.8 | 2.5 | 6.4 | 7.3 | 4.6 |
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