The present disclosure relates to a crystal growing method for crystals, in particular relates to a crystal growing method for crystals having a high monocrystalline proportion and a large size.
At present, silicon wafers have been widely used in the semiconductor industry. Many electronic devices contain silicon wafers produced using silicon wafers as materials. However, in order to improve wafer performance, many manufacturers have attempted to use silicon carbide wafers as materials for producing silicon carbide chips. Silicon carbide wafers have the advantages of high temperature resistance and high stability.
As far as the prior art is concerned, it takes a very long time to expand the diameter of silicon carbide crystals, and it takes several years to complete the enlargement of conventional crystals from 6 inches to 8 inches. In addition, traditional crystal growth methods cannot effectively form crystals with a high monocrystalline proportion in a short period of time. Based on the above, how to produce large-sized crystals with a high monocrystalline proportion in a shortened time is a problem to be solved.
The invention provides a crystal growing method for crystals, which can greatly shorten the time for forming crystals having a high monocrystalline proportion and a large size.
The crystal growing method for crystals of the present disclosure includes the following steps. A first crystal seed is provided, the first crystal seed has a first monocrystalline proportion and a first size. N times of crystal growth processes are performed on the first crystal seed, wherein each of the crystal growth process will increase the first monocrystalline proportion, and the N times of crystal growth processes are performed until a second crystal having a monocrystalline proportion of 100% is reached, and wherein the N times includes more than 3 times of crystal growth processes.
In one embodiment of the present disclosure, each of the N times of crystal growth processes includes adjusting a ratio difference (ΔTz/ΔTx) of an axial temperature gradient (ΔTz) and a radial temperature gradient (ΔTx) of the crystals to control the ratio difference within a range of 0.5 to 3 for forming the second crystal.
In one embodiment of the present disclosure, each of the N times of crystal growth processes includes the following steps. A previously obtained crystal seed is used for crystal growth to obtain an intermediate crystal with increased monocrystalline proportion; when it is confirmed that the monocrystalline proportion of the intermediate crystal is not 100%, the intermediate crystal is sliced to obtain a growth crystal seed, wherein the growth crystal seed is used as a crystal seed for a subsequent crystal growth process; and when it is confirmed that the monocrystalline proportion of the intermediate crystal reached 100%, the crystal growth processes are stopped and the second crystal is obtained.
In one embodiment of the present disclosure, the method further includes the following steps: providing a preliminary crystal seed, the preliminary crystal seed has a size A and a monocrystalline proportion A′, wherein the size A is smaller than the first size, and the monocrystalline proportion A′ is larger than the first monocrystalline proportion; using the preliminary crystal seed to perform a crystal growth process to obtain a first crystal having the first size and the first monocrystalline proportion; and slicing the first crystal to form the first crystal seed.
In one embodiment of the present disclosure, the N times includes more than 3 times and less than 8 times of crystal growth processes.
In one embodiment of the present disclosure, the N times includes more than 4 times and less than 6 times of crystal growth processes.
In one embodiment of the present disclosure, each of the crystal growth processes has different processing conditions.
In one embodiment of the present disclosure, each of the crystal growth processes has a different ratio difference, or different doping amounts of a nitrogen concentration.
In one embodiment of the present disclosure, each of the crystal growth processes includes controlling a doping amount of the nitrogen concentration in a range of 2*1018 atom/cm3 to 3*1018 atom/cm3.
In one embodiment of the present disclosure, the first monocrystalline proportion is 70% to 80%.
In one embodiment of the present disclosure, the first size is 200 mm.
Based on the above, by using the crystal growing method of the present disclosure for growing silicon carbide crystals, it is possible to significantly shorten the time required for forming crystals having a high monocrystalline proportion and a large size, and crystals having expanded diameter and/or with 100% monocrystalline proportion can be achieved within a certain number of crystal growth processes.
The accompanying drawings are included to provide a further understanding of the disclosure, and are incorporated in and constitute a part of this specification. The drawings illustrate exemplary embodiments of the disclosure and, together with the description, serve to explain the principles of the disclosure.
As shown in
As shown in
In the above step S22 and step S24, the silicon carbide crystal 108 is formed on the seed crystal 106 by physical vapor transport (PVT). In some embodiments, the reactor 102 and the raw material 110 are heated by the induction coil 104 to form the silicon carbide crystal 108 on the seed crystal 106. During the manufacturing process, the seed crystal 106 receives the raw material 110 (silicon carbide powder) that is solidified from a gaseous state, and slowly forms semiconductor crystals on the seed crystal 106 until the silicon carbide crystal 108 with the desired size is obtained. Subsequently, referring to
In the above-mentioned embodiment, when the reactor 102 and the raw material 110 are heated to form the silicon carbide crystal 108, the axial temperature gradient (ΔTz) refers to the temperature gradient of the silicon carbide crystal 108 in the thickness direction, while the radial temperature gradient (ΔTx) refers to the temperature gradient of the silicon carbide crystal 108 in a horizontal direction perpendicular to the thickness direction. In some embodiments, the growth rate difference of each crystal direction is utilized to adjust a temperature difference to achieve the ratio difference (ΔTz/ΔTx) in the range of 0.5 to 3. In general, a growth rate of the <11-20> crystal orientation is greater than a growth rate of the <1-100> crystal orientation. In the embodiment of the present disclosure, the growth rates of the two crystal orientations are controlled to be the same, so that the crystals in each axial/radial direction can obtain a certain growth rate for adjusting the ratio difference (ΔTz/ΔTx) to be in the range of 0.5 and 3.
In some embodiments, the ratio difference (ΔTz/ΔTx) of the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) is controlled in the range of 0.5 to 3 to form the silicon carbide crystal 108. In some embodiments, the ratio difference (ΔTz/ΔTx) of the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) is controlled in the range of 2 to 3 to form the silicon carbide crystal 108. In some embodiments, the ratio difference (ΔTz/ΔTx) of the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) is controlled in the range of 2.5 to 3 to form the silicon carbide crystal 108. In cases where the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) are controlled within the above range, the formed silicon carbide crystal 108 can have improved uniformity of the resistivity.
In some embodiments, when the reactor 102 and the raw material 110 are heated to form the silicon carbide crystal 108, that is, during the growth process of the silicon carbide crystal 108, a doping amount of a nitrogen concentration is further increased so that the nitrogen concentration increases from a first concentration to a second concentration. In some embodiments, the first concentration is 2*1018 atoms/cm3, and the second concentration is 3*1018 atoms/cm3. In some embodiments, the first concentration is 2.2*1018 atoms/cm3, and the second concentration is 2.9*1018 atoms/cm3. In some embodiments, the first concentration is 2.5*1018 atoms/cm3, and the second concentration is 2.8*1018 atoms/cm3. In cases where the doping amount of the nitrogen concentration is controlled within the above range, the uniformity of resistivity of the formed silicon carbide crystal can be further optimized.
In the above embodiments, the nitrogen concentration can be increased in a linear fashion or in a stepwise fashion. For example, different doping adjustment methods of the nitrogen concentration are described with reference to
In the embodiment of the present disclosure, increasing the doping amount of the nitrogen concentration is performed by increasing the flow rate of nitrogen gas in the reactor, so that the increase of the flow of nitrogen is controlled in the range of 10 sccm to 50 sccm, and the method shown in the above
In cases where the above method is used to form silicon carbide crystals, a monocrystalline proportion of the formed silicon carbide crystals and the silicon carbide wafers obtained after processing is 100%, and the resistivity of silicon carbide crystals/wafers is in a range of 15 mΩ·cm to 20 mΩ·cm, preferably within the range of 19 mΩ·cm to 20 mΩ·cm, and a deviation of an uniformity of the resistivity of the silicon carbide wafer is less than 0.4%. In some embodiments, the deviation of the uniformity of the resistivity of the silicon carbide wafer is less than 0.01%. In addition, in some embodiments, basal plane dislocations (BPD) of the silicon carbide crystals/wafers is less than 200/cm2. In some embodiments, basal plane dislocations (BPD) of the silicon carbide crystals/wafers is less than 140/cm2. In some embodiments, a bar stacking fault (BSF) of the silicon carbide crystals/wafers is less than 5/wafer. Accordingly, a silicon carbide crystal/wafer with a uniform resistivity distribution can be obtained, and a stress of the formed silicon carbide crystal/wafer is also lowered, and the geometry of the wafers after processing is also improved.
As shown in
In the above-mentioned examples, the crystal growth process is performed for the first crystal seed 202 for N times, wherein each of the crystal growth processes will increase the first monocrystalline proportion, and the N times of crystal growth processes are performed until a second crystal 250 having a monocrystalline proportion of 100% is reached. In other words, when an intermediate crystal having a monocrystalline proportion of 100% is confirmed, the above crystal growth process is stopped to form the second crystal 250. In some embodiments, the N times includes more than 3 times of crystal growth processes. In some embodiments, the N times includes more than 3 times and less than 8 times of crystal growth processes. In some embodiments, the N times includes more than 4 times and less than 6 times of crystal growth processes.
Furthermore, in the above embodiments, each crystal growth process includes adjusting a ratio difference (ΔTz/ΔTx) between an axial temperature gradient (ΔTz) and a radial temperature gradient (ΔTx) of the crystal, so as to control the ratio difference within a range of 0.5 to 3. In the above embodiments, each crystal growth processes includes controlling a doping amount of a nitrogen concentration in a range of 2*1018 atom/cm3 to 3*1018 atom/cm3. In some embodiments, each of the crystal growth processes are different. For example, in the embodiments of the present disclosure, the ratio difference (ΔTz/ΔTx) between an axial temperature gradient (ΔTz) and a radial temperature gradient (ΔTx) for each of the crystal growth processes are different, and/or the doping amount of the nitrogen concentration are different, provided that the above ratio difference and the doping amount of the nitrogen concentration are still controlled in the above ranges. By using the above methods, it is possible to grow from a B-grade seed (low monocrystalline proportion) into an A-grade crystal (monocrystalline proportion being 100%) within a certain number of crystal growth processes. As such, it is possible to significantly shorten the time required for forming crystals having a high monocrystalline proportion and a large size.
As shown in
In order to prove that the method of the present invention can produce silicon carbide crystals with uniform resistivity, and can significantly shorten the time required for forming large-sized crystals with a high monocrystalline proportion, the following examples are performed and described.
In the first example, (i) the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx), (ii) the doping variation method of the nitrogen concentration, and (iii) the doping amount of the nitrogen concentration of Examples 1 to 7 and Comparative Examples 1 to 4 are adjusted in the manner described in Table 1 and Table 2 below. Furthermore, the growth process is performed in the manner described in
100%
100%
100%
100%
From the experimental results of Examples 1 to 7 shown in Table 1 above, when the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) is controlled in the range of 0.5 to 3, and the doping variation method of the nitrogen concentration is adjusted from low concentration to high concentration, and when the doping amount of the nitrogen concentration is controlled in the range of 2*1011 atoms/cm3 to 3*1018 atoms/cm3, then the obtained silicon carbide crystal will have a monocrystalline proportion of 100%, and the silicon carbide wafer obtained after processing can have a uniform resistivity distribution (deviation of the uniformity of the resistivity is less than 0.4%), and the basal plane dislocations (BPD) of the wafer can be controlled below 200/cm2, the bar stacking fault can be controlled to less than or equal to 5/wafer (ea/wf), and the wafer resistivity (15˜20 mΩ·cm) are also within an ideal range, and preferably in the range of 19 mΩ·cm to 20 mΩ·cm.
Taking a step further, when the ratio difference (A Tz/A Tx) is controlled in the range of 2 to 3, and the doping amount of the nitrogen concentration is controlled in the range of 2.1*1018 atoms/cm3 to 2.9*1018 atoms/cm3, then the silicon carbide wafer obtained after processing the silicon carbide crystals has a better uniformity of the resistivity distribution, and less wafer defects and bar stacking faults can be observed. In addition, when the ratio difference (A Tz/A Tx) is controlled in the range of 2.5 to 3, and the doping amount of the nitrogen concentration is controlled in the range of 2.4*1018 atoms/cm3 to 2.8*1018 atoms/cm3, then the obtained silicon carbide wafer has the best uniformity of the resistivity distribution, and defects such as basal plane dislocations (BPD) and bar stacking faults (BSF) are least observed. Accordingly, the silicon carbide wafer obtained by processing the N-type silicon carbide crystals formed by the method of growing silicon carbide crystals according to the embodiments of the present disclosure can have a uniform resistivity distribution, and the crystal stress is low, and the geometry of the processed wafer will also be improved.
In comparison, from the experimental results shown in Table 2, referring to Comparative Example 1, when the ratio difference (ΔTz/ΔTx) is not controlled within the range of 0.5 to 3, and the doping method of the nitrogen concentration is not changed, while a fixed doping concentration of 1*1018 atoms/cm3 is used, the uniformity of the resistivity distribution of the obtained silicon carbide wafer is not good (deviation of the uniformity >5%), and the basal plane dislocation (BPD) results are also not good. Referring to Comparative Example 2, even when the ratio difference (ΔTz/ΔTx) is controlled within the range of 0.5 to 3, if there is no doping variation in the nitrogen concentration whereby a fixed doping concentration is used, then the uniformity of the resistivity distribution of the obtained silicon carbide wafer is still not good (deviation of the uniformity >4%), and the defects such as basal plane dislocations (BPD) and bar stacking faults (BSF) results are also not good. Referring to Comparative Examples 3-4, although the doping of the nitrogen concentration is varied from a low concentration to a high concentration, if the ratio difference (ΔTz/ΔTx) is not controlled within the range of 0.5 to 3, and if the doping amount of the nitrogen concentration is not controlled within the range of 2*1018 atoms/cm3 to 3*1018 atoms/cm3, although the uniformity of the resistivity distribution is slightly improved compared with Comparative Examples 1-2 (deviation of the uniformity >1.5%), the uniformity of the resistivity distribution is still not within the ideal range, and the defects such as basal plane dislocations (BPD) and bar stacking faults (BSF) results are still not good.
In the second example, (i) the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx), (ii) the doping variation method of the nitrogen concentration, and (iii) the doping amount of the nitrogen concentration of the crystal growth process of Examples 8 to 11 and Comparative Examples 5 to 8 are adjusted in the manner described in Tables 3-10 below. In addition, the crystal growth process is performed using the first crystal seed in the manner described in
As can be seen from the experimental results of Examples 8-11 shown in Tables 3-6 above, when the ratio difference (ΔTz/ΔTx) is controlled within the range of 0.5 to 3, and the doping amount of the nitrogen concentration is controlled within the range of 2*1018 atoms/cm3 5 to 3*1018 atoms/cm3, then no matter how the doping method of the nitrogen concentration is varied, a B-grade crystal seed (poor monocrystalline proportion) can be grown into an A-grade crystal (monocrystalline proportion of 100%) within 6 times (N=6) of the crystal growth process, and the basal plane dislocations (BPD), the resistivity, the uniformity of the resistivity and bar stacking faults (BSF) can all be controlled within an ideal range, for example, the BSF is less than or equal to 5/wafer.
In comparison, as can be seen from the experimental results of Comparative Examples 5-8 shown in Tables 7-10 above, if the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) in each crystal growth process is not within the above range, and the doping amount of the nitrogen concentration is outside the above range, then even if the crystal growth process has been carried out for 11 to 13 times, it is still impossible to make the B-grade crystal seed (poor monocrystalline proportion) to grow to form crystals having a monocrystalline proportion of 100%, and the basal plane dislocations (BPD), uniformity of resistivity and bar stacking fault results are still poor. Accordingly, it can be understood that the crystal growth method of the embodiment of the present disclosure can significantly shorten the time required for forming crystals having a high monocrystalline proportion and a large size.
In the third example, (i) the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx), (ii) the doping variation method of the nitrogen concentration, and (iii) the doping amount of the nitrogen concentration of the crystal growth process of Example 12 and Comparative Example 9 are adjusted in the manner described in Tables 11-12 below. In addition, the method as shown in
As can be seen from the experimental results of Example 12 shown in Table 11 above, when a smaller-sized A-grade preliminary seed (monocrystalline proportion of 100%) is further used for diameter expansion to form the first crystal seed, and the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) of each crystal growth process is controlled within the range of 0.5 to 3, and the doping amount of the nitrogen concentration is controlled within the range of 2*1018 atoms/cm3 to 3*1018 atoms/cm3, then no matter how the doping method of the nitrogen concentration is varied, the smaller-sized A grade crystal seed (monocrystalline proportion of 100%) can be grown into a diameter-expanded large size A-grade crystal (monocrystalline proportion of 100%) within 1 time of preliminary diameter expansion and 4 times (N=4) of the crystal growth process, and the basal plane dislocations (BPD), the resistivity, the uniformity of the resistivity and bar stacking faults (BSF) can all be controlled within an ideal range, for example, the BSF is less than or equal to 5/wafer.
In comparison, as can be seen from the experimental results of Comparative Example 9 shown in Table 12 above, if the ratio difference (ΔTz/ΔTx) between the axial temperature gradient (ΔTz) and the radial temperature gradient (ΔTx) in each crystal growth process is not within the above range, and the doping amount of the nitrogen concentration is outside the above range, then even if one time of preliminary diameter expansion and 10 times of the crystal growth process has been performed, it is still impossible to make the small-sized A-grade crystal seed (monocrystalline proportion of 100%) to grow to form larger size crystals having a monocrystalline proportion of 100%, and the basal plane dislocations (BPD), uniformity of resistivity and bar stacking fault results are still poor. Accordingly, it can be understood that the crystal growth method of the embodiment of the present disclosure can significantly shorten the time required for forming crystals having a high monocrystalline proportion and a large size, thus the multiple expansion steps and years of expansion time required for traditional crystal size expansion can be avoided.
In summary, the N-type silicon carbide crystals formed by the method of growing silicon carbide crystals of the embodiment of the present disclosure can have a uniform resistivity distribution. Accordingly, the crystal stress of the formed silicon carbide crystals is also lowered, and the geometry of the processed wafer is also improved. In addition, through the crystal growth method of the embodiment of the present disclosure, the time to form a large-sized crystal with a high monocrystalline proportion can be greatly shortened, and crystals having expanded diameter and/or with 100% monocrystalline proportion can be achieved within a certain number of crystal growth processes.
It will be apparent to those skilled in the art that various modifications and variations can be made to the disclosed embodiments without departing from the scope or spirit of the disclosure. In view of the foregoing, it is intended that the disclosure covers modifications and variations provided that they fall within the scope of the following claims and their equivalents.
This application claims the priority benefits of U.S. provisional application Ser. No. 63/359,203, filed on Jul. 8, 2022, U.S. provisional application Ser. No. 63/359,205, filed on Jul. 8, 2022, and U.S. provisional application Ser. No. 63/359,208, filed on Jul. 8, 2022. The entirety of the above-mentioned patent application is hereby incorporated by reference herein and made a part of this specification.
Number | Date | Country | |
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63359203 | Jul 2022 | US | |
63359205 | Jul 2022 | US | |
63359208 | Jul 2022 | US |