JPWO2012036263A1 - Silicon ingot manufacturing container and silicon ingot manufacturing method - Google Patents

Abstract

Provided are a silicon ingot manufacturing container and a silicon ingot manufacturing method capable of easily taking out the grown silicon ingot from the container and improving the yield of the silicon ingot. In a bottomed cylindrical silicon ingot manufacturing container having an upper surface opened for solidifying silicon melt to grow silicon polycrystal, the side wall of the container has a vertically formed side lower part, and the side lower part The side surface middle portion is provided so as to be inclined toward the upper surface opening at a predetermined taper angle θ with respect to the vertical direction, and the side surface upper portion is provided so as to extend vertically to the side surface middle portion. A silicon raw material is introduced into this silicon ingot manufacturing container so that the surface of the silicon melt is located at the inclined portion, and a silicon polycrystal is grown while pulling up the seed crystal at a very low speed by the chiroporus method.

Description

  The present invention relates to a container for producing a silicon ingot for producing a solar cell grade silicon ingot and a method for producing the silicon ingot.

  Conventionally, as a method for producing silicon ingots used for solar cells and the like, a casting method (casting) in which a silicon melt is accommodated in a container such as a crucible or a mold, and the silicon melt is solidified from below to grow silicon polycrystals. (Patent Documents 1 to 5). According to this casting method, the direction of crystal growth is uniform when the silicon melt is solidified, so that it is possible to manufacture a high-quality wafer in which an increase in specific resistance due to grain boundaries is suppressed. Moreover, according to the casting method, mass production of silicon ingots becomes possible.

  In general, a release material is formed on the inner surface of a container used in the casting method. When a silicon ingot is manufactured by a casting method, if silicon reacts with the container when the silicon melt is solidified in the container, the silicon crystals are fixed to the container, making it difficult to take out the ingot. Therefore, a release material is formed on the inner surface of the container so that the silicon crystal does not come into direct contact with the container.

Further, although the density of the silicon melt is 2.5 g / cm ³ , the solid density is 2.33 g / cm ³ , so that the volume expands by about 7% when the silicon melt is solidified in the container. It becomes. And since stress arises in a container with this system expansion, it becomes difficult to take out a silicon ingot from a container, and also a mold release material formed in a container may be damaged. When the release material is damaged, the silicon crystal comes into contact with the container and is fixed, so that the take-out property of the silicon ingot is further deteriorated.
Therefore, there is a need for a technique that relieves stress associated with volume expansion when solidifying a silicon melt. For example, a technique has been proposed in which the opening of the container is tilted outward from the vertical direction to relieve the stress component perpendicular to the side surface of the container and make it difficult for silicon crystals to bite into the container (for example, Patent Document 1). Patent Document 1 discloses a tapered container in which the entire side surface is inclined at 3 ° or more in a direction extending toward the opening of the container.

Japanese Utility Model Publication No. 58-22936 Japanese Utility Model Publication No. 3-22907 JP-A-6-345416 Japanese Patent Laid-Open No. 10-182133 Special table 2010-503596 gazette

However, when using the tapered container described in Patent Document 1, if the taper angle on the side surface of the container is too small, the effect of dispersing the stress associated with the volume expansion during the solidification of silicon cannot be obtained. It is difficult to solve the problem that the release material is damaged. Further, if the taper angle on the side surface of the container is too large, the loss when cutting the outer peripheral portion of the silicon ingot increases, and the yield (raw material collection rate) decreases, which is not desirable (see FIG. 5).
Further, when a silicon ingot is manufactured by a casting method, a silicon crystal is grown from the bottom of a container where a release material is formed, and therefore it is difficult to reduce crystal grain boundaries. As a result, the crystal quality is lowered due to carrier loss, and the yield is lowered due to the growth of crystal grain boundaries.

  SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and a silicon ingot manufacturing container and a silicon ingot that can easily take out a grown silicon ingot from the container and can improve the yield of the silicon ingot. It aims at providing the manufacturing method of.

The invention according to claim 1 is a bottomed cylindrical silicon ingot manufacturing container having an open upper surface for solidifying a silicon melt to grow a silicon polycrystal.
The side wall of the container is vertically formed on the lower side of the side, and the side of the side is formed so as to be inclined toward the upper surface opening at a predetermined taper angle θ with respect to the lower side of the side. It is characterized by comprising a side surface upper part vertically connected to the middle part of the side surface.

  The invention described in claim 2 is the container for producing a silicon ingot according to claim 1, wherein the taper angle θ is 10 to 80 °.

  The invention described in claim 3 is the container for producing a silicon ingot according to claim 2, wherein the taper angle θ is 15 to 60 °.

  The invention according to claim 4 is the container for producing a silicon ingot according to claim 2, wherein the taper angle θ is 20 to 70 °.

  The invention according to claim 5 is the container for producing a silicon ingot according to claim 2, wherein the taper angle θ is 20 to 45 °.

The invention according to claim 6 is the container for producing a silicon ingot according to any one of claims 1 to 5,
It is characterized by being composed of a material composed of any one of quartz, Si3N4, SiC, graphite, and alumina, or a material combining two or more.

The invention according to claim 7 is the silicon ingot manufacturing container according to any one of claims 1 to 6, wherein the silicon raw material is charged so that the surface of the silicon melt is located at the inclined portion,
The silicon melt is solidified to grow a silicon polycrystal.

The invention according to claim 8 is the method for producing a silicon ingot according to claim 7, wherein a seed crystal is brought into contact with the surface of the silicon melt,
While pulling up the seed crystal, the silicon melt is solidified from the surface to grow a silicon polycrystal.

  The invention according to claim 9 is the method for producing a silicon ingot according to claim 8, wherein the seed crystal is pulled up at a speed corresponding to volume expansion when the silicon melt is solidified.

Below, the background that led to the completion of the present invention will be described.
Conventionally, as one of crystal growth methods, a chiropolos method is known in which a seed crystal is brought into contact with a melt surface, and the crystal is grown downward from the melt surface. In this chiloporous method, crystals grow from the melt surface with little foreign matter, so that a higher quality silicon crystal can be expected than the casting method. The present inventor has repeatedly studied to establish a method for producing a silicon ingot using the chiloporous method instead of the casting method in which the crystal is grown from the bottom of the container in which the release material is formed.

  First, when manufacturing a silicon ingot using the chiroporous method, a method was devised to relieve the longitudinal stress associated with volume expansion during solidification of silicon by pulling up the grown crystal at a very low speed. However, when a silicon ingot is manufactured by this method, there are many places where the release material formed on the inner surface of the container has disappeared in a planar shape, and it is difficult to take out the silicon ingot.

In order to investigate the cause, the container after the silicon ingot was manufactured was observed. As a result, the mold release material was planar at the top periphery of the silicon ingot, that is, the portion corresponding to the portion where the surface of the silicon melt was solidified and crystallized. It became clear that it disappeared. Moreover, it was confirmed that the convex part about 0.1-0.5 mm in height is formed in the circumferential direction at the top periphery of the silicon ingot.
On the other hand, when the silicon ingot was manufactured by the casting method, the release material disappeared at the portion corresponding to the top of the silicon ingot. From this, it was considered that the stress accompanying the volume expansion when the vicinity of the surface of the silicon melt solidifies is significantly greater than the stress accompanying the volume expansion when the other portion solidifies, regardless of the crystal growth method. In the case of using the chiroporus method, when the vicinity of the surface of the silicon melt is solidified, the laterally expanded silicon crystal (especially the convex portion on the top periphery) bites into the release material, and in this state, it is half-strengthened. It was thought that the release material was peeled off by being pulled up.

  And, by focusing on the part where the surface of the silicon melt will be located and improving the shape of the container, it is possible to effectively disperse the stress accompanying volume expansion (particularly lateral volume expansion) during silicon solidification As a result, the inventors have obtained knowledge that it is possible to achieve both the take-out property of the silicon ingot from the container and the yield, thereby completing the present invention.

According to the present invention, stress generated in the container due to volume expansion at the time of silicon solidification is relieved, so that the release material formed on the inner surface of the container can be effectively prevented from being damaged. Therefore, the grown silicon ingot can be easily taken out without being fixed to the container.
Further, in the silicon ingot manufacturing container, the portion where the stress accompanying volume expansion during silicon solidification is increased is the inclined portion, and the portion where the stress is lower (lower side) is formed vertically, so the outer peripheral portion of the silicon ingot Processing loss when cutting is reduced. Therefore, the yield of silicon ingots can be improved.

It is sectional drawing of the container for silicon ingot manufacture to which this invention is applied. It is a figure which shows an example of the crystal growth apparatus using the container for silicon ingot manufacture to which this invention is applied. It is a figure which shows the growth process of the silicon polycrystal when using the crystal growth apparatus of embodiment. It is a figure which shows the crystal growth apparatus using the container for manufacture of a general straight body type silicon ingot. It is a figure which shows the loss which generate | occur | produces when using the conventional taper type container. Section (a) of the side wall of the container for producing silicon ingot used in the embodiment of the present invention, an example of a container shape when viewed from the top of the container toward the bottom wall (rectangular container (b), cylindrical container (c )), And a schematic explanatory diagram of their preferred thicknesses and lengths.

Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a sectional view of a container for producing a silicon ingot to which the present invention is applied. A container (hereinafter referred to as a container) 11 for producing a silicon ingot shown in FIG. 1 is a bottomed cylindrical or rectangular tube container whose upper surface is opened, for example, formed by molding a quartz material. The side wall of the container 11 is inclined so as to expand toward the upper surface opening at a taper angle (inclination angle with respect to the vertical direction) θ at a side lower part (hereinafter referred to as a straight body part) 11c formed vertically. A side surface middle portion (hereinafter referred to as an inclined portion) 11b provided continuously and a side surface upper portion 11a provided vertically connected to the inclined portion 11b are partitioned.

  Here, as shown in FIG. 6A, when the thickness of the side wall 11a and the bottom wall 11d of the container 11 is T1, the thickness T1 is preferably about 5 to 20 mm. If it is less than 5 mm, the vulnerability of the container material becomes a problem. On the other hand, if it is larger than 20 mm, the influence due to the increase in the heat insulating property of the container cannot be ignored, the silicon melting time increases, the lead time and the power cost increase, and the productivity decreases. For the same reason, the thickness T2 of the side surface lower part 11c is desirably about 5 to 30 mm. The length Lc of the side lower portion 11c is not particularly limited, but when the raw material is melted in the container, the ratio of the length La + Lb above the side lower portion 11c to the length Lc of the side lower portion 11c (La + Lb) It is desirable that / Lc is “2” or more. Since the silicon raw material has a solid density smaller than that of the liquid, in order to bring the melt surface position to at least the position of Lc (the uppermost end of the straight body portion 11c), the raw material is placed in the container at least twice as much as Lc. It is necessary to fill up to the height. Although the degree of filling into the container varies depending on the shape of the raw material, the above dimensional ratio is sufficient for practical use. The thickness and length of the container 11 described above are not limited to the case of a rectangular tube-shaped container, and the same applies to the case of a cylindrical container.

  As shown in FIG. 6 (a), if the internal dimensions of the upper and lower portions of the container 11 are m1 and m2, respectively, the difference (m1−m2) between them is in the range of 2 to 50 mm, preferably 10 to 20 mm. It is desirable to be. If it is less than 2 mm, it is impossible to prevent the silicon ingot during crystal growth from biting into the release material and the container. If it exceeds 50 mm, the thermal insulation of the container side inclined part and the thick part at the bottom of the side will increase, so the silicon melting time will increase and lead time and power costs will increase as compared to the case of 50 mm or less. The nature will decline. Therefore, for example, when obtaining a Si ingot of about 150 to 270 kg from a rectangular or cylindrical container, m2 is 600 mm, m1 is 602 to 650 mm, preferably 610 mm to 620 mm.

  When the silicon melt is accommodated in the container 11 and the silicon melt is solidified to grow a silicon polycrystal, the stress accompanying the volume expansion when the silicon melt located in the inclined portion 11b is solidified is the inclined portion 11b. It is dispersed into a component perpendicular to the component and a component parallel to the component. For example, by setting the taper angle θ to 3 ° or more and less than 90 °, it is possible to disperse the stress accompanying volume expansion to such an extent that the release material does not peel off. According to the experiment, when the taper angle θ is less than 3 °, the grown silicon ingot bites into the release material, and it is confirmed that the release material is damaged. Therefore, the taper angle θ is desirably 3 ° or more.

FIG. 2 is a diagram illustrating an example of a crystal growth apparatus using the container 11.
The crystal growth apparatus 1 shown in FIG. 2 is for manufacturing a silicon ingot by the chiroporus method, and uses a container 11 in which a release material 12 such as a Si3N4 sintered body is formed on the inner surface. In the crystal growth apparatus 1, a container 11 is supported by a susceptor 13 made of graphite, and a heater 14 is disposed on the outer periphery of the susceptor 13. A crystal pulling shaft 15 is disposed in the center of the container 11, and a seed crystal 16 made of Si single crystal (or Si polycrystal) is attached to the tip thereof.

When a silicon ingot is manufactured using the crystal growth apparatus 1 by the chiloporous method, a silicon raw material (for example, silicon melt) is charged into the container 11 so that the surface of the silicon melt 17 is positioned at the inclined portion 11b. Then, the seed crystal 16 is brought into contact with the surface of the silicon melt 17, and the silicon melt 17 is solidified from the surface to grow a silicon polycrystal.
At this time, by growing the silicon polycrystal while pulling up the seed crystal 16 at an extremely low speed, it is possible to relieve the longitudinal stress associated with the volume expansion during the solidification of the silicon. That is, the pulling speed of the seed crystal 16 is set according to the volume expansion in the vertical direction when the silicon melt 17 is solidified.

  Further, since the surface of the silicon melt 17 is located at the inclined portion 11b of the container 11, the lateral stress generated in the container 11 due to volume expansion when the vicinity of the melt surface solidifies is dispersed. That is, since the stress component perpendicular to the inclined portion 11b decreases according to the taper angle θ, the silicon crystal can be prevented from biting into the release material 12. Therefore, since the release material 12 is not damaged during the growth process of the silicon polycrystal, the grown silicon ingot can be easily taken out without being fixed to the container.

By appropriately setting the dimensions of the container 11 (inner diameter of the straight body 11c, taper angle θ, etc.) and the amount of silicon raw material to be introduced (surface position of the silicon melt 17), the seed crystal 16 can be pulled up. It is also possible to prevent the top periphery of the silicon ingot from contacting the inner surface of the container 11 (inclined portion 11b).
For example, when the vicinity of the surface of the silicon melt located in the inclined portion 11b is solidified, when the crystal formed on the liquid surface from the seed crystal 16 to the straight body portion of the container is pulled up by L, before and after the pulling, The diameter of the melt surface is expanded by 2L tan θ. Therefore, if this amount of diameter expansion (2Ltanθ) is larger than the volume expansion in the lateral direction at the time of silicon solidification, the top peripheral edge of the silicon ingot does not contact the inner surface of the container 11 (inclined portion 11b).
It is known that the silicon melt expands by about 1 mm in the lateral direction when solidified, and according to experiments by the present inventors, the height α (0.1-0. (About 5 mm) is formed, and by setting the pulling amount L and the taper angle θ of the seed crystal 16 such that the diameter expansion amount (2Ltanθ) is larger than (1 + α). The top periphery of the silicon ingot can be prevented from contacting the inner surface of the container 11 (inclined portion 11b). For example, when L = 10.5 (mm) and α = 0.1 (mm), θ ≧ 3 °.

Further, in the container 11, only the portion where a large stress is generated due to the volume expansion at the time of silicon solidification is the inclined portion 11b, and the side lower portion 11c where the stress is small is formed vertically, so that the outer peripheral portion of the silicon ingot is cut. Thus, the loss when processing into a columnar or prismatic shape is reduced. Therefore, the yield of silicon ingots can be improved.
That is, as shown in FIG. 5, when the entire side surface of the container is inclined, the stress associated with the volume expansion during silicon solidification can be dispersed, but the difference between the bottom outer diameter and the upper outer diameter of the silicon ingot increases. Therefore, the loss increases when the silicon ingot is processed into a cylindrical shape or a prismatic shape.

For example, when an ingot having a bottom diameter of 90 mm, a height of 110 mm, and a top diameter of 128 mm is obtained using a rectangular cylindrical container having a taper angle of 10 ° on the entire side surface of the container, the loss volume is 56% of the whole. Become. Similarly, in order to produce an ingot having a bottom diameter of 90 mm and a height of 110 mm, when the taper angles are 20 °, 30 °, 45 °, and 70 °, the upper outer diameters of the rectangular tube container and the ingot are remarkably large. In addition to increasing the size of the furnace, the loss rates of the ingots on the bottom of the vessel are calculated to be 70%, 79%, 87%, and 97%, respectively. As described above, when the conventional method of inclining the entire side surface of the container to increase the taper angle is performed, the yield of the prismatic ingot is significantly reduced. There is a demerit that the number of cutouts will increase if the yield is increased as much as possible.
On the other hand, in the case where the container 11 according to the embodiment of the present invention is used, the loss volume ratio is 36% because only the upper portion of the side surface of the ingot Top is tapered and the other side surface portion is almost a straight body. Even when the taper angle is changed to 10 °, 20 °, 30 °, 45 °, and 70 °, the loss volume ratio remains 36%.

Further, when a silicon ingot is manufactured using the chiroporous method, a silicon polycrystal is grown while pulling up the seed crystal. Therefore, by adjusting the pulling speed appropriately, the top periphery of the silicon ingot is separated from the release material 12. Growth can be advanced while maintaining a non-contact state. Therefore, it is possible to more effectively prevent the silicon ingot from biting into the release material 12, and the biting operation does not hinder the growth crystal pulling operation.
Further, by pulling up the seed crystal 16 in accordance with the volume expansion at the time of silicon solidification, the stress in the vertical direction accompanying the volume expansion is relieved, so that a problem due to the compression of the silicon melt does not occur.

  In addition, by setting the taper angle θ to 3 ° or more and less than 90 °, the stress accompanying the volume expansion at the time of silicon solidification can be dispersed to the extent that the release material 12 is not damaged, but if the taper angle θ is too small The effect of dispersing stress associated with volume expansion is small, and in some cases, the release material 12 may be damaged. On the other hand, if the taper angle θ is too large, the inclined portion 11b protrudes laterally in order to secure the height of the inclined portion 11b, leading to an increase in the size of the device and an increase in loss, and the taper. Since the release material is easily broken at the curved portion that is the boundary between the surface and the straight body portion, there is a possibility that the ingot cannot be taken out well. From such a viewpoint, the taper angle θ is desirably set in the range of 10 ° to 80 °, preferably 20 ° to 70 °, or 15 ° to 60 °, more preferably 20 ° to 45 °.

[Example]
In Examples 1 to 4, a silicon ingot was manufactured by the chiropoulos method using the crystal growth apparatus 1. The container 11 has a cylindrical shape, and its dimensions are such that the inner diameter (m1) of the opening on the straight body 11a is 146 mm, the inner diameter (m2) of the bottom of the straight body 11c is 125 mm, and the height Lc of the straight body 11c. 30 mm and La + Lb 60 mm. The height Lb of the inclined portion 11b was 29 mm, 18 mm, 10 mm, and 4 mm when the taper angle θ = 20 °, 30 °, 45 °, and 70 °, respectively.
First, a silicon melt to which boron (concentration: 1.0 × 10 ¹⁶ atoms / cm ³ ) is added is poured into the cylindrical container 11, and the surface of the silicon melt is set at the midpoint of the inclined portion 11 b (with respect to the straight body portion 11 c). The silicon melt was held at 5.25 mm from the boundary so that the temperature gradient in the depth direction was 10 ° C./cm.

Then, a seed crystal 16 made of a Si single crystal having a crystal orientation of <100> and a 3.5 mm square is brought into contact with the surface of the silicon melt, and a silicon polycrystal is grown while pulling up the seed crystal 16 manually at 1 mm / h. I let you. At this time, the container 11 and the seed crystal 16 were rotated at 5 rpm, and a silicon polycrystal was grown concentrically around the seed crystal 16. The silicon melt was completely solidified by growth for 3 hours to obtain a silicon ingot according to the example. The time when the temperature of the bottom of the container 11 reached 1410 ° C., the freezing point of silicon, was regarded as the end point of crystal growth. These results are shown in Table 1.

  In the manufacture of silicon ingots according to Examples 1 to 4, as shown in FIG. 3, the silicon polycrystalline 18 did not bite into the release material 12 during the growth process, and the pulling operation was not hindered. That is, the compressive stress generated in the silicon melt 17 was effectively relieved by using the container 11 having the inclined portion 11b and growing the silicon polycrystal while pulling up the seed crystal 16.

Further, the manufactured silicon ingot could be easily taken out from the container 11. Further, the fusion between the container 11 and the top periphery of the silicon ingot, which has been a problem until now, did not occur. Moreover, there was no practical problem such as cracking of the ingot when it was processed into a straight cylinder-shaped silicon ingot.
Further, in the obtained silicon ingot, the crystal grain boundaries were aligned in the vertical direction, and the crystal quality was improved as compared with the silicon ingot produced by the casting method. Thus, the effectiveness by using the container 11 of the embodiment to grow a crystal by the chiloporous method was confirmed.
In Examples 1 to 4, the taper angle θ of the inclined portion 11b is shown as 20 °, 30 °, 45 °, and 70 °. However, the same result is obtained when the taper angle θ is 60 °. Obtained. Moreover, as a result of performing an experiment by changing the taper angle θ little by little in the range of 10 to 80 ° and comparing it, when the taper angle θ is 15 to 60 °, the take-out property of the silicon ingot from the container is better. In other words, it was confirmed that the yield is most excellent when the taper angle θ is 20 to 45 °.

[Comparative example]
FIG. 4 is a diagram showing a schematic configuration of the crystal growth apparatus used in Comparative Example 4. In FIG. 4, the same reference numerals as those in the crystal growth apparatus 1 of the embodiment are assigned to the 20th series. The crystal growth apparatus 2 is different from the crystal growth apparatus 1 of the embodiment in that a general straight barrel type container 21 is used.
In Comparative Examples 1 to 4, silicon ingots were produced by the chiroporous method using the crystal growth apparatus 2. As the cylindrical container 21, a straight barrel container having an inner diameter of 125 mm was used. The input amount of silicon raw material, the growth condition of silicon polycrystal, and the like were the same as in the example.

In Comparative Example 1, the container was caught during the pulling of the crystal, and as a result of the growth progressing, the volume expansion stress concentrated on the bottom of the container and the container was destroyed. When the container 21 after the silicon ingot was taken out was confirmed, peeling of the release material 22 was not observed in most of the bottom and side surfaces of the container 21, but in the portion corresponding to the top of the silicon ingot, There were many regions where the release material 22 disappeared. When the vicinity of the surface of the silicon melt 27 is solidified, the laterally expanded silicon polycrystal 28 bites into the release material 22, and in this state, the release material 22 is peeled off by being forcibly pulled up. It is considered that it was difficult to take out the silicon ingot because the polycrystal was fixed to the container 21.
In the case of the taper angle of 8 ° in Comparative Example 2, the crystal was not caught by the container when the crystal was pulled by the chiloporous method.
In the case of Comparative Example 3, the release material was broken at the curved portion of the container's tapered portion and the straight body portion, and the ingot and the container were fused at that portion, making it impossible to take out the ingot. It seems that the release material weakened at the curved portion could not withstand the volume expansion stress.

  In the production of the silicon ingot according to the comparative example 4, as shown in FIG. 4, the silicon polycrystal 28 bites into the release material 22 during the growth process, thereby hindering the pulling operation. As a result of the restricted upward movement of the growth crystal (lowering the pulling speed), the silicon melt is compressed without relaxation of the stress due to volume expansion during the solidification of the silicon, and the melt is intense from the center of the container. The phenomenon of spraying up and splashing outside the container occurred (silicon melt sprayed up). Since squirting occurred during the growth process, good crystal growth was hindered, and furthermore, expensive device members were damaged.

By combining these results, it has been found that the taper angle θ at which the silicon ingot can be removed from the container without any problem is in the range of 10 ° to 80 °.
In addition, it was found that the taper angle θ is more preferably 20 ° to 70 ° in consideration of easy peeling of the release material at the curved portion and the volume expansion stress of Si in the lateral direction.

  As mentioned above, although the invention made by this inventor was concretely demonstrated based on embodiment, this invention is not limited to the said embodiment, It can change in the range which does not deviate from the summary.

  For example, in the embodiment, the case where the container 11 is made of a quartz material has been described. However, the container 11 may be made of a material composed of any one of quartz, Si3N4, SiC, graphite, and alumina, or a combination of two or more. it can.

  Further, for example, according to the container 11, since the stress accompanying the volume expansion at the time of silicon solidification is dispersed in the inclined portion 11b, it is also effective when a silicon ingot is manufactured by a casting method. Even when a silicon ingot is manufactured by a casting method, the surface of the silicon melt may be positioned at the inclined portion 11b. Even when the shape of the container 11 is changed from a cylindrical shape to a rectangular tube shape, the same results as in Examples 1 to 4 and Comparative Examples 1 to 4 are obtained.

  The embodiment disclosed this time should be considered as illustrative in all points and not restrictive. The scope of the present invention is defined by the terms of the claims, rather than the description above, and is intended to include any modifications within the scope and meaning equivalent to the terms of the claims.

DESCRIPTION OF SYMBOLS 1 Crystal growth apparatus 11 Silicon ingot manufacturing container 11a Side surface upper part 11b Side surface center part (inclined part)
11c Lower side (straight trunk)
12 Release material 13 Susceptor 14 Heater 15 Crystal pulling shaft 16 Seed crystal 17 Silicon melt 18 Silicon polycrystal θ Taper angle

Claims (9)

A bottomed cylindrical silicon ingot manufacturing container having an open top surface for solidifying a silicon melt and growing silicon polycrystals,
The side wall of the container is vertically formed on the lower side of the side, and the side of the side is formed so as to be inclined toward the upper surface opening at a predetermined taper angle θ with respect to the lower side of the side. A container for producing a silicon ingot, characterized in that the container is composed of an upper part of a side face provided vertically in the middle part of the side face.   The said taper angle (theta) is 10-80 degrees, The container for silicon ingot manufacture of Claim 1 characterized by the above-mentioned.   The said taper angle (theta) is 15-60 degrees, The container for silicon ingot manufacture of Claim 2 characterized by the above-mentioned.   The said taper angle (theta) is 20-70 degrees, The container for silicon ingot manufacture of Claim 2 characterized by the above-mentioned.   The said taper angle (theta) is 20-45 degrees, The container for silicon ingot manufacture of Claim 2 characterized by the above-mentioned.   The silicon ingot according to any one of claims 1 to 5, wherein the silicon ingot is made of a material made of any one of quartz, Si3N4, SiC, graphite, and alumina, or a material that is a combination of two or more. Manufacturing container. A silicon raw material is charged into the silicon ingot manufacturing container according to any one of claims 1 to 6 so that a surface of a silicon melt is located at the inclined portion,
A method for producing a silicon ingot, wherein the silicon melt is solidified to grow a silicon polycrystal. A seed crystal is brought into contact with the surface of the silicon melt,
The method for producing a silicon ingot according to claim 7, wherein the silicon melt is solidified from the surface while pulling up the seed crystal to grow a silicon polycrystal.   The method for producing a silicon ingot according to claim 8, wherein the seed crystal is pulled up at a speed corresponding to a volume expansion when the silicon melt is solidified.

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