JPH0250927A - Method for refining metal galimu - Google Patents

Method for refining metal galimu

Info

Publication number
JPH0250927A
JPH0250927A JP19879888A JP19879888A JPH0250927A JP H0250927 A JPH0250927 A JP H0250927A JP 19879888 A JP19879888 A JP 19879888A JP 19879888 A JP19879888 A JP 19879888A JP H0250927 A JPH0250927 A JP H0250927A
Authority
JP
Japan
Prior art keywords
gallium
interface
cooling medium
molten
seed crystals
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP19879888A
Other languages
Japanese (ja)
Inventor
Shoji Mimura
彰治 味村
Kazumasa Arai
新井 一正
Nobuhiko Hamabe
浜辺 順彦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Nippon Light Metal Co Ltd
Original Assignee
Mitsubishi Kasei Corp
Nippon Light Metal Co Ltd
Mitsubishi Chemical Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Kasei Corp, Nippon Light Metal Co Ltd, Mitsubishi Chemical Industries Ltd filed Critical Mitsubishi Kasei Corp
Priority to JP19879888A priority Critical patent/JPH0250927A/en
Publication of JPH0250927A publication Critical patent/JPH0250927A/en
Pending legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To obtain Ga of high quality at the time of growing seed crystals put on the side of a cooling medium of metallic Ga by finding the solidifying speed from a solid-liquid interface detected by the scanning with infrared rays or supersonic waves and regulating the progressing condition in the solidifying. CONSTITUTION:Seed crystals are put on the side of a cooling medium 2 of molten Ga 6, are grown and are solidified in the direction of the other side into crystal solidified metal 7. At this time, scanning is executed with infrared rays or ultrasonic waves to detect the interface between the liquid area (molten Ga 6) and the solid area (crystal solidified metal 7). By the result in the detection of the interface, the solidifying speed in the metallic Ga 7 is regulated to obtain Ga of high quality.

Description

【発明の詳細な説明】 「発明の目的」 本発明は金属ガリウムの精製法に係り、金属ガリウムを
均一に一方向凝固せしめ、有効な管理を可能とすると共
に経済的な精製を得しめようとするものである。
[Detailed Description of the Invention] "Object of the Invention" The present invention relates to a method for refining metallic gallium, and aims to uniformly solidify metallic gallium in one direction, enable effective control, and achieve economical refining. It is something to do.

(産業上の利用分野) 半導体素子や発光素子原料などとして用いられるガリウ
ムの一方向凝固精製技術。
(Industrial application field) One-way solidification and purification technology for gallium, which is used as a raw material for semiconductor devices and light-emitting devices.

(従来の技術) ガリウムは電子材料としての半導体素子や発光素子原料
として優れた特性を有しており、近年その需要は急速に
増大し、この製造ないし精製法についてはそれなりの検
討がなされている。即ち、このガリウムは天然に一様に
存在しているものの散在していて、ガリウムを採算可能
な割合で含有した鉱石は存在しないから、亜鉛やゲルマ
ニウム、特にアルミニウムなどの生産における副生成物
として得ることとならざるを得ない。しかし上記したよ
うな何れの工程からの副生成物であっても、その純度は
せいぜい99.999%(ファイブナイン)程度であり
、上記した半導体素子用原料としてのガリウムメタル純
度は少なくとも99.9999%(シソクスナイン)以
上であるから更に精製して純度を高めることが必要であ
る。
(Prior art) Gallium has excellent properties as a raw material for semiconductor elements and light emitting elements as an electronic material, and its demand has increased rapidly in recent years, and a considerable amount of research has been conducted on its production and purification methods. . In other words, although gallium exists uniformly in nature, it is scattered, and there is no ore that contains gallium in a profitable proportion, so it can be obtained as a by-product in the production of zinc, germanium, and especially aluminum. This has no choice but to happen. However, the purity of by-products from any of the above processes is at most about 99.999% (five nines), and the purity of gallium metal as a raw material for semiconductor devices is at least 99.9999%. % (Sixoxnine) or more, it is necessary to further refine the product to increase its purity.

然してこのようなガリウムメタルの精製法としては、精
製電解法、分別結晶法、帯溶融精製法あるいは単結晶引
き上げ法などが知られている。
However, known methods for refining gallium metal include a refining electrolytic method, a fractional crystallization method, a zone melting refining method, and a single crystal pulling method.

即ち精製電解法は、粗ガリウムメタルを陽極として不純
物濃度を制御した水溶液にガリウムとガリウムより卑な
金属を陽極溶解し、陰極にはガリウムとガリウムより責
な金属のみが電析する性質を利用した方法である。又分
別結晶法は固体ガリウムの方が液体ガリウムより軽いた
め、その液体ガリウム表面を静かに融点以下として液体
表面に固体ガリウムが小塊となって浮いてくるようにし
、これを選別して取出し、所謂偏析現象を利用して精製
する方法がある。
In other words, the refining electrolytic method utilizes the property of using crude gallium metal as an anode, dissolving gallium and metals more base than gallium in an aqueous solution with a controlled impurity concentration, and electrodepositing only gallium and metals more base than gallium on the cathode. It's a method. In addition, in the fractional crystallization method, since solid gallium is lighter than liquid gallium, the surface of the liquid gallium is gently brought below the melting point so that the solid gallium floats on the liquid surface as small lumps, which are then sorted and extracted. There is a method of purification that utilizes the so-called segregation phenomenon.

帯溶融精製法は、所謂ゾーンメルト法であって、例えば
水平に保持したガリウムメタルを交互に加熱冷却を牟り
返して偏析現象を利用し不純物を溶融体側に取除いて行
く方法である。又単結晶引き上げ法はJ、G、 tla
rper (米国特許第3088853号)あるいはP
、 de、 Ia−Beteque  (Mem、 S
ci、 Rev。
The zone melting refining method is the so-called zone melting method, and is a method in which, for example, a gallium metal held horizontally is alternately heated and cooled to remove impurities to the melt side by utilizing the segregation phenomenon. Also, the single crystal pulling method is J, G, tla
rper (US Pat. No. 3,088,853) or P
, de, Ia-Beteque (Mem, S
ci, Rev.

Met、67  (1)  57−69  (1970
) )によって提案されたもので、溶融したガリウムメ
タルに冷却した種子結晶の先端を接触させ、該部分に成
長するガリウムの単結晶をゆっくりと引き上げ、偏析現
象を利用して精製する方法である。
Met, 67 (1) 57-69 (1970
)) is a method in which the tip of a cooled seed crystal is brought into contact with molten gallium metal, and the single crystal of gallium that grows in that area is slowly pulled up and purified using the segregation phenomenon.

更に本発明者等は上記したような従来法によるものの純
度を高め、あるいは操業的不利を解消することについて
検討を重ね、特願昭61−110594(特開昭62−
270494)や特願昭6276080号のような方法
を提案した。即ち溶融ガリウムの表面に種子結晶を存在
せしめた条件下で該溶融ガリウムの表面を気体によって
冷却し、種子結晶による結晶成長速度を制御して溶融ガ
リウムの大部分を凝固せしめ、不純物の高められた残余
の溶融ガリウムを除去する方法である。又これとは別に
本発明者等は大量のガリウムを処理するに適した方法と
して特願昭62−76080号の方法をも提案している
。即ち上記先願方法を改良し溶融ガリウムを収容した容
器の一端に冷媒を循環する冷却室を設けて液状冷却媒体
を採用し冷却効率を高めると共に結果成長速度の制御を
容易化し、ガリウム結晶の成長速度を所定範囲内に維持
するようにしたものである。
Furthermore, the present inventors have repeatedly studied ways to improve the purity of conventional methods as described above, or to eliminate operational disadvantages, and have filed Japanese Patent Application No. 110594/1983 (Japanese Patent Application Laid-open No. 62-110594).
270494) and Japanese Patent Application No. 6276080. That is, the surface of the molten gallium is cooled with gas under conditions in which seed crystals are present on the surface of the molten gallium, and the crystal growth rate by the seed crystals is controlled to solidify most of the molten gallium, thereby increasing impurities. This method removes the remaining molten gallium. Apart from this, the present inventors have also proposed the method of Japanese Patent Application No. 76080/1983 as a method suitable for processing large amounts of gallium. That is, by improving the above-mentioned method of the prior application, a cooling chamber for circulating a coolant is provided at one end of a container containing molten gallium, and a liquid cooling medium is used to increase cooling efficiency and, as a result, to facilitate control of the growth rate, and to grow gallium crystals. The speed is maintained within a predetermined range.

(発明が解決しようとする課題) 前項におけるような従来からの精製法においてはなお問
題点が多い。即ち精製電解法によるものは精製されたガ
リウムの純度が電極からの汚染、あるいは高純度なガリ
ウム水溶液が得難いなどの理由のために、やはり99.
999%台に止まる。また分別結晶法においても固体の
表面に汚染した液体ガリウムが付着するため高純度ガリ
ウムを得ることが困難である。
(Problems to be Solved by the Invention) There are still many problems in the conventional purification methods as described in the previous section. In other words, the purity of purified gallium using the purification electrolytic method is still 99.9% due to contamination from the electrodes or the difficulty of obtaining a high-purity gallium aqueous solution.
It stays at the 999% level. Furthermore, even in the fractional crystallization method, it is difficult to obtain high purity gallium because contaminated liquid gallium adheres to the surface of the solid.

帯溶融精製法は原理的には優れた方法と言えるが、ガリ
ウムメタルの場合には過冷却が大きくて操作が困難であ
り、又凝固したメタルの取出しが容易でない。単結晶引
き上げ法も高純度ガリウムの精製法として有用であるが
、99.9999%以上のガリウムメタルを得るには繰
返して実施する必要があり、装置を多数用意しなげれば
ないと共に工数が大となって経済的に不利である。
Although the zone melting refining method can be said to be an excellent method in principle, in the case of gallium metal, it is difficult to operate due to large supercooling, and it is not easy to take out the solidified metal. The single crystal pulling method is also useful as a method for purifying high-purity gallium, but to obtain gallium metal of 99.9999% or higher, it must be carried out repeatedly, requiring the preparation of a large number of equipment, and requiring a large amount of man-hours. Therefore, it is economically disadvantageous.

これらの不利を解消すべく提案した前記本発明者等の提
案によるものは高純度のガリウムを簡易且つ経済的に得
しめるものとして有効である。しかし、この方法を工業
的規模で操業する場合において、その凝固速度が5〜3
Qim/hrと制限され、しかもその凝固速度を的確に
制御することが必要であって、平均的には上記範囲内で
あっても遅速が生じたような場合においては溶融ガリウ
ム中に濃縮された不純物が凝固する固体ガリウム中に取
込まれ、あるいは溶融ガリウム中への不純物濃縮が整然
と図られないこととなって製品固体ガリウムにおける純
度が阻害され、特に品質的に不安定となる。従ってその
精製に当たっては入念な管理が要求されるが、従来にお
いてはそうした管理は専ら作業者の目視によらざるを得
す、経済的負担が大きいと共に誤認の可能性も高い。な
おこれらの事由から前記したように凝固速度や1回の精
製処理量についての制限が厳しいものとならざるを得ず
、生産性を高めることが困難である。
The proposal proposed by the present inventors to overcome these disadvantages is effective in obtaining high purity gallium simply and economically. However, when this method is operated on an industrial scale, the solidification rate is 5 to 3.
Qim/hr, and it is necessary to accurately control the solidification rate, and in cases where the solidification rate is slow even within the above range on average, it is necessary to concentrate in the molten gallium. Impurities are incorporated into the solid gallium that solidifies, or the impurities are not concentrated in the molten gallium in an orderly manner, impeding the purity of the solid gallium product and making it particularly unstable in terms of quality. Therefore, careful control is required during its refining, but conventionally, such control has to be done solely through visual inspection by workers, which is a heavy economic burden and has a high possibility of misidentification. For these reasons, as described above, restrictions on the coagulation rate and the amount of purification processed at one time have to be severe, making it difficult to increase productivity.

「発明の構成」 (課題を解決するための手段) 溶融したガリウムの冷却媒体側に種子結晶を存在せしめ
冷却媒体による冷却効果で」1記種子結晶を成長し他側
方向に凝固固体化せしめるに当り、赤外線あるいは超音
波による走査が溶融した液体域と固体化した固体域との
界面を交叉するように検出操作をなし、この界面検出結
果により金属ガリウムの凝固速度を制御しつつ精製する
ことを特徴とする金属ガリウムの精製法。
"Structure of the Invention" (Means for Solving the Problems) Seed crystals are made to exist on the cooling medium side of molten gallium, and by the cooling effect of the cooling medium, the seed crystals are grown and solidified toward the other side. In this process, a detection operation is performed so that infrared or ultrasonic scanning intersects the interface between the molten liquid region and the solidified solid region, and the solidification rate of metallic gallium is controlled and purified based on the results of this interface detection. Characteristic method for refining metallic gallium.

(作用) 溶融ガリウムの冷却媒体側に存せしめられた種子結晶が
冷却媒体による冷却効果で成長し他側方向に凝固固体化
が進行し溶融ガリウム中不純分が溶融ガリウム中に濃縮
し、固体化されたガリウムメタルの純度を上昇させる。
(Function) Seed crystals kept on the cooling medium side of the molten gallium grow due to the cooling effect of the cooling medium, solidification progresses toward the other side, and impurities in the molten gallium are concentrated in the molten gallium and solidified. Increases the purity of gallium metal.

赤外線あるいは超音波による走査が液体域固体域の界面
を交叉するように行われることにより位置と赤外線の反
則量との関係あるいは位置と超音波の透過速度との関係
が融液部分と固体部分において変化することを検出して
界面を求め、この界面と時間の関係から凝固速度が得ら
れる。又斯うした凝固速度により前記冷却媒体の温度ま
たは量の何れか一方または双方を制御することによって
前記のような凝固固体化の進行状態を適正に制御する。
By scanning with infrared rays or ultrasonic waves so as to cross the interface between the liquid and solid regions, the relationship between the position and the amount of infrared fouling, or the relationship between the position and the transmission speed of the ultrasonic waves, can be determined in the melt and solid parts. The interface is determined by detecting the change, and the solidification rate can be obtained from the relationship between this interface and time. Further, by controlling either or both of the temperature and the amount of the cooling medium according to the solidification rate, the progress of solidification as described above can be appropriately controlled.

即ち均斉な凝固固体化を得しめ、融液部分への不純物濃
縮を円滑に行わしめて固体化した凝固体の品質を均一化
する。
That is, uniform solidification is achieved, impurities are smoothly concentrated in the melt portion, and the quality of the solidified solid is made uniform.

(実施例) 本発明によるものの具体的な実施態様について説明する
と、本発明方法を実施する具体的設備の1例は第1.2
図に示す如くであって、溶融ガリウムを収容するボート
1の冷却媒体側にコーナー部3aを有する隔膜3を設け
、このような隔膜3部分を冷却室2内に位置せしめ、冷
却室2には冷却媒体の導入口4と排出口5を設けて冷媒
の循環を図り、前記隔膜3部分を介しボート1に収容さ
れたガリウム融液6に冷却効果を与えるように成ってい
る。即ちボート1に収容されたガリウム融液6に対し前
記コーナ一部3aに種子結晶を添加し、又融液6面に稀
塩酸などの保護被覆8を施した条件下で上記のような冷
却を与えることにより種子結晶が成長し、結晶メタル7
がボート1の他側方向に向けて進行する。
(Example) To explain the specific embodiments of the present invention, one example of specific equipment for carrying out the method of the present invention is shown in Section 1.2.
As shown in the figure, a diaphragm 3 having a corner portion 3a is provided on the cooling medium side of a boat 1 that accommodates molten gallium, and such a diaphragm 3 portion is located inside a cooling chamber 2. A coolant inlet 4 and a coolant outlet 5 are provided to circulate the coolant and provide a cooling effect to the gallium melt 6 accommodated in the boat 1 through the diaphragm 3 portion. That is, seed crystals were added to the corner part 3a of the gallium melt 6 stored in the boat 1, and the melt 6 surface was coated with a protective coating 8 such as diluted hydrochloric acid, and the cooling was performed as described above. By giving seed crystals grow, crystal metal 7
is moving toward the other side of the boat 1.

このような一方向凝固方式による精製に関し本発明者等
は実地的に仔細に検討したが、−船釣には冷媒の温度や
流速を調節することにより予め周囲の温度条件を仮りに
一定とする熱量計算で冷媒の冷却温度曲線に従い自動的
に凝固精製処理し得るように考えられるが、実際の処理
操作に当って相当長時間に亘る凝固精製中周辺温度の制
御を完全に行うことが困難であり、又固体ガリウムの結
晶成長方向の制御を有効になし難く、結晶軸の方向によ
り熱伝導率が異なるので固体ガリウム中の温度勾配を予
想し、特定化し難いなどの事実が確認され、凝固ないし
その速度を管理することが困難であって、例えば凝固速
度を設定値の±10%以内に維持し得ない。即ち斯うし
た凝固速度の変動は得られた金属ガリウムの品質に影響
し、安定した製品を得ることができない。
The present inventors have conducted detailed practical studies regarding refining using such a unidirectional solidification method. It is thought that the coagulation and refining process can be performed automatically according to the cooling temperature curve of the refrigerant using calorific value calculations, but in actual processing operations, it is difficult to completely control the ambient temperature during the coagulation and refining process, which lasts for quite a long time. In addition, it has been confirmed that it is difficult to effectively control the crystal growth direction of solid gallium, and that it is difficult to predict and specify the temperature gradient in solid gallium because the thermal conductivity differs depending on the direction of the crystal axis. It is difficult to control the rate, eg, it is not possible to maintain the solidification rate within ±10% of the set value. That is, such fluctuations in the solidification rate affect the quality of the obtained metallic gallium, making it impossible to obtain a stable product.

そこで本発明においては前記したような一方向凝固方式
に従ったガリウムの精製を行うに当り、上記したボート
1に関し第3図に示すように赤外線温度計11を用い、
あるいは第4図に示すような超音波探傷器15を用いて
前記のような出入口4.5に供給排出される恒温槽13
からの冷媒を制御する。即ち第3図の赤外線温度計11
を用いるときはボート1の上方から赤外線を一定時間毎
に固体メタル7と融液6の界面を交叉した方向に走査し
て測定し、その夫々の測定位置での赤外線量の関係が不
連続になる点から界面位置を求めることができる。一方
策4図に示すように超音波探傷器15を用いた場合には
ボート1の両側面に受信プローブ15aと発信プローブ
15bを夫々設け、一定時間毎に結晶成長方向にそった
方向、即ち固体メタル7と融液6の界面を交叉した方向
に走査して超音波の透過速度を測定し、界面位置と前記
透過速度との関係を求める。つまり固体ガリウム7中の
音速は融液である液体ガリウム6中の音速より約30%
大きいので上記のような操作で界面位置が検出でき、斯
うした方法で一定時間毎に検出された界面位置で凝固速
度が求められる。
Therefore, in the present invention, when purifying gallium according to the one-way solidification method as described above, an infrared thermometer 11 is used as shown in FIG.
Alternatively, using an ultrasonic flaw detector 15 as shown in FIG.
Control the refrigerant from. That is, the infrared thermometer 11 in FIG.
When using the infrared rays from above the boat 1, the infrared rays are scanned and measured at regular intervals in a direction crossing the interface between the solid metal 7 and the melt 6, and the relationship between the amounts of infrared rays at each measurement position is discontinuous. The interface position can be determined from the point. On the other hand, as shown in Figure 4, when using an ultrasonic flaw detector 15, a receiving probe 15a and a transmitting probe 15b are installed on both sides of the boat 1, and the probe is inserted in the direction along the crystal growth direction at regular intervals, that is, in the solid state. The ultrasonic transmission speed is measured by scanning the interface between the metal 7 and the melt 6 in the intersecting direction, and the relationship between the interface position and the transmission speed is determined. In other words, the speed of sound in solid gallium 7 is about 30% of the speed of sound in liquid gallium 6, which is a melt.
Since it is large, the interface position can be detected by the operation described above, and the solidification rate can be determined from the interface position detected at regular intervals using this method.

従ってこのように得られる凝固速度が好ましい値を採る
ようにコンピューターその他の計算制御機構12にデー
タを送り、又循環式恒温槽13に温度、流量の指示を送
ることにより自動的且つ的確な凝固速度制御をなすこと
ができる。
Therefore, by sending data to the computer or other calculation control mechanism 12 so that the solidification rate obtained in this way takes a preferable value, and by sending instructions for temperature and flow rate to the circulating constant temperature bath 13, the solidification rate can be automatically and accurately determined. can be controlled.

前記した種子結晶としては別に準備された純度の高いガ
リウム小結晶を用い、あるいは冷水を添加して結晶核を
析出させ、更には別に準備し過冷却された高純度ガリウ
ム結晶に触れて適冷状態となった竿状体をガリウム融液
に接触させるなどの方法で結晶核を形成させたものを用
いる。ボート1周辺の雰囲気温度については、好ましく
はガリウム融点と略同じ30℃前後に維持するか、ある
いは低部より加温したりしてガリウム融液温度を融点よ
り2°C以内に保つことにより略安定した結晶成長と好
ましい精製効果を得しめる。
As the seed crystal described above, a separately prepared high-purity small gallium crystal is used, or cold water is added to precipitate the crystal nucleus, and then a separately prepared supercooled high-purity gallium crystal is touched to cool it appropriately. A crystal nucleus is formed by contacting the resulting rod-shaped body with a gallium melt, and the like is used. The ambient temperature around the boat 1 is preferably maintained at around 30°C, which is approximately the same as the melting point of gallium, or by heating from the lower part to maintain the temperature of the gallium melt within 2°C of the melting point. Achieves stable crystal growth and favorable purification effects.

ガリウム融液6における凝固点は、本発明者らの実地検
討結果からして不純物の種類や量の如何によりそれなり
に低下するものといえる。即ちこの関係について発表さ
れた文献は存在しないが、不純物濃度が数百ppmレベ
ルであるこの種の精製処理では凝固点効果は最大でも0
.1°C以下であって実質的に無視することができる。
Based on the results of practical studies conducted by the present inventors, it can be said that the freezing point of the gallium melt 6 is lowered depending on the type and amount of impurities. In other words, although there is no published literature regarding this relationship, in this type of purification process where the impurity concentration is at the hundreds of ppm level, the freezing point effect is at most 0.
.. It is less than 1°C and can be virtually ignored.

ガリウムは高純度になればなるほど、過冷却が顕著にな
ることが確認され、結晶成長時における融液の温度につ
いては一般的に29〜31℃であり、融液温度が29°
C未満となると、1 kg以上を精製するような条件下
においては結晶成長面が平滑とならないで凹凸に冨んだ
形状となり易い。又融液温度が31°C以上となると結
晶制御が困難となる。固化した金属ガリウムの先端部に
水などによる冷却効果を与え、融液側を保温する場合に
おいては融点の温度は最大でも1°C程度までしか低下
せず、適切に上記したような範囲内に維持することが可
能であり、凝固界面において好ましい温度条件を形成す
ることができる。
It has been confirmed that the higher the purity of gallium, the more pronounced the supercooling becomes.The temperature of the melt during crystal growth is generally 29 to 31℃, and the temperature of the melt is 29℃.
If it is less than C, the crystal growth surface will not be smooth and will tend to have an uneven shape under conditions where 1 kg or more is to be purified. Furthermore, if the melt temperature is 31°C or higher, crystal control becomes difficult. When applying a cooling effect to the tip of solidified metal gallium with water or the like to keep the melt side warm, the melting point temperature will only decrease by about 1°C at most, and should be kept within the range described above. It is possible to maintain a favorable temperature condition at the solidification interface.

結晶成長速度を所定の設定値とするための冷却媒体2の
温度はボート1の形状、その材質、処理されるガリウム
メタル融液量などによって異なるが、夫々設計操業に応
じて適宜に設定すればよい。
The temperature of the cooling medium 2 for setting the crystal growth rate to a predetermined set value varies depending on the shape of the boat 1, its material, the amount of gallium metal melt to be processed, etc., but it can be set appropriately according to the design operation. good.

冷却媒体は通常水で充分であるが、隔膜を厚くしたり、
熱伝導率の小さい材質の隔膜を使用し、あるいはガリウ
ムメタル融液が多量になると冷却媒体の温度を0°C以
下にしなければならない時があり、このような場合に水
を用いると凍結する恐れがあるので、シリコンオイル等
の非水溶媒やアルコール若しくはエチレングリコールな
どを添加したて水を用いればよい。
Water is usually sufficient as the cooling medium, but thickening the diaphragm or
If a diaphragm made of a material with low thermal conductivity is used or a large amount of gallium metal melt is used, the temperature of the cooling medium may have to be kept below 0°C, and if water is used in such cases, there is a risk of freezing. Therefore, fresh water to which a nonaqueous solvent such as silicone oil, alcohol, or ethylene glycol has been added may be used.

上述した第3図の赤外線量を測定する方式で界面を求め
るときの好ましい赤外線波長範囲は0.75〜20μm
であり、この範囲より外れると測定精度が低下するので
好ましくない。又第4図の超音波を用いる場合において
好ましい超音波周波数範囲は0.5〜20MHzであっ
て、この範囲外のときは何れにしても測定精度が劣化す
る。
The preferred infrared wavelength range when determining the interface using the method of measuring the amount of infrared rays in Figure 3 described above is 0.75 to 20 μm.
If it deviates from this range, the measurement accuracy will decrease, which is not preferable. Further, when using the ultrasonic wave shown in FIG. 4, the preferable ultrasonic frequency range is 0.5 to 20 MHz, and measurement accuracy deteriorates in any case outside this range.

本発明によるものの具体的な精製例について述べると以
下の如くである。
A specific example of purification according to the present invention will be described below.

精製例1 第3図に示すような設備を構成し、その第1.2図に示
すようなポリエチレン製ボート1として長さ20cmの
ものを用い、不純物としてCu : 4.9ppm 、
 In : 22ppm 、、Sn : 9.Oppm
を含有した30℃の溶融ガリウム1 kgを注入すると
共に約0.1規定の稀塩酸でその表面を覆い、冷却室2
には30°Cの温水を恒温槽13から約2β/minの
供給量で送入循環せしめ、ボート1の隔膜3におけるコ
ーナ一部3aに予め他の容器に準備した結晶核を種子結
晶として添加し、最初は結晶成長が不安定であるので徐
々に温度を低下せしめ、結晶の大きさが冷却室2に突出
したコーナ一部の大きさを越えた時点で凝固速度が20
m+e/hrになるように冷却媒体の温度を約15°C
として低下し、そのときから凝固速度を波長8〜13μ
mの赤外線温度計(株式会社チノー製携帯用デジタル放
射線温度計IR−AHOT)11の検出結果によって制
御し、約12時間に亘る精製を行なった。精製時間と凝
固長さの関係から凝固速度の変動を求めたところ、設定
値の4.5%以内であることが確認され、得られた精製
ガリウムにおける不純物は平均値がcu:0.28pp
m 、In : 0.38ppm XSn : 0.2
6ppmであり、非常に高品質の精製ガリウムを安定し
て得ることができた。
Purification Example 1 The equipment as shown in Fig. 3 was constructed, and a polyethylene boat 1 having a length of 20 cm as shown in Fig. 1.2 was used, and Cu: 4.9 ppm as impurities.
In: 22ppm, Sn: 9. Oppm
Inject 1 kg of molten gallium at 30°C containing
30°C warm water is fed and circulated from the constant temperature bath 13 at a rate of about 2β/min, and crystal nuclei prepared in advance in another container are added as seed crystals to the corner part 3a of the diaphragm 3 of the boat 1. However, since the crystal growth is unstable at first, the temperature is gradually lowered, and when the size of the crystal exceeds the size of the part of the corner protruding into the cooling chamber 2, the solidification rate decreases to 20%.
Adjust the temperature of the cooling medium to approximately 15°C to obtain m+e/hr.
From that point on, the solidification rate decreases to a wavelength of 8 to 13μ.
Purification was carried out for about 12 hours under the control of the detection results of an infrared thermometer (portable digital radiation thermometer IR-AHOT manufactured by Chino Co., Ltd.) 11. When the fluctuation of the solidification rate was determined from the relationship between the purification time and the solidification length, it was confirmed that it was within 4.5% of the set value, and the average value of impurities in the obtained purified gallium was cu: 0.28pp.
m, In: 0.38ppm XSn: 0.2
6 ppm, and very high quality purified gallium could be stably obtained.

なお比較例として従来の目視により界面を判定し制御し
ながら上記の同じ条件で精製した場合は、凝固速度の変
動が設定値の10.0〜20.0%であって、精製ガリ
ウムにおける不純物は平均値がCu : 0.56pp
m 、In : 0.63ppm 、 Sn : 0.
52ppmであって赤外線温度計の検出結果によって制
御したときと比較して約30〜50%精製の効率が悪く
なった。
As a comparative example, when refining was performed under the same conditions as above while visually determining and controlling the interface, the solidification rate fluctuation was 10.0 to 20.0% of the set value, and the impurities in purified gallium were Average value is Cu: 0.56pp
m, In: 0.63 ppm, Sn: 0.
It was 52 ppm, and the purification efficiency was about 30 to 50% worse than when it was controlled based on the detection results of an infrared thermometer.

精製例2 第4図に示すように発信プローブと受信プロブとをボー
ト1の両長側面外側に接触せしめ、しかも水平方向にス
ライドせしめて測定する超音波発信m(米国ソニック・
インストルメンツ社製据置型MKII超音波深傷器)1
5を用い、2MHzで測定し、精製例1におけると同等
なガリウムを用い、凝固速度も同しく 20 mm/h
rとなるように制御して精製処理した。
Purification Example 2 As shown in Fig. 4, ultrasonic transmitter m (U.S. Sonic Corporation) measures the transmitting probe and the receiving probe by making them contact the outer sides of both long sides of the boat 1 and sliding them in the horizontal direction.
Instruments stationary MKII ultrasonic deep wound instrument) 1
5, measured at 2 MHz, using the same gallium as in Purification Example 1, and the same solidification rate as 20 mm/h.
The purification treatment was carried out by controlling the temperature to be r.

精製時間と凝固長さの関係から凝固速度の変動を求めた
結果は18.5〜21.5ii/hrであって、設定値
の7.5%以内であり、精製ガリウムにおける不純物は
平均値が、Cu : 0.30ppm 、 In : 
0.42ppm、Sn : 0.30ppmであって、
精製例1と同様に高品質のものであることが確認された
The fluctuation of the solidification rate was determined from the relationship between the purification time and the solidification length, and the result was 18.5 to 21.5ii/hr, which was within 7.5% of the set value, and the average value of impurities in purified gallium was 18.5 to 21.5ii/hr. , Cu: 0.30ppm, In:
0.42ppm, Sn: 0.30ppm,
It was confirmed that the product was of high quality as in Purification Example 1.

「発明の効果」 以上説明したような本発明によるときは安定した凝固速
度によって的確に制御し高品質のガリウムを得しめ、又
作業者の専従などを必要としないことから低コストであ
って大量の原料メタルをも合理的に処理し得るなどの効
果を有しており、工業的にその効果の大きい発明である
"Effects of the Invention" According to the present invention as explained above, high-quality gallium can be obtained by accurately controlling the solidification rate with a stable rate, and since it does not require full-time workers, it is possible to produce gallium at low cost and in large quantities. This invention has the advantage of being able to rationally process raw material metals, making it a highly effective invention industrially.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の技術的内容を示すものであって、第1図
は本発明を実施する際に用いた精製ポートの平面図、第
2図はその凝固精製途中の状態を示した断面図、第3図
は赤外線放射温度計を用いた本発明の1つの実施態様を
示す概略図、第4図は超音波探傷器を用いたもう1つの
実施態様についての概略説明図である。 然してこれらの図面において、1はボーI・、2は冷却
室、3は隔膜、3aはそのコーナ一部、4は導入口、5
は排出口、6は溶融ガリウム、7は結晶固体化メタル、
8は稀塩酸などの保護被覆、11は赤外線温度計、12
は計算制御機構、13は循環式恒温槽、15は超音波探
傷器、15aはその発信プローブ、15bはその受信プ
ローブを示すものである。 特 許 出 願 人   日本軽金属株式会社同 三菱化成株式会社 発 明 者 味 村 彰 冶 同 新  井 正 同 浜 辺  順 彦
The drawings show the technical contents of the present invention, and FIG. 1 is a plan view of a refining port used in carrying out the present invention, and FIG. 2 is a sectional view showing the state in the middle of coagulation and refining. FIG. 3 is a schematic diagram showing one embodiment of the present invention using an infrared radiation thermometer, and FIG. 4 is a schematic explanatory diagram of another embodiment using an ultrasonic flaw detector. In these drawings, 1 is a bow I, 2 is a cooling chamber, 3 is a diaphragm, 3a is a part of the corner, 4 is an inlet, and 5 is a diaphragm.
is the discharge port, 6 is the molten gallium, 7 is the crystal solidified metal,
8 is a protective coating such as dilute hydrochloric acid, 11 is an infrared thermometer, 12
13 is a calculation control mechanism, 13 is a circulation type constant temperature bath, 15 is an ultrasonic flaw detector, 15a is its transmitting probe, and 15b is its receiving probe. Patent applicant Nippon Light Metal Co., Ltd. Mitsubishi Kasei Co., Ltd. Inventor Akiharu Ajimura Doshin Isei Hamabe Yoshihiko

Claims (1)

【特許請求の範囲】 1、溶融したガリウムの冷却媒体側に種子結晶を存在せ
しめ冷却媒体による冷却効果で上記種子結晶を成長し他
側方向に凝固固体化せしめるに当り、赤外線あるいは超
音波による走査が溶融した液体域と固体化した固体域と
の界面を交叉するように検出操作をなし、この界面検出
結果により金属ガリウムの凝固速度を制御しつつ精製す
ることを特徴とする金属ガリウムの精製法。 2、流動性冷却媒体の温度または流量の何れか一方また
は双方を調節して金属ガリウムの凝固速度を制御する請
求項1に記載の金属ガリウムの精製法。
[Scope of Claims] 1. When seed crystals are present on the cooling medium side of the molten gallium, and the seed crystals are grown by the cooling effect of the cooling medium and solidified toward the other side, scanning with infrared rays or ultrasonic waves is performed. A method for refining metallic gallium, characterized in that a detection operation is performed so that gallium intersects the interface between a molten liquid region and a solidified solid region, and the solidification rate of metallic gallium is controlled and purified based on the detection result of this interface. . 2. The method for purifying metallic gallium according to claim 1, wherein the solidification rate of metallic gallium is controlled by adjusting one or both of the temperature and flow rate of the fluid cooling medium.
JP19879888A 1988-08-11 1988-08-11 Method for refining metal galimu Pending JPH0250927A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19879888A JPH0250927A (en) 1988-08-11 1988-08-11 Method for refining metal galimu

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19879888A JPH0250927A (en) 1988-08-11 1988-08-11 Method for refining metal galimu

Publications (1)

Publication Number Publication Date
JPH0250927A true JPH0250927A (en) 1990-02-20

Family

ID=16397084

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19879888A Pending JPH0250927A (en) 1988-08-11 1988-08-11 Method for refining metal galimu

Country Status (1)

Country Link
JP (1) JPH0250927A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5458669A (en) * 1992-10-28 1995-10-17 Sumitomo Chemical Company, Limited Process for purification of gallium material
WO2000026422A1 (en) * 1998-10-29 2000-05-11 Dowa Mining Co., Ltd. High purity gallium for preparation of compound semiconductor, and method and apparatus for purifying the same
JP2002241859A (en) * 2001-02-09 2002-08-28 Furukawa Co Ltd Method of refining metal
JP2002241860A (en) * 2001-02-09 2002-08-28 Furukawa Co Ltd Method of refining metal

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5458669A (en) * 1992-10-28 1995-10-17 Sumitomo Chemical Company, Limited Process for purification of gallium material
WO2000026422A1 (en) * 1998-10-29 2000-05-11 Dowa Mining Co., Ltd. High purity gallium for preparation of compound semiconductor, and method and apparatus for purifying the same
US6533838B1 (en) 1998-10-29 2003-03-18 Dowa Mining Co., Ltd. High purity gallium for preparation of compound semiconductor, and method and apparatus for purifying the same
JP2002241859A (en) * 2001-02-09 2002-08-28 Furukawa Co Ltd Method of refining metal
JP2002241860A (en) * 2001-02-09 2002-08-28 Furukawa Co Ltd Method of refining metal

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