JP2001232234A - Method for concentrating gallium compound from precipitate containing gallium compound, abrasive grain, and cutting oil - Google Patents

Method for concentrating gallium compound from precipitate containing gallium compound, abrasive grain, and cutting oil

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Publication number
JP2001232234A
JP2001232234A JP2000054347A JP2000054347A JP2001232234A JP 2001232234 A JP2001232234 A JP 2001232234A JP 2000054347 A JP2000054347 A JP 2000054347A JP 2000054347 A JP2000054347 A JP 2000054347A JP 2001232234 A JP2001232234 A JP 2001232234A
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JP
Japan
Prior art keywords
gallium compound
solvent
cutting oil
gallium
abrasive grains
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.)
Granted
Application number
JP2000054347A
Other languages
Japanese (ja)
Other versions
JP3436304B2 (en
Inventor
Saneyuki Kakimoto
実行 柿本
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining Co Ltd
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Filing date
Publication date
Application filed by Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP2000054347A priority Critical patent/JP3436304B2/en
Publication of JP2001232234A publication Critical patent/JP2001232234A/en
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Publication of JP3436304B2 publication Critical patent/JP3436304B2/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Grinding-Machine Dressing And Accessory Apparatuses (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a gallium compound concentration method with an improved gallium compound recovery ratio and capable of suppressing generation of industrial wastes. SOLUTION: The method for concentrating a gallium compound from a precipitate containing a gallium compound, an abrasive grain, and a cutting oil comprises a first step of dissolving the cutting oil of the precipitate in a solvent compatible with the cutting oil and having a boiling point lower than the thermal decomposition temperature of the gallium compound and simultaneously dispersing the gallium compound and the abrasive grain of the precipitate in the solvent, a second step of wet classifying the solvent in which the gallium compound and the abrasive grain are dispersed and separating the solvent in which a fine powder containing mainly the gallium compound is dispersed and the solvent in which a coarse powder containing mainly the abrasive grain is dispersed, a third step of separating the solvent from the solvent in which the fine powder is dispersed to obtain the fine powder, and a fourth step of supplementing the abrasive grain in the same quantity as that of the abrasive grain separated as the fine powder after the solvent is removed based on necessity from the solvent in which the coarse powder is dispersed, adjusting the quantity of the cutting oil, and making the gallium compound a slurry for the time of wire saw cutting.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、リン化ガリウム等
ガリウムを含む化合物半導体結晶ウエハの製造過程で発
生するガリウム化合物、砥粒および切削油を含む澱物か
らガリウム分を濃縮して回収するためのガリウム化合物
の濃縮方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for concentrating and recovering gallium from a gallium compound, abrasive grains and cutting oil containing cutting oil generated during the production of a compound semiconductor crystal wafer containing gallium such as gallium phosphide. And a method for concentrating a gallium compound.

【0002】[0002]

【従来の技術】リン化ガリウム等ガリウムを含む化合物
半導体結晶ウエハの製造過程で、ガリウムを含む化合物
半導体結晶(以下、ガリウム化合物という)を切断する
際には、従来、ダイヤモンド内周刃切断装置が用いられ
ていた。この際に切削屑として発生する澱物はガリウム
化合物の切削粉がほとんどであり、金属ガリウム回収の
ための原料として有効利用されていた。
2. Description of the Related Art In the process of manufacturing a compound semiconductor crystal containing gallium such as gallium phosphide, when cutting a compound semiconductor crystal containing gallium (hereinafter referred to as a gallium compound), a diamond inner peripheral blade cutting device has conventionally been used. Was used. Most of the sediment generated as cutting chips at this time is a cutting powder of a gallium compound, and has been effectively used as a raw material for recovering metallic gallium.

【0003】ところで、近年、切断ロス低減による低コ
スト化のため、ガリウム化合物の切断方法については、
切断しろのより少ないワイヤーソー切断による方法に置
き換わってきた。このワイヤーソー切断による方法では
砥粒を分散させた切削油(以下、スラリーという)を用
いるため、ワイヤーソー切断の際に発生する澱物は、微
細な切削粉(細粉)、より粗大な砥粒(粗粉)および切
削油を含む混合物として捕集される。そして、ワイヤー
ソー切断では砥粒の使用量が多いため、上記澱物中のガ
リウム化合物含有量は10重量%以下となりガリウム濃
度は低かった。
[0003] Recently, in order to reduce the cost by reducing the cutting loss, cutting methods for gallium compounds have been described.
It has been replaced by a wire saw cutting method with less cutting margin. In this wire saw cutting method, cutting oil in which abrasive grains are dispersed (hereinafter referred to as slurry) is used, so that the deposits generated when cutting the wire saw are fine cutting powder (fine powder) and coarser grinding powder. Collected as a mixture containing grains (coarse powder) and cutting oil. In the wire saw cutting, the gallium compound content in the sediment was 10% by weight or less due to the large amount of abrasive grains used, and the gallium concentration was low.

【0004】そのため、ワイヤーソー切断の際に発生し
た上記澱物からガリウム分を回収しようとした場合、ガ
リウム化合物濃度の低い澱物に対して回収処理を施す必
要があることから、回収効率が悪く、経済的に見合わな
いため、従来、上記澱物は産業廃棄物として処分されて
いた。
[0004] Therefore, when gallium is to be recovered from the above-mentioned sediment generated at the time of cutting the wire saw, it is necessary to perform a recovery treatment on the sediment having a low concentration of the gallium compound. Conventionally, the above deposits have been disposed of as industrial waste because they are not economically viable.

【0005】しかし、不足しがちなガリウム資源を有効
に利用するという観点から、ワイヤーソー切断の際に発
生した澱物から経済的にガリウム分を回収する方法が強
く要望されていた。
[0005] However, from the viewpoint of effectively utilizing the gallium resources, which tend to be insufficient, there has been a strong demand for a method of economically recovering gallium from the deposits generated when cutting a wire saw.

【0006】この様な技術的背景の下、本出願人は、ガ
リウム化合物、砥粒および切削油を含む澱物からのガリ
ウム分を簡便に、かつ、著しく濃縮して回収する方法を
既に提案している(特願平11−76884号明細書参
照)。
Under such technical background, the present applicant has already proposed a method for simply and remarkably concentrating and recovering gallium content from a deposit containing a gallium compound, abrasive grains and cutting oil. (See Japanese Patent Application No. 11-76884).

【0007】すなわち、出願人が提案した上記方法は、
ガリウム化合物、砥粒および切削油を含む澱物からのガ
リウム分の濃縮方法であって、切削油と相溶しかつガリ
ウム化合物の熱分解温度より低い沸点を有する溶媒に上
記澱物内の切削油を溶解させると共に澱物内のガリウム
化合物と砥粒を分散させる第一工程と、上記ガリウム化
合物と砥粒が分散された溶媒から砥粒を除去するために
ガリウム分を主に含む細粉と砥粒を主に含む粗粉に湿式
分級して上記細粉が分散された溶媒を得る第二工程と、
上記細粉が分散された溶媒から溶媒を分離して細粉を得
る第三工程と、得られた上記細粉をガリウム化合物の熱
分解温度未満の温度で加熱して残留する上記溶媒を細粉
から除去する第四工程を具備することを特徴とするもの
であった。
That is, the method proposed by the applicant is as follows:
A method for concentrating gallium from a precipitate containing a gallium compound, abrasive grains and cutting oil, wherein the cutting oil in the precipitate is mixed with a solvent having a boiling point lower than a thermal decomposition temperature of the gallium compound and being compatible with the cutting oil. Dissolving the gallium compound and abrasive grains in the precipitate and dispersing the abrasive grains, and a fine powder mainly containing a gallium component and an abrasive for removing the abrasive grains from the solvent in which the gallium compound and the abrasive grains are dispersed. A second step of obtaining a solvent in which the fine powder is dispersed by wet classification into coarse powder mainly containing grains,
A third step of separating the solvent from the solvent in which the fine powder is dispersed to obtain fine powder, and heating the obtained fine powder at a temperature lower than the thermal decomposition temperature of the gallium compound to remove the remaining solvent into fine powder; And a fourth step of removing from the substrate.

【0008】[0008]

【発明が解決しようとする課題】ところで上記方法によ
れば、第二工程において澱物中のガリウム化合物の約9
0%が細粉として回収できるものの、主として砥粒から
なる粗粉にも、まだ約10%のガリウム化合物が含まれ
ていた。ところが、この粗粉は産業廃棄物として処分さ
れているため、回収されず、ガリウム化合物の回収率は
約90%が上限となっていた。
According to the above method, however, in the second step, about 9% of the gallium compound in the precipitate is removed.
Although 0% could be recovered as fine powder, coarse powder mainly composed of abrasive grains still contained about 10% of a gallium compound. However, since the coarse powder is disposed of as industrial waste, it is not recovered, and the recovery rate of the gallium compound is about 90% at the upper limit.

【0009】本発明はこのような問題点に着目してなさ
れたもので、その課題とするところは、ガリウム化合物
の回収率の更なる向上と、産業廃棄物の減量にある。
The present invention has been made in view of such problems, and has as its object to further improve the recovery rate of gallium compounds and reduce the amount of industrial waste.

【0010】[0010]

【課題を解決するための手段】すなわち、請求項1に係
る発明は、ガリウム化合物をワイヤーソーで切断した際
に発生するガリウム化合物、砥粒および切削油を含む澱
物からのガリウム分の濃縮方法において、切削油と相溶
しかつガリウム化合物の熱分解温度より低い沸点を有す
る溶媒に上記澱物内の切削油を溶解させると共に澱物内
のガリウム化合物と砥粒を分散させる第一工程と、上記
ガリウム化合物と砥粒が分散された溶媒を湿式分級し、
ガリウム化合物を主に含む細粉が分散された溶媒と砥粒
を主に含む粗粉が分散された溶媒とに分離する第二工程
と、第二工程で得られた細粉が分散された溶媒から溶媒
を分離して細粉を得る第三工程と、第二工程で得られた
粗粉が分散された溶媒から必要に応じて溶媒を除去した
後、第二工程において細粉として分離された砥粒量と同
量以下の砥粒を補充するとともに、粗粉および補充され
た砥粒に対する切削油の量を調整し、ガリウム化合物を
ワイヤーソー切断する際のスラリーとする第四工程を具
備することを特徴とするものである。
That is, the invention according to claim 1 is a method for concentrating gallium from a gallium compound, an abrasive, and a sediment containing cutting oil generated when the gallium compound is cut with a wire saw. In, a first step of dissolving the cutting oil in the precipitate and dispersing the gallium compound and abrasive grains in the precipitate in a solvent compatible with the cutting oil and having a boiling point lower than the thermal decomposition temperature of the gallium compound, Wet classification of the gallium compound and the solvent in which the abrasive grains are dispersed,
The second step of separating the solvent in which the fine powder mainly containing gallium compound is dispersed and the solvent in which the coarse powder mainly containing abrasive grains is dispersed, and the solvent in which the fine powder obtained in the second step is dispersed The third step of obtaining a fine powder by separating the solvent from the, the coarse powder obtained in the second step was removed as a fine powder in the second step after removing the solvent as necessary from the dispersed solvent A fourth step of replenishing abrasive grains equal to or less than the amount of abrasive grains, adjusting the amount of cutting oil for the coarse powder and the replenished abrasive grains, and preparing a slurry for cutting the gallium compound with a wire saw is provided. It is characterized by the following.

【0011】そして、請求項1記載の発明に係るガリウ
ム化合物の濃縮方法によれば、第二工程において粗粉と
して分離されたガリウム分も、粗粉を砥粒として繰り返
し再使用することにより、最終的には全て細粉として分
離、回収することができる。また、粗粉を砥粒として再
使用することにより、新規に使用される砥粒量が抑制さ
れるため、最終的に処分される産業廃棄物の量も減ずる
ことができる。
According to the method for concentrating gallium compounds according to the first aspect of the present invention, the gallium component separated as coarse powder in the second step can be finally reused by repeatedly using the coarse powder as abrasive grains. Specifically, all can be separated and recovered as fine powder. In addition, since the coarse powder is reused as abrasive grains, the amount of newly used abrasive grains is suppressed, so that the amount of industrial waste finally disposed of can be reduced.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施の形態につい
て詳細に説明する。
Embodiments of the present invention will be described below in detail.

【0013】まず、本発明に係るガリウム化合物の濃縮
方法は、以下の第一工程から第四工程を具備することを
特徴とするものである。
First, the method for concentrating a gallium compound according to the present invention comprises the following first to fourth steps.

【0014】(1)第一工程 この方法の第一工程では、切削油と相溶しかつガリウム
化合物の熱分解温度より低い沸点を有する溶媒に上記澱
物内の切削油を溶解させると共に澱物内のガリウム化合
物と砥粒を分散させる。
(1) First Step In the first step of the method, the cutting oil in the precipitate is dissolved in a solvent compatible with the cutting oil and having a boiling point lower than the thermal decomposition temperature of the gallium compound. Disperse the gallium compound and abrasive grains within.

【0015】ここで、澱物内のガリウム化合物と砥粒を
上記溶媒に分散させるのは以下の理由による。すなわ
ち、ワイヤーソー切断時における砥粒は、通常、切削油
に高濃度に分散されていることから上記澱物が高粘度で
あるため、澱物内のガリウム化合物と砥粒を溶媒に分散
させないと、第二工程における湿式分級による砥粒の除
去が不十分になる場合があるからである。
Here, the gallium compound and abrasive grains in the precipitate are dispersed in the solvent for the following reasons. That is, the abrasive grains at the time of wire saw cutting are usually dispersed in a high concentration in cutting oil, so that the above-mentioned precipitate has a high viscosity, so that the gallium compound and the abrasive grains in the precipitate must be dispersed in a solvent. This is because removal of abrasive grains by wet classification in the second step may be insufficient.

【0016】溶媒は、切削油と相溶しかつガリウム化合
物の熱分解温度より低い沸点を有するものであれば特に
制限はないが、切削油が好ましい(請求項2)。
The solvent is not particularly limited as long as it is compatible with the cutting oil and has a boiling point lower than the thermal decomposition temperature of the gallium compound, but cutting oil is preferable (claim 2).

【0017】第二工程における湿式分級の分離効率の点
からは、切削油よりも低粘度の溶媒、例えば灯油の方が
溶媒として適している。しかし、第二工程で分離される
粗粉は、第四工程においてワイヤーソー切断用のスラリ
ーとして再生されることになるが、その際、切削油より
低粘度の溶媒が残存していると、スラリーの粘度を適切
な値に調整することが困難となる。その点、溶媒が切削
油であれば、溶媒の量を調整する必要があったとして
も、除去する必要はなくなる。
From the viewpoint of the separation efficiency of the wet classification in the second step, a solvent having a lower viscosity than cutting oil, for example, kerosene, is more suitable as the solvent. However, the coarse powder separated in the second step is regenerated as a wire saw cutting slurry in the fourth step. At this time, if a solvent having a lower viscosity than the cutting oil remains, the slurry It is difficult to adjust the viscosity of the mixture to an appropriate value. In this regard, if the solvent is cutting oil, it is not necessary to remove the solvent even if the amount of the solvent needs to be adjusted.

【0018】尚、切削油や灯油の沸点には温度範囲が通
常あるが、温度範囲のある沸点の高低をいう場合に用い
る沸点は『沸点の上限』を本明細書では意味する。
The boiling point of cutting oil or kerosene usually has a temperature range, but the boiling point used when referring to the level of a certain boiling point in the temperature range means "the upper limit of the boiling point" in this specification.

【0019】(2)第二工程 第二工程では、ガリウム化合物と砥粒が分散された溶媒
から砥粒を除去するためにガリウム分を主に含む細粉と
砥粒を主に含む粗粉に湿式分級して上記細粉が分散され
た溶媒を得る。
(2) Second Step In the second step, in order to remove the abrasive grains from the solvent in which the gallium compound and the abrasive grains are dispersed, fine powder mainly containing gallium and coarse powder mainly containing abrasive grains are removed. Wet classification is performed to obtain a solvent in which the fine powder is dispersed.

【0020】ここで、湿式分級としては、自然沈降法、
上記細粉よりも大きな開口径を有するフィルタを用いた
濾過法も適用できるが、連続処理が可能で経済的な液体
サイクロンを用いた方法(請求項3)が適している。
尚、液体サイクロンにおける分級点の設定に関しては、
以下のような設定方法が例示される。すなわち、上記澱
物の一部を試料として採取し、かつ、採取した澱物を乾
燥させた後、この乾燥させた澱物を、ガリウム化合物を
溶解するエッチング液、例えば王水等で処理し、処理前
後の澱物の各粒度分布の比較(すなわち、ガリウム化合
物と砥粒が含まれた処理前の澱物の粒度分布と、ガリウ
ム化合物が除去された処理後の澱物の粒度分布の比較)
から澱物内に含まれるガリウム化合物の粒度分布を事前
に測定し、ガリウム化合物の最大粒径程度に設定すると
よい。
Here, the wet classification includes a natural sedimentation method,
Although a filtration method using a filter having a larger opening diameter than the fine powder can be applied, a method using a liquid cyclone that can be continuously processed and is economical (claim 3) is suitable.
In addition, regarding the setting of the classification point in the hydrocyclone,
The following setting method is exemplified. That is, a part of the precipitate is collected as a sample, and after the collected precipitate is dried, the dried precipitate is treated with an etchant that dissolves a gallium compound, such as aqua regia, Comparison of each particle size distribution of the precipitate before and after the treatment (that is, comparison of the particle size distribution of the precipitate before the treatment containing the gallium compound and the abrasive grains and the particle size distribution of the precipitate after the treatment with the gallium compound removed)
The particle size distribution of the gallium compound contained in the sediment is preferably measured in advance and set to about the maximum particle size of the gallium compound.

【0021】(3)第三工程 第三工程では、細粉が分散された溶媒から溶媒を分離し
てガリウム分を主に含む上記細粉を得る。
(3) Third Step In the third step, the solvent is separated from the solvent in which the fine powder is dispersed to obtain the fine powder mainly containing gallium.

【0022】ここで、細粉が分散された溶媒から溶媒を
分離する手段としては、自然沈降法、上記細粉よりも小
さな開口径を有するフィルタを用いた濾過法も適用でき
るが、連続処理が可能で経済的なデカンタ型遠心分離装
置を用いた方法が適している。より経済的な観点から、
デカンタ型遠心分離装置により分離された溶媒について
は、第一工程の溶媒として再利用することが好ましい。
Here, as a means for separating the solvent from the solvent in which the fine powder is dispersed, a natural sedimentation method and a filtration method using a filter having a smaller opening diameter than the fine powder can be applied. Suitable and economical methods using decanter centrifuges are suitable. From a more economic perspective,
The solvent separated by the decanter-type centrifugal separator is preferably reused as the solvent in the first step.

【0023】尚、第三工程で得られた細粉からは、細粉
を酸に溶解した後中和して、ガリウム分を一旦水酸化ガ
リウムとし、その後、水酸化ガリウムをアルカリ性溶液
に溶解し、電解することで金属ガリウムが回収できる。
From the fine powder obtained in the third step, the fine powder is dissolved in an acid and then neutralized to convert the gallium content into gallium hydroxide, and then the gallium hydroxide is dissolved in an alkaline solution. The metal gallium can be recovered by electrolysis.

【0024】(4)第四工程 第四工程では、第二工程で得られた粗粉が分散された溶
媒から必要に応じて溶媒を除去した後、第二工程におい
て細粉として分離された砥粒量と同量の砥粒を補充する
とともに、粗粉および補充された砥粒に対する切削油の
量を調整し、ガリウム化合物をワイヤーソー切断する際
のスラリーとする。
(4) Fourth Step In the fourth step, after removing the solvent as necessary from the solvent in which the coarse powder obtained in the second step is dispersed, the abrasive powder separated as fine powder in the second step is removed. The same amount of abrasive grains as the amount of grains is replenished, and the amount of cutting oil for the coarse powder and the replenished abrasive grains is adjusted to obtain a slurry for cutting the gallium compound with a wire saw.

【0025】ここで、必要に応じてというのは、第一工
程で添加した溶媒が切削油以外の低粘度の溶媒である場
合は、切削特性に悪影響を与えない程度まで粗粉から溶
媒を除去する必要があるが、溶媒が切削油の場合は必ず
しも除去する必要がないからである。
Here, if necessary, when the solvent added in the first step is a solvent having a low viscosity other than the cutting oil, the solvent is removed from the coarse powder to such an extent that the cutting characteristics are not adversely affected. However, when the solvent is cutting oil, it is not necessary to remove the solvent.

【0026】また、本工程では細粉とともに分離された
砥粒量と同量以下の砥粒を補充する。粗粉量が十分で有
れば必ずしも新品の砥粒を補充する必要はないが、細粉
とともに分離された砥粒量と同量補充する場合も厳密に
同量である必要はない。湿式分級によって細粉として分
離される固形分の分析値から、事前に細粉として分離さ
れてしまう砥粒量を計算しておき、計算された値分、砥
粒を補充してもよい。
Further, in this step, abrasive particles having the same amount or less as the amount of the separated abrasive particles together with the fine powder are replenished. If the amount of coarse powder is sufficient, it is not always necessary to replenish the new abrasive grains, but it is not necessary that the amount is exactly the same when replenishing the same amount as the amount of abrasive grains separated together with the fine powder. The amount of abrasive grains separated as fine powder may be calculated in advance from the analysis value of solids separated as fine powder by wet classification, and abrasive grains may be supplemented by the calculated value.

【0027】また、上記澱物中にワイヤーソーのワイヤ
ー片など磁性物が含まれている場合には、この磁性物を
除去することが好ましい。具体的には、第一工程、第二
工程および第三工程の少なくとも一つの工程時に、溶媒
内に含まれるワイヤー片などの磁性物を磁石を用いて除
去する(請求項4)。この除去処理により、第三工程で
得られた細粉を原料として金属ガリウムを得る際に、金
属ガリウムの不純物濃度を下げるための繁雑な脱Fe処
理を省略することが可能となる。
When a magnetic material such as a wire piece of a wire saw is contained in the above-mentioned sediment, it is preferable to remove the magnetic material. Specifically, in at least one of the first step, the second step, and the third step, a magnetic substance such as a wire piece contained in the solvent is removed using a magnet (claim 4). By this removal treatment, when obtaining the metal gallium using the fine powder obtained in the third step as a raw material, it is possible to omit a complicated de-Fe treatment for reducing the impurity concentration of the metal gallium.

【0028】さらに、第二工程で分離された粗粉には異
物が混入することがあるが、砥粒径よりも大きな異物が
スラリー中に混入すると切削特性に悪影響を及ぼすの
で、このような異物は除去することが好ましい。具体的
には、第一工程、第二工程および第四工程の少なくとも
一つの工程時において、固形分をフィルターでろ過する
(請求項5)。
Further, foreign matter may be mixed in the coarse powder separated in the second step. However, if foreign matter larger than the abrasive particle diameter is mixed in the slurry, the cutting characteristics are adversely affected. Is preferably removed. Specifically, in at least one of the first step, the second step, and the fourth step, the solid content is filtered with a filter (claim 5).

【0029】このように本発明に係る濃縮方法によれ
ば、粗粉をスラリーとして再使用するため、粗粉として
分離されたガリウム化合物は、再度ガリウム化合物の濃
縮工程に回され、産業廃棄物として処分されることな
く、最終的には細粉として回収できるようになる。ま
た、産業廃棄物として処分されるのは、細粉として分離
された砥粒に限られるため、産業廃棄物の量も減ずるこ
とができる。
As described above, according to the concentration method of the present invention, since the coarse powder is reused as a slurry, the gallium compound separated as the coarse powder is returned to the concentration step of the gallium compound again to produce industrial waste. It will eventually be collected as fine powder without being disposed of. Further, since only the abrasive grains separated as fine powder are disposed of as industrial waste, the amount of industrial waste can be reduced.

【0030】[0030]

【実施例】以下、本発明の実施例について具体的に説明
する。
Embodiments of the present invention will be specifically described below.

【0031】リン化ガリウム単結晶(熱分解温度:68
0℃)18本をワイヤーソーで切断した際に切削屑とし
て発生した澱物を以下のように処理した。尚、この澱物
は、リン化ガリウムの切削粉、SiCが主成分の砥粒、
および切削油(沸点:200〜400℃)を含む。この
澱物を分析した結果を以下の表1に示す。
Gallium phosphide single crystal (pyrolysis temperature: 68
(0 ° C.) The deposits generated as cutting chips when 18 pieces were cut with a wire saw were treated as follows. In addition, this deposit is a cutting powder of gallium phosphide, abrasive grains mainly composed of SiC,
And cutting oil (boiling point: 200 to 400 ° C.). The results of analyzing the precipitate are shown in Table 1 below.

【0032】[0032]

【表1】 [Table 1]

【0033】また、この澱物の一部を資料として採取
し、かつ、採取した澱物を乾燥させた後、この乾燥させ
た澱物を王水で処理し、王水エッチング処理前後の澱物
の粒度分布を図1に示す。そして、図1に示されたリン
化ガリウムと砥粒が含まれたエッチング前の粒度分布
と、リン化ガリウムが除去されたエッチング後の粒度分
布との比較から、澱物内に含まれるリン化ガリウムは5
μm以下の粒径であると推察される。
Further, a part of the precipitate is collected as a material, and the collected precipitate is dried. The dried precipitate is treated with aqua regia, and the precipitate before and after the aqua regia etching treatment is performed. Is shown in FIG. From the comparison between the particle size distribution before etching containing gallium phosphide and abrasive grains shown in FIG. 1 and the particle size distribution after etching with gallium phosphide removed, the phosphidization contained in the sediment was confirmed. Gallium is 5
It is presumed that the particle size is not more than μm.

【0034】まず、上記澱物56.1kg(ガリウム化
合物含有量5122g)を切削油375リットル内に投
入し、攪拌・分散後、永久磁石を入れ磁石に吸着された
ものを除去して分散液を得た。
First, 56.1 kg of the above-mentioned sediment (gallium compound content: 5122 g) was put into 375 liters of cutting oil, and after stirring and dispersion, a permanent magnet was put in to remove the material adsorbed by the magnet, and the dispersion was dispersed. Obtained.

【0035】次に、得られた分散液を、100μmフィ
ルタでろ過し、粗大粒子を除去後、液体サイクロンによ
り5μmを境として分級し、ガリウム分を主に含む上流
分散液(細粉が含まれる)約355リットルと、砥粒を
主に含む下流分散液(粗粉が含まれる)約39リットル
を得た。
Next, the obtained dispersion is filtered with a 100 μm filter to remove coarse particles, and then classified using a liquid cyclone at a boundary of 5 μm to obtain an upstream dispersion mainly containing gallium (including fine powder). ) About 355 liters and about 39 liters of a downstream dispersion (including coarse powder) mainly containing abrasive grains were obtained.

【0036】この分級処理で得られた細粉を含む上流分
散液約355リットルを、デカンタ型遠心分離装置を用
いて遠心加速度3200G、滞留時間60秒の条件で遠
心分離し、12.8kg(ガリウム化合物含有量459
5g)の固形分を得た。また、粗粉を含む下流分散液約
39リットルを静置し、固形分を自然沈降させ、上澄み
の切削油を除去して45.5kg(ガリウム化合物含有
量514g)の固形分を得た。
About 355 liters of the upstream dispersion containing fine powder obtained by this classification was centrifuged using a decanter-type centrifugal separator under the conditions of a centrifugal acceleration of 3200 G and a residence time of 60 seconds to obtain 12.8 kg (gallium). Compound content 459
5 g) of a solid was obtained. Further, about 39 liters of the downstream dispersion containing the coarse powder was allowed to stand, and the solid content was allowed to settle by itself, and the cutting oil in the supernatant was removed to obtain 45.5 kg (514 g of a gallium compound content).

【0037】上流分散液固形分および下流分散液固形分
を分析した結果を以下の表2に示す。
The results of analyzing the solid content of the upstream dispersion and the solid content of the downstream dispersion are shown in Table 2 below.

【0038】[0038]

【表2】 [Table 2]

【0039】次に、下流分散液固形分に上流分散液固形
分中の砥粒重量、すなわち細粉として分離された砥粒重
量と同じ重量の新品砥粒を6.78kg補充後、切削油
を添加して比重調整を行い、再びワイヤーソー切断のス
ラリーとしてリン化ガリウム単結晶18本の切断に使用
した。なお、切断特性は新品の砥粒から調合したスラリ
ー使用時と差は見られなかった。
Next, after adding 6.78 kg of new abrasive grains having the same weight as the weight of the abrasive grains in the solid content of the upstream dispersion liquid, that is, the weight of the abrasive grains separated as fine powder, the cutting oil was added to the solid content of the downstream dispersion liquid. After the addition, the specific gravity was adjusted, and the slurry was again used as a slurry for wire saw cutting for cutting 18 gallium phosphide single crystals. It should be noted that the cutting characteristics were not different from those when using a slurry prepared from new abrasive grains.

【0040】切断後の澱物を放置し、固形分を自然沈降
させた後、上澄みの切削油を除去して得た2回目の澱物
の分析結果を表3に示す。
The cut precipitate was allowed to stand, the solid content was allowed to settle, and the cutting oil in the supernatant was removed. The results of the second precipitate analysis are shown in Table 3.

【0041】[0041]

【表3】 [Table 3]

【0042】上記澱物57.1kg(ガリウム化合物含
有量5636g)を1回目の澱物処理と同様の方法で処
理し、13.0kg(ガリウム化合物含有量5122
g)の上流分散液固形分と45.9kg(ガリウム化合
物含有量505g)の下流分散液固形分を得た。上流分
散液固形分と下流分散液固形分の分析結果を表4に示
す。
57.1 kg of the above-mentioned precipitate (gallium compound content: 5636 g) was treated in the same manner as in the first treatment of the precipitate, and 13.0 kg (gallium compound content: 5122 g) was obtained.
g) of the upstream dispersion solid content and 45.9 kg (gallium compound content 505 g) of the downstream dispersion solid content were obtained. Table 4 shows the analysis results of the solid content of the upstream dispersion and the solid content of the downstream dispersion.

【0043】[0043]

【表4】 [Table 4]

【0044】表2と表4の下流分散液固形分の含有率の
比較から分かるように、粗粉をスラリーとして再使用し
ても、粗粉中にガリウム化合物が濃縮されることはな
く、再使用を繰り返せば、ガリウム化合物は最終的に細
粉として回収されることがわかる。
As can be seen from the comparison of the content of the solid content of the downstream dispersion in Tables 2 and 4, even if the coarse powder is reused as a slurry, the gallium compound is not concentrated in the coarse powder. It can be seen that the gallium compound is ultimately recovered as fine powder by repeated use.

【0045】[0045]

【発明の効果】このように本発明に係る澱物からのガリ
ウム化合物の濃縮方法によれば、湿式分級後の粗粉をス
ラリーとして再使用することによって、粗粉として分離
されるガリウム化合物も、最終的には細粉として回収で
きるようになる。また、産業廃棄物として処分されるの
は、細粉として分離された砥粒に限られるため、産業廃
棄物の量も減ずることができる。
As described above, according to the method for concentrating gallium compounds from sediments according to the present invention, the gallium compounds separated as coarse powders by reusing the coarse powder after wet classification as a slurry can be obtained. Eventually, it can be recovered as fine powder. Further, since only the abrasive grains separated as fine powder are disposed of as industrial waste, the amount of industrial waste can be reduced.

【図面の簡単な説明】[Brief description of the drawings]

【図1】王水エッチング前後の澱物の粒度分布を示すグ
ラフ図。
FIG. 1 is a graph showing the particle size distribution of a precipitate before and after aqua regia etching.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C01B 25/08 C01B 25/08 C22B 1/00 601 C22B 1/00 601 7/00 7/00 H 58/00 58/00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C01B 25/08 C01B 25/08 C22B 1/00 601 C22B 1/00 601 7/00 7/00 H58 / 00 58/00

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】ガリウム化合物をワイヤーソーで切断した
際に発生するガリウム化合物、砥粒および切削油を含む
澱物からのガリウム分の濃縮方法において、切削油と相
溶しかつガリウム化合物の熱分解温度より低い沸点を有
する溶媒に上記澱物内の切削油を溶解させると共に澱物
内のガリウム化合物と砥粒を分散させる第一工程と、上
記ガリウム化合物と砥粒が分散された溶媒を湿式分級
し、ガリウム化合物を主に含む細粉が分散された溶媒と
砥粒を主に含む粗粉が分散された溶媒とを得る第二工程
と、第二工程で得られた細粉が分散された溶媒から溶媒
を分離して細粉を得る第三工程と、第二工程で得られた
粗粉が分散された溶媒から必要に応じて溶媒を除去した
後、第二工程において細粉として分離された砥粒量と同
量以下の砥粒を補充するとともに、粗粉および補充され
た砥粒に対する切削油の量を調整し、ガリウム化合物を
ワイヤーソー切断する際のスラリーとする第四工程を具
備することを特徴とするガリウム化合物、砥粒および切
削油を含む澱物からのガリウム化合物の濃縮方法。
In a method of concentrating gallium from a gallium compound generated when a gallium compound is cut by a wire saw, a grit containing abrasive grains and cutting oil, the gallium compound is compatible with cutting oil and thermally decomposes the gallium compound. A first step of dissolving the cutting oil in the precipitate in a solvent having a boiling point lower than the temperature and dispersing the gallium compound and the abrasive grains in the precipitate, and wet classifying the solvent in which the gallium compound and the abrasive grains are dispersed. And the second step of obtaining a solvent in which the fine powder mainly containing the gallium compound is dispersed and the solvent in which the coarse powder mainly containing the abrasive grains is dispersed, the fine powder obtained in the second step is dispersed. The third step of separating the solvent from the solvent to obtain a fine powder, the coarse powder obtained in the second step after removing the solvent as necessary from the dispersed solvent is separated as fine powder in the second step Replenish abrasive particles less than the same amount Gallium compound, abrasive grains and cutting, characterized by comprising a fourth step of adjusting the amount of cutting oil with respect to the coarse powder and the replenished abrasive grains and making the slurry when the gallium compound is cut with a wire saw. A method for concentrating a gallium compound from an oil-containing precipitate.
【請求項2】上記第一工程における溶媒が切削油である
ことを特徴とする請求項1記載のガリウム化合物、砥粒
および切削油を含む澱物からのガリウム化合物の濃縮方
法。
2. The method according to claim 1, wherein the solvent used in the first step is a cutting oil.
【請求項3】液体サイクロンを用いて上記第二工程にお
ける湿式分級を行うことを特徴とする請求項1または2
記載のガリウム化合物、砥粒および切削油を含む澱物か
らのガリウム化合物の濃縮方法。
3. The method according to claim 1, wherein the wet classification in the second step is performed using a liquid cyclone.
A method for concentrating a gallium compound from a deposit containing the gallium compound, abrasive grains and cutting oil described in the above.
【請求項4】第一工程、第二工程および第三工程の少な
くとも一つの工程時に、磁石を用いて上記澱物中に含ま
れる磁性物を除去することを特徴とする請求項1〜3の
いずれかに記載のガリウム化合物、砥粒および切削油を
含む澱物からのガリウム化合物の濃縮方法。
4. The method according to claim 1, wherein at least one of the first step, the second step and the third step removes a magnetic substance contained in the precipitate using a magnet. A method for concentrating a gallium compound from a precipitate containing the gallium compound, abrasive grains and cutting oil according to any one of the above.
【請求項5】第一工程、第二工程および第四工程の少な
くとも一つの工程時に、最大砥粒径以上の異物を除去す
る手段を有することを特徴とする請求項1〜4のいずれ
かに記載のガリウム化合物、砥粒および切削油を含む澱
物からのガリウム化合物の濃縮方法。
5. The method according to claim 1, further comprising: means for removing foreign matters having a maximum abrasive grain size or more in at least one of the first step, the second step, and the fourth step. A method for concentrating a gallium compound from a deposit containing the gallium compound, abrasive grains and cutting oil described in the above.
JP2000054347A 2000-02-25 2000-02-25 Method for concentrating gallium compound from sediment containing gallium compound, abrasive grains and cutting oil Expired - Fee Related JP3436304B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000054347A JP3436304B2 (en) 2000-02-25 2000-02-25 Method for concentrating gallium compound from sediment containing gallium compound, abrasive grains and cutting oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000054347A JP3436304B2 (en) 2000-02-25 2000-02-25 Method for concentrating gallium compound from sediment containing gallium compound, abrasive grains and cutting oil

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011074475A (en) * 2009-10-01 2011-04-14 Sumitomo Electric Ind Ltd Method for recovering gallium

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011074475A (en) * 2009-10-01 2011-04-14 Sumitomo Electric Ind Ltd Method for recovering gallium

Also Published As

Publication number Publication date
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