JP3134189B2 - How to collect abrasives - Google Patents

How to collect abrasives

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Publication number
JP3134189B2
JP3134189B2 JP09253620A JP25362097A JP3134189B2 JP 3134189 B2 JP3134189 B2 JP 3134189B2 JP 09253620 A JP09253620 A JP 09253620A JP 25362097 A JP25362097 A JP 25362097A JP 3134189 B2 JP3134189 B2 JP 3134189B2
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JP
Japan
Prior art keywords
polishing
abrasive
waste
alkali metal
aqueous solution
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.)
Expired - Fee Related
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JP09253620A
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Japanese (ja)
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JPH1190825A (en
Inventor
和裕 加藤
Original Assignee
福島県
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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、研磨材で光学ガラ
スや水晶発振子などを精密研磨した後に生じる、使用済
みの研磨廃棄物を原料として、これから研磨材を回収す
る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 recovering an abrasive from a used abrasive waste generated after precision polishing of an optical glass or a crystal oscillator with an abrasive.

【0002】[0002]

【従来の技術】現在使用されている光学ガラスや水晶発
振子を仕上工程で精密研磨する研磨材としては、酸化セ
リウムを主成分とし、これに酸化ランタン、酸化ネオジ
ム、酸化プラセオジムなどが加わった希土類元素酸化物
が使用されている。従来の酸化セリウムを主成分とした
研磨材の製造方法としては、希土類鉱石を粉砕・分級
後、化学処理して得られたケーキを乾燥・焼成し、更に
粉砕・分級して製造する方法や、希土類鉱石の粉砕物を
化学処理して得られた塩化希土水溶液から、水酸化セリ
ウムを主成分とするセリウム濃縮物を製造して、これを
乾燥・焼成し、更に粉砕・分級して製造するなどの方法
が行われていた。
2. Description of the Related Art Currently used abrasives for precisely polishing optical glass and quartz oscillators in a finishing process are mainly cerium oxide, and rare earth elements containing lanthanum oxide, neodymium oxide, praseodymium oxide, etc. Elemental oxides are used. As a conventional method for producing an abrasive containing cerium oxide as a main component, after pulverizing and classifying a rare earth ore, a method of producing a cake obtained by chemical treatment by drying and firing, and further pulverizing and classifying, From a rare earth chloride aqueous solution obtained by chemically treating a pulverized rare earth ore, a cerium concentrate containing cerium hydroxide as a main component is manufactured, dried, calcined, and further pulverized and classified to produce. And so on.

【0003】光学ガラスや水晶振動子を仕上研磨する場
合には、酸化セリウムを主成分とする研磨材のスラリー
を噴射しながら、回転する研磨布に押し付けて精密研磨
している。研磨材のスラリーは循環させながら繰り返し
使用し、ガラス粉や研磨布の繊維、ごみなどが混入して
次第に研磨性能が低下してきたら、新しい研磨材と交換
している。使用済の研磨材のスラリーは、これに凝集剤
を添加して沈殿させ、脱水してケーキ状の研磨廃棄物と
されている。このように仕上の精密研磨に使用する研磨
材として用いられている酸化セリウムなどの希土類酸化
物は比較的軟質であり、研磨によって粒子形状が崩れて
研磨性能が低下してくると従来は考えられていたので、
使用済の研磨廃棄物はそのまま、産業廃棄物として埋め
立て処理されていた。
In the case of finish polishing an optical glass or a quartz oscillator, precision polishing is performed by pressing against a rotating polishing cloth while spraying a slurry of an abrasive mainly composed of cerium oxide. The abrasive slurry is repeatedly used while being circulated, and when the polishing performance gradually decreases due to mixing of glass powder, fibers of the polishing cloth, dust and the like, the abrasive is replaced with a new abrasive. The slurry of the used abrasive is precipitated by adding a coagulant to the slurry and dehydrated to obtain cake-like polishing waste. As described above, rare earth oxides such as cerium oxide used as an abrasive used for precision polishing of finishes are relatively soft, and it is conventionally thought that the particle shape is destroyed by polishing and polishing performance is reduced. Because it was
The used polishing waste was directly landfilled as industrial waste.

【0004】しかしながら研磨材の主構成元素である希
土類元素は世界的にも偏在しており、我が国では全面的
に輸入に依存しているので、安定供給に不安な点もあ
る。また使用済の研磨廃棄物はケーキ状で70〜85%
程度の多量の水分が含み、埋立などその処分費用も1ト
ン当たり数万円と高く、しかも埋立処分場も少なくなっ
ていることから今後の対策が必要となってきていた。
[0004] However, rare earth elements, which are the main constituent elements of abrasives, are unevenly distributed in the world, and Japan is entirely dependent on imports. Used polishing waste is 70-85% in cake form
Since it contains a large amount of water, the disposal costs for landfills are as high as tens of thousands of yen per ton, and the number of landfill sites is small, so future measures are needed.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記問題点に
鑑み種々の研究を行った結果、使用済の研磨廃棄物から
回収した研磨材の粒子は、研磨後においても粒子が崩れ
ておらず、再利用できることを見い出し、これを効率よ
く回収して希土類元素の省資源化を図ると同時に、研磨
廃棄物の減量化と廃棄コストの低減を図った研磨材の回
収方法を提供するものである。
SUMMARY OF THE INVENTION In view of the above problems, the present invention has conducted various studies. As a result, the particles of the abrasive recovered from the used polishing waste did not collapse even after polishing. The present invention provides a method for recovering abrasives that aims to reduce the amount of polishing waste and reduce disposal costs while at the same time finding that it can be reused and efficiently recovering it to save resources of rare earth elements. .

【0006】[0006]

【課題を解決するための手段】本発明の請求項1記載の
研磨材の回収方法は、研磨材として酸化セリウムを主成
分とする使用済の研磨材スラリーを回収して、ここに凝
集剤を添加して固形分を凝縮した後、脱水処理して脱水
ケーキ状の研磨廃棄物を製造し、この研磨廃棄物を原料
として、アルカリ金属水酸化物を、その濃度が6モル/
リットル以下の水溶液に、前記研磨廃棄物を混合して可
溶性の不純物を溶解した後、この不純物が溶解した水溶
液と固形分とを分離し、次いでこの分離した固形分を篩
分けして、ガラス粉や研磨布の繊維、ごみなどの混入物
を分離し、微細な研磨材を回収することを特徴とするも
のである。
According to a first aspect of the present invention, there is provided a method for recovering an abrasive, wherein a used abrasive slurry containing cerium oxide as a main component is recovered as an abrasive, and a coagulant is added thereto. After adding and condensing the solid content, dehydration treatment is performed to produce a dewatered cake-like polishing waste. Using this polishing waste as a raw material, an alkali metal hydroxide having a concentration of 6 mol /
After dissolving the soluble impurities by mixing the polishing waste with an aqueous solution of 1 liter or less, the aqueous solution in which the impurities were dissolved and the solid content were separated, and then the separated solid content was sieved to obtain glass powder. It is characterized by separating contaminants such as fibers and dust of polishing cloth and dust, and collecting fine abrasives.

【0007】更に本発明の請求項2記載の研磨剤の回収
方法は、アルカリ金属水酸化物として、乾物ベースで研
磨廃棄物の5倍以上の重量の水酸化ナトリウムまたは7
倍以上の水酸化カリウムを用いたことを特徴とするもの
である。
Further, the method for recovering an abrasive according to the second aspect of the present invention is characterized in that, as the alkali metal hydroxide, sodium hydroxide or sodium hydroxide having a weight of 5 times or more of the polishing waste on a dry matter basis.
It is characterized by using potassium hydroxide twice or more times.

【0008】[0008]

【発明の実施の形態】以下本発明の実施の形態を詳細に
説明する。使用済の研磨廃棄物は研磨材の主成分である
酸化セリウムの他に酸化ランタン、酸化ネオジム、酸化
プラセオジムなどの希土類酸化物が含まれている。また
研磨廃棄物にはこの他に研磨されたガラス分であるケイ
素化合物や、添加された凝集剤のアルミニウム化合物、
砕かれて細かくなったガラス粉や研磨布の繊維、ごみな
どが混入している。また使用される凝集剤としては、ポ
リ塩化アルミニウムや硫酸アルミニウム、高分子凝集剤
が一般的であり、これらを単独または併用して使用され
ている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be described below in detail. The used polishing waste contains rare earth oxides such as lanthanum oxide, neodymium oxide and praseodymium oxide in addition to cerium oxide which is a main component of the abrasive. In addition, the polishing waste also includes a silicon compound that is a polished glass component, an aluminum compound of an added flocculant,
Glass powder that has been broken down into fine pieces, fibers of polishing cloth, dust and the like are mixed. As the flocculant to be used, polyaluminum chloride, aluminum sulfate, and a polymer flocculant are generally used, and these are used alone or in combination.

【0009】また研磨廃棄物の成分割合は、乾物ベース
で研磨材である希土類酸化物が約60重量%程度、ケイ
素化合物が約12重量%、凝集剤として添加したアルミ
ニウム化合物が約20重量%、その他ガラス粉や研磨布
の繊維、ごみなどである。
[0009] Further, the composition ratio of the polishing waste is about 60% by weight of a rare earth oxide as an abrasive, about 12% by weight of a silicon compound, about 20% by weight of an aluminum compound added as a coagulant, on a dry matter basis. Other examples include glass powder, polishing cloth fibers, and garbage.

【0010】以下、方法について説明すると、循環させ
ながら繰り返し使用して次第に研磨性能が低下してき
た、酸化セリウムを主成分とする研磨材スラリーを回収
して、ここに凝集剤を添加して固形分を凝縮した後、脱
水処理して水分約70〜85重量%の脱水ケーキ状の研
磨廃棄物を製造する。次に規定量以上のアルカリ金属水
酸化物を、その濃度が6モル/リットル以下の水溶液と
し、前記研磨廃棄物を混合して可溶性の不純物を溶解さ
せる。
The method will be described below. A polishing slurry containing cerium oxide as a main component, whose polishing performance has been gradually reduced after repeated use while being circulated, is recovered, and a coagulant is added thereto to obtain a solid content. Is condensed and dewatered to produce a dewatered cake-like abrasive waste having a water content of about 70 to 85% by weight. Next, a predetermined amount or more of alkali metal hydroxide is converted into an aqueous solution having a concentration of 6 mol / liter or less, and the polishing waste is mixed to dissolve soluble impurities.

【0011】この場合、使用するアルカリ金属水酸化物
としては、例えば水酸化ナトリウムまたは水酸化カリウ
ムを用いると安価で効果的である。このアルカリ金属水
酸化物の混合量は水酸化ナトリウムで研磨廃棄物の乾物
ベースで5倍以上、水酸化カリウムで7倍以上の重量と
することにより、研磨廃棄物に混合しているケイ素化合
物や、凝集剤として添加したアルミニウム化合物など可
溶性の不純物を溶解させることができる。
In this case, it is inexpensive and effective to use, for example, sodium hydroxide or potassium hydroxide as the alkali metal hydroxide to be used. The mixing amount of the alkali metal hydroxide is 5 times or more based on the dry matter of the polishing waste with sodium hydroxide, and 7 times or more with potassium hydroxide, so that the silicon compound mixed with the polishing waste can be obtained. In addition, soluble impurities such as an aluminum compound added as a coagulant can be dissolved.

【0012】この場合、アルカリ金属の水酸化物混合量
が規定量未満では、可溶性の不純物を十分に除去するこ
とができない。またアルカリ金属水酸化物濃度が6モル
/リットルを超えると、M−Si−Al複合酸化物
(M;Na、K)や複合水酸化物が生成して不純物が溶
解しない。また生成した複合生成物の粒子は希土類酸化
物に比べて硬度が高く、これが研磨材中に混入すると、
仕上の精密研磨工程で光学ガラスや水晶発振子の表面に
傷を付ける問題があるので上記範囲に限定した。
In this case, if the mixing amount of the hydroxide of the alkali metal is less than the specified amount, the soluble impurities cannot be sufficiently removed. When the alkali metal hydroxide concentration exceeds 6 mol / liter, M-Si-Al composite oxides (M; Na, K) and composite hydroxides are formed, and impurities are not dissolved. Also, the resulting composite product particles have a higher hardness than the rare earth oxide, and when this is mixed into the abrasive,
Since there is a problem of scratching the surface of the optical glass or the crystal oscillator in the finishing precision polishing step, the range is limited to the above range.

【0013】このようにアルカリ金属水酸化物の水溶液
を研磨廃棄物に混合して化学処理し、可溶性の不純物を
溶解した後、遠心分離装置でこの水溶液と固形分とを分
離する。分離した水溶液中には、研磨されたガラス分で
あるケイ素分や、添加された凝集剤のアルミニウム分が
溶解している。
As described above, the aqueous solution of the alkali metal hydroxide is mixed with the polishing waste and subjected to chemical treatment to dissolve soluble impurities. Then, the aqueous solution and the solid content are separated by a centrifugal separator. In the separated aqueous solution, a silicon component, which is a polished glass component, and an aluminum component, which is an added coagulant, are dissolved.

【0014】また分離した固形分には、研磨材粒子のほ
か、溶解しなかったガラス粉や研磨布の繊維、ごみなど
が含まれている。この固形分を洗浄液が中性となるまで
水洗いしてから、乾燥させた後、篩分けして数μm以下
の研磨材粒子とこれより大きいガラス粉や研磨布の繊
維、ごみなどを分離して、除去する。この場合、凝集剤
は既にアルカリ金属水酸化物の水溶液で分解されている
ので、固形分は崩れやすく分散が良くなっており、篩分
作業を容易に行うことができる。
[0014] The separated solid content contains, in addition to the abrasive particles, undissolved glass powder, fibers of a polishing cloth, dust, and the like. This solid content is washed with water until the washing liquid becomes neutral, and then dried and then sieved to separate abrasive particles of several μm or less from glass powder or fibers of a polishing cloth larger than this, and dust and the like. ,Remove. In this case, since the flocculant has already been decomposed with the aqueous solution of the alkali metal hydroxide, the solid content is easily broken and the dispersion is good, so that the sieving operation can be easily performed.

【0015】このようにして分離回収された微細粒子
は、不純物として残留しているケイ素分やアルミニウム
分が酸化物換算で約2重量%程度である。しかも回収し
た酸化セリウムなどの希土類酸化物粒子を顕微鏡観察し
たところ、粒子形状は崩れておらず、新品と同様であ
り、研磨性能についても新品とほぼ同様であることが確
認された。
In the fine particles separated and recovered in this way, silicon and aluminum remaining as impurities are about 2% by weight in terms of oxide. In addition, microscopic observation of the recovered rare earth oxide particles such as cerium oxide confirmed that the particle shape was not distorted and was the same as that of a new product, and that the polishing performance was almost the same as that of the new product.

【0016】[0016]

【実施例】以下本発明の実施例について説明する。希土
類鉱石を粉砕・分級後、化学処理して得られたケーキを
乾燥・焼成し、更に粉砕・分級して製造した酸化物換算
でセリウム分約45重量%、ランタン分約25重量%、
ネオジム分約10重量%、プラセオジム分約3重量%の
混合成分からなる新品の研磨材をスラリー状にして光学
ガラスの研磨を行った。繰り返し循環させながら使用し
て研磨材スラリーの研磨性能が低下してきたらこれを回
収した。次にこの回収した研磨材スラリーに、凝集材と
なるポリ塩化アルミニウムと高分子凝集剤を添加してス
ラリーに含まれる固形分を凝集した後、脱水処理して水
分約85%の脱水ケーキ状の研磨廃棄物を得た。
Embodiments of the present invention will be described below. After pulverizing and classifying the rare earth ore, the cake obtained by the chemical treatment is dried and calcined, and then pulverized and classified, and the cerium content is about 45% by weight and the lanthanum content is about 25% by weight in terms of oxide.
The optical glass was polished with a new abrasive made of a mixed component containing about 10% by weight of neodymium and about 3% by weight of praseodymium. When the polishing performance of the abrasive slurry was reduced while being used while being repeatedly circulated, it was collected. Next, a polyaluminum chloride as a flocculant and a polymer flocculant are added to the recovered abrasive slurry to coagulate the solids contained in the slurry, and then dewatered to form a dewatered cake having a water content of about 85%. Polishing waste was obtained.

【0017】次に表1の試料No1〜No3に示すよう
に、研磨廃棄物の乾物ベースで5〜10倍の重量の水酸
化ナトリウム(NaOH)を蒸留水に溶解し、2〜6モ
ル/リットルの範囲の水溶液を調製し、これに50gの
研磨廃棄物の脱水ケーキを混合、化学処理をした。可溶
性の不純物を溶解した後、遠心分離装置でこの不純物が
溶解した水溶液と固形分を分離した。次にこの固形分を
洗浄液が中性になるまで水洗いしてから、乾燥させた
後、篩分けして数μm以下の研磨材粒子とこれより大き
いガラス粉や研磨布の繊維、ごみなどを分離して、除去
した。
Next, as shown in Samples No. 1 to No. 3 in Table 1, 5 to 10 times the weight of sodium hydroxide (NaOH) based on the dry matter of the polishing waste was dissolved in distilled water to obtain 2 to 6 mol / liter. Was prepared, and 50 g of a dewatered cake of polishing waste was mixed and chemically treated. After dissolving the soluble impurities, the aqueous solution in which the impurities were dissolved and the solid content were separated by a centrifugal separator. Next, the solid content is washed with water until the washing liquid becomes neutral, dried, and then sieved to separate abrasive particles of several μm or less from glass powder, polishing cloth fibers, dust, etc. which are larger than this. And removed.

【0018】このようにして篩分けして回収された微細
粒子の組成を分析したところ、研磨材となる酸化セリウ
ムを主成分とする希土類化合物と、残留した不純物の混
合比率は表1の試料番号No1〜No3に示す通りであ
った。またこの回収した再生研磨材に蒸留水を加えて1
0重量%の研磨材スラリーを作成して、この研磨性能を
測定し、その結果を表2に示した。また比較のために水
酸化ナトリウム/廃棄物重量比が規定より少ないもの
(No4)、水酸化ナトリウム水溶液濃度が規定より高
いもの(No5)、および新品の研磨材についても同様
の測定を行い、その結果を表2に併記した。
When the composition of the fine particles collected by sieving in this manner was analyzed, the mixing ratio of the rare earth compound mainly composed of cerium oxide serving as the abrasive and the remaining impurities was determined by the sample number in Table 1. No. 1 to No. 3. Distilled water was added to the recovered reclaimed abrasive for 1 hour.
A polishing slurry of 0% by weight was prepared, and the polishing performance was measured. The results are shown in Table 2. For the sake of comparison, the same measurement was carried out for a sodium hydroxide / waste weight ratio smaller than the specified value (No. 4), a sodium hydroxide aqueous solution concentration higher than the specified value (No. 5), and a new abrasive. The results are shown in Table 2.

【0019】研磨条件は下記の通りとした。 研磨試料:株式会社オハラ製S−BSL7ガラス試料、
16mmφ×6個 研磨盤:200mm 研磨盤回転速度:約150rpm 研磨圧:約210g/cm2 研磨時間:30分 評価方法:鏡面研磨したガラス試料の表面にフッ化水素
エッチングにより深さ数十μmの溝をつけ、表面粗さ形
状測定装置により、研磨前後の表面粗さと溝の深さを測
定し、この変化から研磨速度を測定して、その結果を表
2に示した。
The polishing conditions were as follows. Polishing sample: S-BSL7 glass sample manufactured by Ohara Corporation,
16 mmφ x 6 Polishing machine: 200 mm Polishing machine rotation speed: Approx. 150 rpm Polishing pressure: Approx. 210 g / cm2 Polishing time: 30 minutes Evaluation method: Groove having a depth of several tens μm by hydrogen fluoride etching on the surface of a mirror-polished glass sample The surface roughness before and after polishing and the depth of the groove were measured by a surface roughness profile measuring apparatus, and the polishing rate was measured from the change. The results are shown in Table 2.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【表2】 [Table 2]

【0022】上表の結果より、本発明により回収して再
生した研磨材(No1〜No3)は、不純物残留量が低
く、研磨試験でも新品に比べて研磨速度が極めてわずか
に劣る程度で、表面粗さはほぼ新品と同様の良好な面が
得られた。また水酸化ナトリウム/廃棄物重量比が規定
より少ないNo4の試料は、不純物が十分に溶解せず表
面粗さも悪く、研磨速度も遅い。また水酸化ナトリウム
水溶液濃度が規定より多いNo5の試料は、Na−Si
−Al複合酸化物や複合水酸化物などが生成されて、研
磨速度は大きいが、表面粗さは悪いことが確認された。
From the results shown in the above table, the abrasives recovered and reclaimed according to the present invention (No. 1 to No. 3) have a low residual amount of impurities, and the polishing rate is very slightly inferior to that of a new abrasive in a polishing test. Roughness was almost as good as new. In addition, the sample of No. 4 in which the weight ratio of sodium hydroxide / waste is smaller than the specified value does not dissolve impurities sufficiently, has poor surface roughness, and has a low polishing rate. Further, the sample of No. 5 in which the concentration of the aqueous sodium hydroxide solution was higher than the specified value was Na-Si
-Al composite oxide, composite hydroxide and the like were generated, and it was confirmed that the polishing rate was high but the surface roughness was poor.

【0023】不純物を溶解させるアルカリ金属水酸化物
として、水酸化ナトリウムに代えて水酸化カリウムを用
いた場合についても、表3に示す処理条件(No6〜N
o7)で処理し、得られた回収研磨剤からスラリーを作
成して、この研磨性能を測定し、その結果を表4に示し
た。
When potassium hydroxide was used in place of sodium hydroxide as the alkali metal hydroxide for dissolving impurities, the treatment conditions (Nos.
o7), a slurry was prepared from the recovered abrasive, and its polishing performance was measured. The results are shown in Table 4.

【0024】[0024]

【表3】 [Table 3]

【0025】[0025]

【表4】 [Table 4]

【0026】[0026]

【発明の効果】上表の結果、本発明に係る研磨材の回収
方法によれば、極めて簡単な方法により、使用済の研磨
廃棄物から効率良く希土類酸化物の粒子が回収でき、回
収後の希土類酸化物の粒子も崩れておらず、研磨材とし
て再利用できることを見い出し、希少な希土類元素の省
資源化を図り、新品に比べて再生処理コストは半分以下
であり、同時に研磨廃棄物の減量化と廃棄廃棄コストの
低減を図ることができた。
As a result of the above table, according to the method for recovering abrasives according to the present invention, rare earth oxide particles can be efficiently recovered from used polishing waste by an extremely simple method. We found that the particles of the rare earth oxides were not broken down and could be reused as an abrasive, and conserved resources of rare rare earth elements. Reprocessing costs were less than half that of new ones, and at the same time the amount of polishing waste was reduced. And reduction of waste disposal costs.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 研磨材として酸化セリウムを主成分とす
る使用済の研磨材スラリーを回収して、ここに凝集剤を
添加して固形分を凝縮した後、脱水処理して脱水ケーキ
状の研磨廃棄物を製造し、この研磨廃棄物を原料とし
て、アルカリ金属水酸化物を、その濃度が6モル/リッ
トル以下の水溶液に、前記研磨廃棄物を混合して可溶性
の不純物を溶解した後、この不純物が溶解した水溶液と
固形分とを分離し、次いでこの分離した固形分を篩分け
して、ガラス粉や研磨布の繊維、ごみなどの混入物を分
離し、微細な研磨材を回収することを特徴とする研磨材
の回収方法。 【講求項2】 アルカリ金属水酸化物として、乾物ベー
スで研磨廃棄物の5倍以上の重量の水酸化ナトリウムま
たは7倍以上の水酸化カリウムを用いたことを特徴とす
る請求項1記載の研磨材の回収方法。
1. A used abrasive slurry containing cerium oxide as a main component as an abrasive is collected, a coagulant is added thereto to condense a solid content, and then a dewatering treatment is performed to form a dewatered cake. A waste is produced, and the polishing waste is used as a raw material, and the alkali metal hydroxide is mixed with an aqueous solution having a concentration of 6 mol / L or less to dissolve the soluble impurities. Separating the solid solution from the aqueous solution in which the impurities are dissolved, and then sieving the separated solid to separate contaminants such as glass powder, fibers of a polishing cloth, and dust, and recover fine abrasives. A method for collecting an abrasive. 2. The polishing method according to claim 1, wherein the alkali metal hydroxide is sodium hydroxide or potassium hydroxide that is at least 5 times the weight of the polishing waste on a dry matter basis. Material collection method.
JP09253620A 1997-09-18 1997-09-18 How to collect abrasives Expired - Fee Related JP3134189B2 (en)

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JP4729428B2 (en) * 2006-04-07 2011-07-20 Agcセイミケミカル株式会社 Regeneration method of cerium-based abrasive
KR100769352B1 (en) 2006-05-18 2007-10-24 주식회사 랜코 Method of recycling metallic grains
KR101450865B1 (en) * 2006-10-24 2014-10-14 동우 화인켐 주식회사 Reproduction method of spent abrasives for polishing a glass panel for display
KR101075934B1 (en) * 2009-10-07 2011-10-21 주식회사 랜코 Method of recycling metallic grains using eco-friendly process
KR101245276B1 (en) 2010-03-12 2013-03-19 주식회사 엘지화학 Method for recycling Cerium oxide abrasive
WO2012053432A1 (en) * 2010-10-18 2012-04-26 Dowaエコシステム株式会社 Method for recovering cerium oxide polishing agent and recovered product containing cerium oxide polishing agent
US20130298476A1 (en) 2011-01-24 2013-11-14 Atsushi Takahashi Method for Recovering Abrasive Material Component from used Abrasive Material Slurry, and Cerium Oxide Recovered through Method
JP2012245582A (en) * 2011-05-27 2012-12-13 Nippon Electric Glass Co Ltd Method for manufacturing cerium oxide-based abrasive
JP2013126928A (en) * 2011-12-19 2013-06-27 Shin-Etsu Chemical Co Ltd Method for recovering cerium oxide
US9796894B2 (en) 2011-12-22 2017-10-24 Konica Minolta, Inc. Abrasive material regeneration method and regenerated abrasive material
US10017675B2 (en) 2011-12-27 2018-07-10 Konica Minolta, Inc. Method for separating polishing material and regenerated polishing material
CN104203497B (en) 2012-02-16 2016-11-16 柯尼卡美能达株式会社 Grinding-material renovation process
JP6107668B2 (en) * 2012-02-17 2017-04-05 コニカミノルタ株式会社 Abrasive recycling method
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JP5943529B2 (en) * 2012-09-13 2016-07-05 エルジー・ケム・リミテッド Recycling method of waste abrasive containing ceria
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JP6155961B2 (en) * 2013-08-20 2017-07-05 日本電気硝子株式会社 Method for recycling cerium oxide abrasive
JP5850192B1 (en) * 2015-03-19 2016-02-03 コニカミノルタ株式会社 Abrasive recovery method
JP5967246B2 (en) * 2015-04-03 2016-08-10 信越化学工業株式会社 Recovery method of cerium oxide
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