JPH06196464A - Manufacture of semiconductor cleaning diethyl carbonate - Google Patents

Manufacture of semiconductor cleaning diethyl carbonate

Info

Publication number
JPH06196464A
JPH06196464A JP35802092A JP35802092A JPH06196464A JP H06196464 A JPH06196464 A JP H06196464A JP 35802092 A JP35802092 A JP 35802092A JP 35802092 A JP35802092 A JP 35802092A JP H06196464 A JPH06196464 A JP H06196464A
Authority
JP
Japan
Prior art keywords
diethyl carbonate
cleaned
pure water
chlorine
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.)
Pending
Application number
JP35802092A
Other languages
Japanese (ja)
Inventor
Kazutaka Kubota
和孝 久保田
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.)
SAN SEAL KK
Original Assignee
SAN SEAL KK
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 SAN SEAL KK filed Critical SAN SEAL KK
Priority to JP35802092A priority Critical patent/JPH06196464A/en
Publication of JPH06196464A publication Critical patent/JPH06196464A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain semiconductor cleaning diethyl carbonate by a method wherein chlorine-containing diethyl carbonate is cleaned with weak alkaline water solution, then cleaned with pure water until it grows neutral, and dehydrated. CONSTITUTION:Chlorine-containing diethyl carbonate is cleaned a few times with weak alkaline water solution, for instance, alkaline metal hydrogen carbonate such as sodium hydrogencarbonate. Diethyl carbonate is cleaned with pure water after it is cleaned with alkaline water solution. It is preferable that deionized pure water is used. Diethyl carbonate is cleaned with pure water a few times till it grows neutral, and diethyl carbonate is recovered. Diethyl carbonate is cleaned with pure water and dehydrated. In this case, dehydration means that water content and residual chlorine are removed from diethyl carbonate usually through adsorption. Diethyl carbonate is brought into contact with adsorbent to remove water content and residual chlorine from it. By this setup, semiconductor cleaning diethyl carbonate can be manufactured from marketing diethyl carbonate.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、炭酸ジエチルから半導
体洗浄用炭酸ジエチルを製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing semiconductor cleaning diethyl carbonate from diethyl carbonate.

【0002】[0002]

【従来の技術及び課題】半導体の洗浄剤は、その信頼性
向上のために不可欠である。半導体の洗浄には従来、フ
ロンが使用されていたが、フロンは大気中で分解されず
成層圏に達して紫外線で分解され、その際に生ずる塩素
原子がオゾン層を破壊することがわかった。
2. Description of the Related Art Cleaning agents for semiconductors are indispensable for improving their reliability. Conventionally, chlorofluorocarbon has been used for cleaning semiconductors, but it has been found that chlorofluorocarbon does not decompose in the atmosphere, reaches the stratosphere and is decomposed by ultraviolet rays, and chlorine atoms generated at that time destroy the ozone layer.

【0003】そのため、公害のないフロンの代替物の開
発研究がなされてきたが、その代替物も完全なものは得
られていないのが実状である。そこで本発明者らは純粋
な炭酸ジエチルを半導体洗浄剤として用いることにより
上記の課題を解決できることを知った。
For this reason, research and development have been conducted on alternatives to CFCs that do not cause pollution, but in reality, complete alternatives have not been obtained. Therefore, the present inventors have found that the above problem can be solved by using pure diethyl carbonate as a semiconductor cleaning agent.

【0004】市販の炭酸ジエチルは、通常、ホスゲンと
エチレングリコールとの反応、エチレンオキサイドと炭
酸ガスとの反応、等によって製造され、塩素を含有して
いるのが通常である。しかし、塩素を含んだ炭酸ジエチ
ルを半導体の洗浄に使用すると、半導体の腐食の原因と
なる。
Commercially available diethyl carbonate is usually produced by the reaction of phosgene with ethylene glycol, the reaction of ethylene oxide with carbon dioxide gas, etc., and usually contains chlorine. However, the use of chlorine-containing diethyl carbonate for cleaning semiconductors causes corrosion of the semiconductors.

【0005】[0005]

【課題を解決するための手段】本発明はこの課題を解決
するために塩素を含有する炭酸ジエチルに特定の処理を
施すことにより、塩素を殆ど含まないか又は半導体洗浄
に支障のない程度まで塩素の含有量を減らすことによっ
て半導体洗浄用炭酸ジエチルを製造する方法に関する。
In order to solve this problem, the present invention performs a specific treatment on chlorine-containing diethyl carbonate so that chlorine is hardly contained or the semiconductor cleaning is not hindered. The present invention relates to a method for producing diethyl carbonate for cleaning semiconductors by reducing the content thereof.

【0006】すなわち本発明は、塩素を含有する炭酸ジ
エチルを弱アルカリ水溶液で洗浄し、純水で中性になる
まで洗浄し、次いで脱水することを特徴とする、半導体
洗浄用炭酸ジエチルの製造方法である。
That is, according to the present invention, a method for producing diethyl carbonate for semiconductor cleaning is characterized in that diethyl carbonate containing chlorine is washed with a weak alkaline aqueous solution, washed with pure water until neutral, and then dehydrated. Is.

【0007】本発明においては、塩素を含有する炭酸ジ
エチルを弱アルカリ水溶液で洗浄する。ここで用いられ
る弱アルカリ水溶液のアルカリとしては炭酸ジエチルを
分解させない弱アルカリであれば各種のものが使用し得
る。
In the present invention, chlorine-containing diethyl carbonate is washed with a weak alkaline aqueous solution. As the alkali of the weak alkaline aqueous solution used here, various kinds can be used as long as they are weak alkalis which do not decompose diethyl carbonate.

【0008】例えば、炭酸水素ナトリウムで例示される
アルカリ金属炭酸水素塩は好適に使用される。弱アルカ
リ水溶液のpHは7.1 〜9、特に8〜8.5好まし
い。アルカリ水溶液による洗浄は通常、数回行う。
For example, an alkali metal hydrogen carbonate exemplified by sodium hydrogen carbonate is preferably used. The pH of the weak alkaline aqueous solution is preferably 7.1 to 9, particularly preferably 8 to 8.5. Washing with an alkaline aqueous solution is usually performed several times.

【0009】アルカリ水溶液で洗浄後、純水で洗浄す
る。純水としては脱水イオン水が好ましい。洗浄を中性
になるまで数回繰り返し炭酸ジエチル層を回収する。
After washing with an alkaline aqueous solution, washing with pure water is performed. Deionized ionized water is preferable as pure water. The diethyl carbonate layer is recovered by repeating the washing several times until it becomes neutral.

【0010】純水で洗浄後、脱水する。ここにいう脱水
は、水分及び残留塩素を除去するものであり、通常、吸
着によって除去する。この脱水工程で水分が実質的に除
去され、塩素は5ppb 以下まで低減される。
After washing with pure water, dehydration is performed. The dehydration mentioned here removes water and residual chlorine, and is usually removed by adsorption. In this dehydration step, water is substantially removed and chlorine is reduced to 5 ppb or less.

【0011】吸着に用いる吸着剤や吸着の手段として
は、炭酸ジエチルを分解させないもので、水分及び残留
塩素を除去し得るものであればよく、例えばセラミック
ス、動物骨を有効成分とする処理剤、等で例示される吸
着剤と接触させる方法、ゲル浸透クロマトグラフィー(G
PC) を用いて行う方法、等のそれ自体公知の吸着剤、吸
着手段の中から適宜、選択し採用される。
The adsorbent used for adsorption and the means for adsorbing may be any one that does not decompose diethyl carbonate and can remove water and residual chlorine. For example, a treating agent containing ceramics or animal bones as an active ingredient, Method of contacting with an adsorbent exemplified by gel permeation chromatography (G
The method is performed by appropriately selecting from an adsorbent and an adsorbing means known per se such as a method using PC).

【0012】セラミックスとしては、例えばアルミナ、
シリカ・アルミナ、ゼオライト、等で例示される各種の
ものがあるが、吸着性能を考慮し適宜選択される。ゲル
浸透クロマトグラフィー(GPC) は非水系ゲルクロマトグ
ラフィーともいい、有機溶媒を移動相に用いる排除クロ
マトグラフィーであり、各種のものから適宜選択して使
用される。
As the ceramics, for example, alumina,
There are various types such as silica / alumina and zeolite, which are appropriately selected in consideration of adsorption performance. Gel permeation chromatography (GPC) is also called non-aqueous gel chromatography, is exclusion chromatography using an organic solvent as a mobile phase, and is appropriately selected and used from various types.

【0013】動物骨粉を有効成分とする処理剤は、有効
成分である動物骨粉をつなぎ材、及び必要に応じ他の添
加材を混合し、粒状又は粉粒状に成形し、乾燥し、焼成
してなるものである。動物骨粉は、従来畜産場等でほと
んど廃棄されていた骨、特に牛、馬、羊等の硬骨が主体
の動物の骨が採用される。
The treatment agent containing animal bone powder as an active ingredient is obtained by mixing animal bone powder as an active ingredient with a binder and, if necessary, other additives, molding into granules or powder granules, drying and firing. It will be. As animal bone powder, bones that have been mostly discarded in the past, such as cattle, horses, and sheep, are mainly used as animal bone meal.

【0014】これらの動物の生骨の処理は例えば焼成し
やすい大きさに切断し、煮沸し、焼成し、冷却する。上
記煮沸工程によって、外側のみならず気孔内に付着して
いる有機物を骨から大方分離除去することができる。さ
らに上記焼成工程により残存する有機物を完全に除去す
ることができ、同時に骨中の湿度 (水分) を数%以下、
好ましくはほぼ0%にまで低下させる。
The raw bones of these animals are treated, for example, by cutting into a size that is easy to bake, boiling, firing and cooling. By the above-mentioned boiling step, most of the organic substances attached not only to the outside but also inside the pores can be separated and removed from the bone. Furthermore, the remaining organic matter can be completely removed by the above-mentioned firing step, and at the same time, the humidity (water content) in the bone is reduced to several% or less,
It is preferably reduced to almost 0%.

【0015】骨は白骨化して無数の気孔を有した原形組
織状態を維持する。冷却後、この骨を破砕しパウダー機
にかけて20〜200 メッシュ前後、特に好ましくは50〜10
0 メッシュの粉状の骨粉とする。骨粉はアルカリ性であ
り、カルシウム(約33重量%)を主成分とし、リン(約
16.7重量%) 、等を含むものであり、粒子の内外にわた
って無数微小気孔が連通存在している。
The bone is whitened and maintains the original tissue state with numerous pores. After cooling, the bone is crushed and powdered to a size of 20-200 mesh, particularly preferably 50-10.
0 Bone powder in the form of powder. Bone meal is alkaline, contains calcium (about 33% by weight) as a main component, and phosphorus (about 33% by weight).
16.7% by weight), etc., and countless micropores are continuously present inside and outside the particles.

【0016】つなぎ材は動物骨粉を粒状又は粉粒状に成
形するためのつなぎの役目をするものであればよく、例
えばベントナイト、酸性白土、活性白土、カオリン粘
土、セリサイト、パイオフィライト、耐火粘土、モンモ
リロナイト、等があげられる。つなぎ材の他に必要に応
じ他の充填材、添加材を加えてもよい。
The binder may be any one that functions as a binder for forming animal bone powder into granules or powder granules. For example, bentonite, acid clay, activated clay, kaolin clay, sericite, pyrophyllite, refractory clay. , Montmorillonite, etc. In addition to the binder, other fillers and additives may be added if necessary.

【0017】処理剤中の動物骨粉の割合は吸着性能を考
慮すれば、動物骨粉の割合の多いもの、例えば動物骨粉
が50〜80重量%のものがあげられる。濾過剤は粒状又は
粉粒状であるが、その大きさは通常、2 〜30mm、好まし
くは 5〜20mmである。その他、各種の吸着剤が使用し得
る。
Considering the adsorption performance, the proportion of animal bone powder in the treatment agent is high in the proportion of animal bone powder, for example, 50 to 80% by weight of animal bone powder. The filtering agent is granular or powdery, and the size thereof is usually 2 to 30 mm, preferably 5 to 20 mm. In addition, various adsorbents can be used.

【0018】本発明の方法においては、脱水処理後の炭
酸ジエチルは塩素の含有量が低減され、かつ脱水された
ものである。
In the method of the present invention, the dehydrated diethyl carbonate has a reduced chlorine content and is dehydrated.

【0019】[0019]

【実施例】以下の順序で炭酸ジエチルを精製した。 1.市販の炭酸ジエチル1リットルを0.1%炭酸水素
ナトリウム溶液1リットルで抽出を行った。 2.1.の操作を数回繰り返した。 3.2.で得られた炭酸ジエチルを純水(脱イオン水)
で、中性になるまで、数回抽出し、炭酸ジエチル層を回
収した。 4.3.で得られた炭酸ジエチルを、三層のカラム(上
から順にA.炭酸水素ナトリウム(40/60メッシュ) 、
B.合成ゼオライト系脱水剤(40/60メッシュ) 、C.合
成ゼオライト系脱水剤(ペレット状))に供給し、再精
製した。
EXAMPLE Diethyl carbonate was purified in the following order. 1. 1 liter of commercially available diethyl carbonate was extracted with 1 liter of 0.1% sodium hydrogen carbonate solution. 2.1. The above operation was repeated several times. 3.2. Pure water (deionized water) from the diethyl carbonate obtained in
Then, the mixture was extracted several times until it became neutral, and the diethyl carbonate layer was collected. 4.3. The diethyl carbonate obtained in Step 3 was added to a three-layer column (from top to bottom: A. sodium hydrogen carbonate (40/60 mesh),
B. Synthetic zeolite-based dehydrating agent (40/60 mesh), C.I. It was supplied to a synthetic zeolite-based dehydrating agent (pellet form) and repurified.

【0020】上記のカラム操作により得られた炭酸ジエ
チルを用いて半導体洗浄剤テストを行ったところ、ウェ
ハーの表面に付着した汚染物、不要物は洗浄除去され、
塩素及びそれに類似するイオンによるサビは認められな
かった。
When a semiconductor cleaning agent test was conducted using the diethyl carbonate obtained by the above column operation, contaminants and unnecessary substances adhering to the surface of the wafer were washed and removed.
Rust due to chlorine and similar ions was not observed.

【0021】[0021]

【発明の効果】本発明によれば、市販の炭酸ジエチルか
ら半導体洗浄用炭酸ジエチルを製造することができる。
ここで得られる半導体洗浄用炭酸ジエチルは、ウェハー
の表面に付着する汚染物、不要物、等の溶解性が高く、
ウェハーの腐食がなく、非フロン系であってオゾン層を
破壊することがない等の利点を有し、本発明によればウ
ェハーを好適に洗浄することができる。
According to the present invention, it is possible to produce diethyl carbonate for semiconductor cleaning from commercially available diethyl carbonate.
Diethyl carbonate for semiconductor cleaning obtained here has high solubility for contaminants, unwanted substances, etc. adhering to the surface of the wafer,
According to the present invention, the wafer can be suitably washed, because it has the advantages that it does not corrode the wafer, it is a non-CFC type, it does not destroy the ozone layer, and the like.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 塩素を含有する炭酸ジエチルを弱アルカ
リ水溶液で洗浄し、純水で中性になるまで洗浄し、次い
で脱水することを特徴とする、半導体洗浄用炭酸ジエチ
ルの製造方法
1. A method for producing diethyl carbonate for semiconductor cleaning, which comprises washing diethyl carbonate containing chlorine with a weak alkaline aqueous solution, washing with pure water until neutral, and then dehydrating.
【請求項2】 弱アルカリ水溶液がアルカリ金属炭酸水
素塩の水溶液である請求項1記載の方法
2. The method according to claim 1, wherein the weak alkaline aqueous solution is an aqueous solution of an alkali metal hydrogen carbonate.
【請求項3】 弱アルカリ水溶液が炭酸水素ナトリウム
の水溶液である請求項1記載の方法
3. The method according to claim 1, wherein the weak alkaline aqueous solution is an aqueous solution of sodium hydrogen carbonate.
【請求項4】 純水が脱イオン水である請求項1記載の
方法
4. The method according to claim 1, wherein the pure water is deionized water.
【請求項5】 脱水が、水分及び残留塩素を吸着によっ
て除去するものである請求項1記載の方法
5. The method according to claim 1, wherein the dehydration removes water and residual chlorine by adsorption.
【請求項6】 吸着に用いる吸着剤がセラミックスであ
る請求項5記載の方法
6. The method according to claim 5, wherein the adsorbent used for adsorption is ceramics.
【請求項7】 吸着を動物骨を有効成分とする処理剤と
接触させて行う請求項5記載の方法
7. The method according to claim 5, wherein the adsorption is carried out by contacting with a treatment agent containing animal bone as an active ingredient.
【請求項8】 吸着をゲル浸透クロマトグラフィー(GP
C) を用いて行う請求項5記載の方法
8. Adsorption by gel permeation chromatography (GP
The method according to claim 5, wherein C) is used.
JP35802092A 1992-12-25 1992-12-25 Manufacture of semiconductor cleaning diethyl carbonate Pending JPH06196464A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35802092A JPH06196464A (en) 1992-12-25 1992-12-25 Manufacture of semiconductor cleaning diethyl carbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35802092A JPH06196464A (en) 1992-12-25 1992-12-25 Manufacture of semiconductor cleaning diethyl carbonate

Publications (1)

Publication Number Publication Date
JPH06196464A true JPH06196464A (en) 1994-07-15

Family

ID=18457135

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35802092A Pending JPH06196464A (en) 1992-12-25 1992-12-25 Manufacture of semiconductor cleaning diethyl carbonate

Country Status (1)

Country Link
JP (1) JPH06196464A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0745580A1 (en) * 1995-06-01 1996-12-04 Bayer Ag Process for purifying diarylcarbonates using aluminosilicates
WO2007074692A1 (en) * 2005-12-27 2007-07-05 Asahi Kasei Chemicals Corporation Process for industrial production of dialkyl carbonate and diol
WO2007074664A1 (en) * 2005-12-26 2007-07-05 Asahi Kasei Chemicals Corporation Process for industrial separation of dialkyl carbonate
US8058465B2 (en) 2005-11-25 2011-11-15 Asahi Kasei Chemicals Corporation Process for industrially producing dialkyl carbonate and diol

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0745580A1 (en) * 1995-06-01 1996-12-04 Bayer Ag Process for purifying diarylcarbonates using aluminosilicates
US8058465B2 (en) 2005-11-25 2011-11-15 Asahi Kasei Chemicals Corporation Process for industrially producing dialkyl carbonate and diol
WO2007074664A1 (en) * 2005-12-26 2007-07-05 Asahi Kasei Chemicals Corporation Process for industrial separation of dialkyl carbonate
EA012062B1 (en) * 2005-12-26 2009-08-28 Асахи Касеи Кемикалз Корпорейшн Process for industrial separation of dialkyl carbonate
US8049028B2 (en) 2005-12-26 2011-11-01 Asahi Kasei Chemicals Corporation Industrial process for separating out dialkyl carbonate
WO2007074692A1 (en) * 2005-12-27 2007-07-05 Asahi Kasei Chemicals Corporation Process for industrial production of dialkyl carbonate and diol

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