JPS6138384A - Method of recovering argon gas for atmosphere - Google Patents

Method of recovering argon gas for atmosphere

Info

Publication number
JPS6138384A
JPS6138384A JP59161810A JP16181084A JPS6138384A JP S6138384 A JPS6138384 A JP S6138384A JP 59161810 A JP59161810 A JP 59161810A JP 16181084 A JP16181084 A JP 16181084A JP S6138384 A JPS6138384 A JP S6138384A
Authority
JP
Japan
Prior art keywords
argon
argon gas
liquid
purity
recovered
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
JP59161810A
Other languages
Japanese (ja)
Inventor
宇野 煕
戸田 博章
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.)
Koatsu Gas Kogyo Co Ltd
Original Assignee
Koatsu Gas Kogyo Co 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 Koatsu Gas Kogyo Co Ltd filed Critical Koatsu Gas Kogyo Co Ltd
Priority to JP59161810A priority Critical patent/JPS6138384A/en
Publication of JPS6138384A publication Critical patent/JPS6138384A/en
Pending legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はシリコン半導体用単結晶製造時等、ア体状に再
生する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for regenerating a single crystal into an integral shape during the production of a silicon semiconductor single crystal.

(従来の技術) 従来、上記のような製造時に雰囲気ガスとして用いられ
るアルゴンガスは回収されることのないま\に大気中に
自然放出していたのが大力の実情である。この不経済さ
に着目して用尽した回収アルゴンをフィルター、吸着剤
を介して不純物の一部を除去した后に精製工程に於てN
m、01を除去して最高シクスナインの純度のアルゴン
を再利用する試みが提案されている。
(Prior Art) Conventionally, the reality is that the argon gas used as an atmospheric gas during the manufacturing process as described above has been naturally released into the atmosphere without being recovered. Focusing on this uneconomical issue, we removed some of the impurities from the exhausted recovered argon through a filter and adsorbent, and then used N in the purification process.
Attempts have been proposed to remove m,01 and reuse argon of up to 69 purity.

(発明が解決しようとする問題点) しかしながら、上記先行技術に於てはNmの除去のため
にチタンゲッタ一方式を採用しているために、Nl除去
のために用いたチタンを再活性化することが出来ないと
云う不経済性をなお残しておシ、その改善が望まれてい
た。     ゛(問題を解決するだめの手段) 本発明は上記に鑑み精製に於て、低温無滴を採用すると
共に精製直前の回収アルゴンガスを雰囲気ガスの根源で
ある(高純度の)液体アルゴンの気化の冷熱・、必要に
よっては安価な液体窒素の冷熱を活用して液化させるこ
とにより経済性を更に改善したものである。
(Problems to be Solved by the Invention) However, since the above-mentioned prior art employs a titanium getter system for removing Nm, it is difficult to reactivate the titanium used for removing Nl. However, the uneconomical nature of not being able to do so still remained, and improvements were desired. (Means for Solving the Problem) In view of the above, the present invention employs low-temperature dropless purification and uses recovered argon gas immediately before purification to vaporize (high purity) liquid argon, which is the source of the atmospheric gas. Economic efficiency has been further improved by utilizing the cold energy of liquid nitrogen, and if necessary, the cold energy of inexpensive liquid nitrogen.

本発明によると精製されるアルゴンはシクスナの高純度
のアルゴンガスとはならない迄もその他の雰囲気用ガス
としては広く適用出来るのである。
According to the present invention, the purified argon can be widely used as other atmospheric gases even though it does not become the highly purified argon gas of SIXNA.

即ち本発明は、高純度アルゴンガスを不活性雰囲気とし
て用尽した回収ガス中のダストをフィルターで除去し、
次に圧力吸着及びもしくは熱吸着によって不純物の一部
を除去し、続いて液体アルゴン及びもしくは液体窒素に
よシ液化し、最終的に低温無滴精製して高純度アルゴン
を液状もしくは気体状で回収することを特徴とする雰囲
気用アルゴンガスの回収方法に係わる。
That is, the present invention uses a filter to remove dust in the exhausted recovered gas using high-purity argon gas as an inert atmosphere.
Next, some impurities are removed by pressure adsorption and/or thermal adsorption, followed by liquefaction with liquid argon and/or liquid nitrogen, and finally low-temperature dropless purification to recover high-purity argon in liquid or gas form. The present invention relates to a method for recovering argon gas for atmospheric use.

(作用) シリコン半導体単結晶製造時の不活性雰囲気として用尽
したアルゴンガス中には8 iog、油、水分。
(Function) The argon gas used as an inert atmosphere during the production of silicon semiconductor single crystals contains 8 iog, oil, and moisture.

CO2、O宏、 Nz が不純物として含まれておシ、
純度が97係のオーダであるが、このうち8 io!及
び油は、先づフィルターによって除去され、次に公知の
圧力スイング吸着及びもしくは熱スイング吸着によって
HI3 、 cowが取シ除かれる。 しかしox 、
Nsをなお含む回収アルゴンガスは、次の低温蒸溜に付
される前に液化されるが、この液化の冷熱はアルゴン雰
囲気ガスの根源である高純度の液体アルゴンの気化の冷
熱を用いるが、液体アルゴンの冷熱のみでは冷熱がなお
不足するのであれば液体窒素の冷熱をもって補なうこと
が出来る。
CO2, Ohiro, Nz are included as impurities,
The purity is on the order of 97, of which 8 io! and oil are first removed by a filter and then the HI3, cow is removed by known pressure swing adsorption and/or heat swing adsorption. But ox,
The recovered argon gas, which still contains Ns, is liquefied before being subjected to the next low-temperature distillation. If the cold energy of argon alone is still insufficient, it can be supplemented with the cold energy of liquid nitrogen.

逆に液体窒素のみの冷熱によって液化をすることも可能
である。これら液体アルゴン及びもしくは窒素の冷熱は
、同液体アルゴン及びもしくは窒素を上記回収アルゴン
ガスの液化器の気化器を通して気化させることによって
得られる。そして、液化した液化回収アルゴンは、次に
低温蒸溜に付せられ沸点の最も低いN重(B、P−19
5,8℃)が最初に、続いてAr (B、P−185,
7b ) 、その后0!(B、P−183℃)と云う順
次に夫々分溜され、アルゴンの純度はファイブナイン身
−に達する。
Conversely, it is also possible to liquefy using only the cold heat of liquid nitrogen. The cold energy of the liquid argon and/or nitrogen is obtained by vaporizing the liquid argon and/or nitrogen through the vaporizer of the recovered argon gas liquefier. The liquefied recovered argon is then subjected to low-temperature distillation and has the lowest boiling point, N-weight (B, P-19
5,8℃) first, followed by Ar (B, P-185,
7b), then 0! (B, P - 183°C), and the purity of argon reaches five nines.

上記の回収方法の実施を示すフローチャートを第1図に
示す。―゛によって、上述した各プロセスをフローチャ
ートの各ブロック内に文字をもって表示しであることか
ら容易に理解され得よう。なお、高純度液体アルゴンか
らsi半導体製造装置に至る間の気化器は、通常の気化
器であシこ\で気化した高純度アルゴンガスと、前述の
ように高純度液体アルゴンの一部を回収アルゴンガスの
液化器の気化器(不図示)を経て気化した高純度アルゴ
ンガスとを合流させてSi半導体製造装置に送致するよ
うにしたものである。回収液体アルゴンは純度がファイ
ブナインオーダーであるから、シクスナインオーダーの
要求されるSi半導体装置には、そのま\活用出来ず他
の雰囲気用に応用するものである。また、回収液体アル
ゴンは適宜気化して回収気体アルゴンとしてストックし
ても良い。
A flowchart showing the implementation of the above recovery method is shown in FIG. It can be easily understood that each of the above-mentioned processes is indicated by a letter in each block of the flowchart. The vaporizer used between the high-purity liquid argon and the Si semiconductor manufacturing equipment is a normal vaporizer that collects the vaporized high-purity argon gas and a portion of the high-purity liquid argon as described above. High-purity argon gas vaporized through a vaporizer (not shown) of an argon gas liquefier is combined with the argon gas and sent to the Si semiconductor manufacturing equipment. Since the recovered liquid argon has a purity of the five-nine order, it cannot be used as is for Si semiconductor devices that require six-nine-order purity, but is instead applied to other atmospheres. Further, the recovered liquid argon may be appropriately vaporized and stored as recovered gaseous argon.

(発明の効果) 本発明は以上の如く、フィルター及び吸着によって粗精
製した回収アルゴンガスを液化した后、低温蒸溜によっ
てN!、0.  を夫々分溜してファイブナイン−オー
ダーの回収液体アルゴンもしくは気体アルゴンを得るも
のであるから、従来のチタンゲッターを用いた精製手段
に較べて最終的な純度は低いものの経済的に有利に回収
アルゴンガスの再生が可能となり、この際上記液化を液
体アルゴンもしくは液体窒素の気化の冷熱によって実施
すればコスト的にも特筆となるものでsb、一般的には
これ迄廃棄していた回収アルゴンガスの再生利用に一役
をかった発明である。
(Effects of the Invention) As described above, the present invention liquefies recovered argon gas that has been crudely purified by filtering and adsorption, and then liquefies the recovered argon gas by low-temperature distillation. , 0. This method obtains five-nine-order recovered liquid argon or gaseous argon by fractionating the respective amounts of recovered argon, so although the final purity is lower than that of the conventional purification method using a titanium getter, it is economically advantageous to recover argon. It becomes possible to regenerate the gas, and in this case, if the above liquefaction is carried out using the cold heat of vaporizing liquid argon or liquid nitrogen, it will be noteworthy in terms of cost. This invention played a role in recycling.

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

第1図は本発明を実施するフローチャートである。 一以上一 FIG. 1 is a flowchart for implementing the invention. one or more one

Claims (1)

【特許請求の範囲】[Claims] 1、高純度アルゴンガスを不活性雰囲気として用尽した
回収ガス中のダストをフィルターで除去し、次に圧力吸
着及びもしくは熱吸着によって不純物の一部を除去し、
続いて液体アルゴン及びもしくは液体窒素により液化し
、最終的に低温蒸溜精製して高純度アルゴンを液状もし
くは気体状で回収することを特徴とする雰囲気用アルゴ
ンガスの回収方法。
1. Using a filter to remove dust in the exhausted recovered gas using high-purity argon gas as an inert atmosphere, and then removing some of the impurities by pressure adsorption and/or thermal adsorption,
A method for recovering atmospheric argon gas, which comprises subsequently liquefying it with liquid argon and/or liquid nitrogen, and finally recovering high-purity argon in liquid or gaseous form through low-temperature distillation purification.
JP59161810A 1984-07-31 1984-07-31 Method of recovering argon gas for atmosphere Pending JPS6138384A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59161810A JPS6138384A (en) 1984-07-31 1984-07-31 Method of recovering argon gas for atmosphere

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59161810A JPS6138384A (en) 1984-07-31 1984-07-31 Method of recovering argon gas for atmosphere

Publications (1)

Publication Number Publication Date
JPS6138384A true JPS6138384A (en) 1986-02-24

Family

ID=15742340

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59161810A Pending JPS6138384A (en) 1984-07-31 1984-07-31 Method of recovering argon gas for atmosphere

Country Status (1)

Country Link
JP (1) JPS6138384A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4732580A (en) * 1986-10-01 1988-03-22 The Boc Group, Inc. Argon and nitrogen coproduction process
JPH01310712A (en) * 1988-06-09 1989-12-14 Kinki Reinetsu Kk Producing equipment of atmospheric gas for heating oven

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS594673A (en) * 1982-06-11 1984-01-11 ミネソタ・マイニング・アンド・マニユフアクチユアリング・コンパニ− Treatment of fibrous base material

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS594673A (en) * 1982-06-11 1984-01-11 ミネソタ・マイニング・アンド・マニユフアクチユアリング・コンパニ− Treatment of fibrous base material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4732580A (en) * 1986-10-01 1988-03-22 The Boc Group, Inc. Argon and nitrogen coproduction process
JPH01310712A (en) * 1988-06-09 1989-12-14 Kinki Reinetsu Kk Producing equipment of atmospheric gas for heating oven

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