JPH0454147A - Method for purifying fluorine-based inert liquid - Google Patents
Method for purifying fluorine-based inert liquidInfo
- Publication number
- JPH0454147A JPH0454147A JP16520490A JP16520490A JPH0454147A JP H0454147 A JPH0454147 A JP H0454147A JP 16520490 A JP16520490 A JP 16520490A JP 16520490 A JP16520490 A JP 16520490A JP H0454147 A JPH0454147 A JP H0454147A
- Authority
- JP
- Japan
- Prior art keywords
- fluorine
- inert liquid
- liquid
- impurities
- based inert
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 30
- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 26
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 239000011737 fluorine Substances 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000003921 oil Substances 0.000 abstract description 13
- 229910052799 carbon Inorganic materials 0.000 abstract description 11
- 239000012535 impurity Substances 0.000 abstract description 9
- 238000004821 distillation Methods 0.000 abstract description 5
- 239000003507 refrigerant Substances 0.000 abstract description 5
- OMZSGWSJDCOLKM-UHFFFAOYSA-N copper(II) sulfide Chemical compound [S-2].[Cu+2] OMZSGWSJDCOLKM-UHFFFAOYSA-N 0.000 abstract description 2
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 238000007670 refining Methods 0.000 description 5
- 239000011521 glass Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000013014 purified material Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Organic Insulating Materials (AREA)
- Fire-Extinguishing Compositions (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は、例えばガス絶縁変圧器の絶縁冷媒に使用さ
れるフッ素系不活性液体を精製する方法に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for purifying a fluorine-based inert liquid used as an insulating refrigerant for a gas insulated transformer, for example.
[従来の技術]
ガス絶縁変圧器など高電圧の電気機器に使用される絶縁
冷媒は、優れた電気特性を有することが要求され、一般
に、フロロカーボン(C,F□、o)等のフッ素系不活
性液体が使用されている。[Prior Art] Insulating refrigerants used in high-voltage electrical equipment such as gas-insulated transformers are required to have excellent electrical properties, and are generally fluorinated refrigerants such as fluorocarbons (C, F□, o). Activated liquids are used.
そして、従来、このようなフッ素系不活性液体中の不純
物、特に溶解性の不純物(硫化銅生成の要因となる油分
など)の除去は、従来、蒸留によって行なわれている。Conventionally, impurities, particularly soluble impurities (such as oil that causes the production of copper sulfide) in such a fluorine-based inert liquid have been removed by distillation.
[発明が解決しようとする課題]
しかしながら、蒸留によるフッ素系不活性液体の精製は
極めて煩雑で、より簡易な手段で精製を行なえるように
することが望まれていた。[Problems to be Solved by the Invention] However, purification of fluorine-based inert liquids by distillation is extremely complicated, and it has been desired to be able to purify by simpler means.
この発明は上記のような課題を解消するためになされた
もので、簡易な手順でフッ素系不活性液体を精製できる
方法を得ることを目的とする。This invention was made in order to solve the above-mentioned problems, and its purpose is to obtain a method that can purify a fluorine-based inert liquid using a simple procedure.
[課題を解決するための手段]
この発明に係るフッ素系不活性液体精製方法は、フッ素
系不活性液体を活性炭と接触させることにより精製する
ものである。[Means for Solving the Problems] A method for purifying a fluorine-containing inert liquid according to the present invention purifies a fluorine-containing inert liquid by bringing it into contact with activated carbon.
[作 用]
この発明におけるフッ素系不活性液体精製方法では、活
性炭が、フッ素系不活性液体に接触することにより、こ
のフッ素系不活性液体中の不純物、特に油分を吸着して
除去する。[Function] In the fluorine-containing inert liquid purification method of the present invention, the activated carbon comes into contact with the fluorine-containing inert liquid, thereby adsorbing and removing impurities, particularly oil, in the fluorine-containing inert liquid.
[発明の実施例]
以下、この発明の一実施例として、フッ素系不活性液体
としてフロロカーボン(Cs F x−○)を用いた場
合について説明する。[Embodiments of the Invention] Hereinafter, as an embodiment of the present invention, a case will be described in which fluorocarbon (Cs F x -○) is used as the fluorine-based inert liquid.
試料として用いたC、F、、Oは、予め鉱物系油を添加
し、煮沸して鉱物油を溶解させた。蒸発残渣から求めた
C、F、、O中の油分は118wt、ppm(21℃)
である。C, F, and O used as samples were added with mineral oil in advance and boiled to dissolve the mineral oil. The oil content in C, F, and O determined from the evaporation residue was 118 wt, ppm (21°C)
It is.
一方、C,Fよ、O中の油分の吸着除去に用いた精製処
理材料は、メツシュが30〜80の活性炭。On the other hand, the refining material used to adsorb and remove the oil in C, F, and O is activated carbon with a mesh size of 30 to 80.
活性アルミナ、モレキュラーシーブ5Aおよびセルロー
ス系濾過材である。これらの材料は、使用する前に11
0℃で約24時間乾燥されたものである。Activated alumina, molecular sieve 5A and cellulose filter media. These materials must be rated 11 times before use.
It was dried at 0°C for about 24 hours.
精製処理は、内径的2 am 、高さ50cmのガラス
筒に前記の各精製処理材料を約50g充填して行なった
。なお、前記ガラス筒の底部には、前記の各精製処理材
料からの微粉末が落下するのを防ぐためにガラスウール
を配置した。The purification treatment was carried out by filling a glass cylinder with an inner diameter of 2 am and a height of 50 cm with about 50 g of each of the above-mentioned purification treatment materials. Note that glass wool was placed at the bottom of the glass cylinder to prevent the fine powder from each of the purified materials from falling.
そして、精製処理時には、ガラス筒の上部から約200
11QのC,Fl、0を約50社/分の流量で落下させ
、ガラス筒下部から各精製処理材料を通過したC、F工
、0を採取した。採取された精製処理後のC,Fl、O
について、150+++Ωを約100℃で加熱して蒸発
残渣量を測定した。During the refining process, approximately 200 ml of
11Q C, Fl, and 0 were dropped at a flow rate of approximately 50 per minute, and the C, F, and 0 that had passed through each of the refining materials were collected from the bottom of the glass tube. Collected C, Fl, O after purification treatment
The amount of evaporation residue was measured by heating 150+++Ω at about 100°C.
以上のような手順で、4種類の各精製処理材料によりC
8F□、0を精製処理した場合に、精製処理後の油分量
および油分除去率を下表1に示す。With the above steps, C
When 8F□, 0 was purified, the oil content and oil removal rate after the purification process are shown in Table 1 below.
上記表1から、各精製処理材料にC11F 1 Goを
通過させることにより、C,F1GO中の油分量が低下
することが分かる。特に、活性炭については、120t
it、pprn相当の油分を完全に除去することができ
、他の精製処理材料に比べて、油分除去能力に優れてい
ることが明確である。From Table 1 above, it can be seen that by passing C11F 1 Go through each of the refining materials, the oil content in C and F1 GO decreases. Especially for activated carbon, 120t
It is possible to completely remove oil equivalent to IT, pprn, and it is clear that the oil removal ability is superior to other refining materials.
つまり、活性炭にフッ素系不活性液体を接触させるだけ
で、蒸留のような煩雑な手段を用いることなく、フッ素
系不活性液体中の不純物、特に油分が吸着され除去され
るのである。In other words, by simply bringing the fluorine-based inert liquid into contact with activated carbon, impurities, especially oil, in the fluorine-based inert liquid can be adsorbed and removed without using complicated means such as distillation.
なお、上記実施例では、フッ素系不活性液体中の油分の
除去について説明したが、フッ素系不活性液体の性能上
有害となる他の溶解成分、例えば水分などの除去につい
ても同様の効果があるのは云うまでもない。また、上記
実施例では、フッ素系不活性液体がC,F、、Oである
場合について説明したが、本発明は、これに限定される
ものではなく、他のフッ素系不活性液体についても同様
に適用され、上記実施例と同様の効果を奏する。In addition, in the above example, the removal of oil in the fluorinated inert liquid was explained, but the same effect can be achieved in the removal of other dissolved components that are harmful to the performance of the fluorinated inert liquid, such as water. Needless to say. Further, in the above embodiment, the case where the fluorine-based inert liquid is C, F, O is explained, but the present invention is not limited to this, and the same applies to other fluorine-based inert liquids. , and the same effects as in the above embodiment can be obtained.
[発明の効果]
以上のように、この発明によれば、活性炭にフッ素系不
活性液体を接触させることにより、フッ素系不活性液体
中の不純物の除去が行なわれるので、従来のごとく蒸留
を行なう必要がなく、極めて簡易な手順でフッ素系不活
性液体の精製を行なえる効果がある。[Effects of the Invention] As described above, according to the present invention, impurities in the fluorinated inert liquid are removed by bringing the fluorinated inert liquid into contact with activated carbon. This method is not necessary, and has the effect of purifying a fluorine-based inert liquid using an extremely simple procedure.
Claims (1)
製することを特徴とするフッ素系不活性液体精製方法。A method for purifying a fluorine-based inert liquid, which comprises purifying the fluorine-based inert liquid by bringing it into contact with activated carbon.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16520490A JPH0454147A (en) | 1990-06-21 | 1990-06-21 | Method for purifying fluorine-based inert liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16520490A JPH0454147A (en) | 1990-06-21 | 1990-06-21 | Method for purifying fluorine-based inert liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0454147A true JPH0454147A (en) | 1992-02-21 |
Family
ID=15807817
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16520490A Pending JPH0454147A (en) | 1990-06-21 | 1990-06-21 | Method for purifying fluorine-based inert liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0454147A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06145180A (en) * | 1992-11-09 | 1994-05-24 | Shin Etsu Chem Co Ltd | Purification of organophosphorus compound |
-
1990
- 1990-06-21 JP JP16520490A patent/JPH0454147A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06145180A (en) * | 1992-11-09 | 1994-05-24 | Shin Etsu Chem Co Ltd | Purification of organophosphorus compound |
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