JPH0482845A - Purification of perfluorocarbon - Google Patents
Purification of perfluorocarbonInfo
- Publication number
- JPH0482845A JPH0482845A JP19341490A JP19341490A JPH0482845A JP H0482845 A JPH0482845 A JP H0482845A JP 19341490 A JP19341490 A JP 19341490A JP 19341490 A JP19341490 A JP 19341490A JP H0482845 A JPH0482845 A JP H0482845A
- Authority
- JP
- Japan
- Prior art keywords
- perfluorocarbon
- liquid
- layer
- treatment
- vibration
- 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
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 238000000746 purification Methods 0.000 title abstract description 4
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 238000000034 method Methods 0.000 claims abstract description 22
- 238000003756 stirring Methods 0.000 claims description 11
- 239000000126 substance Substances 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 3
- 206010001497 Agitation Diseases 0.000 abstract 2
- 238000013019 agitation Methods 0.000 abstract 2
- 238000001704 evaporation Methods 0.000 abstract 1
- 230000008020 evaporation Effects 0.000 abstract 1
- 238000009413 insulation Methods 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 238000007710 freezing Methods 0.000 description 6
- 230000008014 freezing Effects 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- RVZRBWKZFJCCIB-UHFFFAOYSA-N perfluorotributylamine Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)N(C(F)(F)C(F)(F)C(F)(F)C(F)(F)F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F RVZRBWKZFJCCIB-UHFFFAOYSA-N 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229960004624 perflexane Drugs 0.000 description 1
- ZJIJAJXFLBMLCK-UHFFFAOYSA-N perfluorohexane Chemical compound FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F ZJIJAJXFLBMLCK-UHFFFAOYSA-N 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、処理効率に優れるパーフルオロカーボンの精
製方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for purifying perfluorocarbon with excellent processing efficiency.
従来の技術及び課題
熱媒体、絶縁油、洗浄液などとして種々の技術分野で使
用されているフロンがオゾン層の破壊物質として指摘さ
れ、その代替物が希求されている中、パーフルオロカー
ボンが提案されている。Conventional technologies and issues CFCs, which are used in various technical fields as heat carriers, insulating oils, cleaning fluids, etc., have been pointed out as substances that deplete the ozone layer, and as alternatives to them are sought after, perfluorocarbons have been proposed. There is.
しかしながら、パーフルオロカーボンには空気等のガス
が100m1あたり数十mlも溶存するため充分に脱気
精製しないと例えばヒートパイプなどの熱媒体として実
用に供しうる高純度物が得られ難く、フロン精製の場合
と同様に凍結法や平衡蒸気圧法にて、空気等の非凝縮性
物質の泡が出なくなるまで処理するにはフロンの場合の
数倍もの処理工程、ないし処理時間を要し、約500m
1のパーフルオロカーボンを精製するのに数時間を要す
るという問題点があった。また、その精製液を蒸留して
ヒートパイプに注入しても当初の5〜30%の留分を注
入したヒートパイプにおいて満足な熱抵抗を示さないと
いう、フロンの場合には生じながった現象が発生し、従
来の方法では充分に精製できない問題点があった。However, since gases such as air are dissolved in perfluorocarbon in an amount of several tens of milliliters per 100 ml, it is difficult to obtain a high-purity product that can be used practically as a heat medium in heat pipes, etc., unless it is thoroughly degassed and purified. In the same way as in the case of fluorocarbons, it takes several times as many processing steps or processing time to treat non-condensable substances such as air until bubbles no longer appear using the freezing method or equilibrium vapor pressure method, and it takes about 500 m
There was a problem in that it took several hours to purify perfluorocarbon No. 1. Furthermore, even if the purified liquid was distilled and injected into the heat pipe, the heat pipe that had been injected with 5 to 30% of the original fraction did not show satisfactory thermal resistance, which did not occur in the case of fluorocarbons. This phenomenon occurred, and there was a problem that the conventional method could not sufficiently purify the product.
課題を解決するための手段
本発明者らは、前記問題点を克服すべく鋭意研究を重ね
た結果、意外にも撹拌処理等によりその目的を達成でき
ることを見出し、本発明をなすに至った。Means for Solving the Problems The present inventors have conducted extensive research to overcome the above-mentioned problems, and have unexpectedly discovered that the object can be achieved by a stirring process, etc., and have accomplished the present invention.
すなわち本発明は、パーフルオロカーボンの液層を撹拌
処理、ないし振動処理することを特徴とするパーフルオ
ロカーボンの精製方法を提供するものである。That is, the present invention provides a method for purifying perfluorocarbon, which is characterized by subjecting a liquid layer of perfluorocarbon to a stirring treatment or a vibration treatment.
作用
パーフルオロカーボンの液層を撹拌、ないし振動させる
方式により、パーフルオロカーボンの液中に溶存する空
気等の非凝縮性物質をスムースにかつ迅速に除去するこ
とができる。その理由は、従来方法にて非凝縮性物質の
泡が出なくなるまで処理しても充分な精製物が得られな
いのと同様、不明である。By stirring or vibrating the perfluorocarbon liquid layer, non-condensable substances such as air dissolved in the perfluorocarbon liquid can be smoothly and quickly removed. The reason for this is unknown, just as conventional methods do not yield sufficient purified products even when treated until no bubbles of non-condensable substances are produced.
発明の構成要素の例示
本発明が精製の対象とするものはパーフルオロカーボン
である。就中、平均分子量が100〜1000、ないし
沸点が30〜300℃のC1F 2n+2型のものであ
る。酸素、窒素、水素の如き異種元素を1重量%以下、
就中0.1重量%以下含有していてもよい。かかるパー
フルオロカーボンは、例えば「フロリナート」の商品名
(スリーエム社)などで市販されている。Exemplification of Components of the Invention The target of the present invention is perfluorocarbon. Among them, C1F 2n+2 type having an average molecular weight of 100 to 1000 and a boiling point of 30 to 300°C. Less than 1% by weight of foreign elements such as oxygen, nitrogen, and hydrogen,
In particular, it may be contained in an amount of 0.1% by weight or less. Such perfluorocarbons are commercially available, for example, under the trade name "Fluorinert" (3M).
精製は、添付図面に例示した如く、パーフルオロカーボ
ンの液層1を撹拌処理、ないし振動処理することにより
行われる。その際、回倒の如(パーフルオロカーボンの
液層1の上にそれに不溶な液体の層2を設ける方式など
、パーフルオロカーボンの揮散防止手段を講じることが
好ましい。なお前記の回倒では、マグネチックスターラ
ー3を介してパーフルオロカーボンの液層1を撹拌する
ようになっている。また図中の4は容器、5は分岐管、
6はコックである。Purification is carried out by stirring or vibrating the perfluorocarbon liquid layer 1, as illustrated in the accompanying drawings. At this time, it is preferable to take measures to prevent the perfluorocarbon from volatilizing, such as spinning (a method of providing a liquid layer 2 insoluble in the perfluorocarbon liquid layer 1 on top of the perfluorocarbon liquid layer 1). The perfluorocarbon liquid layer 1 is stirred through a stirrer 3. In the figure, 4 is a container, 5 is a branch pipe,
6 is the cook.
前記において用いる液体(2)は、パーフルオロカーボ
ンに不溶、就中その溶解度が11000pp以下で、か
つ上層に位置するようパーフルオロカーボンよりも比重
が軽いものであればよい。一般には水などが用いられる
。液体の使用量は、容器の形態等に基づく表面積にもよ
るが一般には、パーフルオロカーボンの液層の上に少な
くとも2 mmの厚さで層が形成されることが好ましい
。The liquid (2) used above may be one that is insoluble in perfluorocarbon, particularly has a solubility of 11,000 pp or less, and has a specific gravity lighter than the perfluorocarbon so that it is located in the upper layer. Water is generally used. Although the amount of liquid used depends on the surface area based on the shape of the container, etc., it is generally preferred that a layer with a thickness of at least 2 mm be formed on the liquid layer of perfluorocarbon.
本発明において撹拌処理、ないし振動処理の方式につい
ては特に限定はない。マグネチックスクーラー等による
撹拌処理や、超音波振動方式等による振動処理などで充
分に目的を達成することができる。なお、撹拌と振動の
画処理を加えてもよい。また、処理に際し吸引等による
減圧処理を加えることにより、処理時間の短縮をはかる
ことができる。処理温度は、パーフルオロカーボンの凍
結温度超から沸点未満までの範囲で適宜に決定してよい
。高温処理の場合、上記した必要に応じ用いる揮散防止
用の液にはパーフルオロカーボンよりも高沸点のものが
用いられる。In the present invention, there is no particular limitation on the method of stirring treatment or vibration treatment. The purpose can be sufficiently achieved by stirring treatment using a magnetic cooler or the like, or vibration treatment using an ultrasonic vibration method or the like. Note that image processing of stirring and vibration may be added. Further, by adding pressure reduction treatment by suction or the like during the treatment, the treatment time can be shortened. The treatment temperature may be determined as appropriate within the range from above the freezing temperature of the perfluorocarbon to below the boiling point. In the case of high-temperature treatment, the above-mentioned volatilization prevention liquid used as necessary has a higher boiling point than perfluorocarbon.
本発明の方法により精製処理されたパーフルオロカーボ
ンは、高純度物としてそのまま例えば熱媒体、絶縁油、
洗浄液などとして実用に供してもよいし、さらに蒸留す
るなどして実用に供してもよい。また、純度をより一層
向上させるべく、凍結法や平衡蒸気圧法等の他の精製方
法を併用してもよい。The perfluorocarbon purified by the method of the present invention can be used as a high-purity product as it is, for example, as a heating medium, insulating oil, etc.
It may be put to practical use as a cleaning liquid or the like, or it may be further distilled and put to practical use. Further, in order to further improve the purity, other purification methods such as freezing method and equilibrium vapor pressure method may be used in combination.
発明の効果
本発明によれば、パーフルオロカーボンの液層に撹拌、
ないし振動を加えるだけの簡単な操作、かつ簡単な設備
で、パーフルオロカーボンの液中に溶存する空気等の非
凝縮性物質をスムースに、かつ速やかに除去することが
でき、処理効率、精製度に優れている。Effects of the Invention According to the present invention, the liquid layer of perfluorocarbon is stirred,
Non-condensable substances such as air dissolved in perfluorocarbon liquid can be removed smoothly and quickly with simple operations such as applying vibration or vibration, improving processing efficiency and purity. Are better.
実施例1
500ml容のフラスコに平均分子量340、沸点56
°Cのフロリナート(テトラデカフルオルヘキサン)1
00mlと水70m lを入れ、マグネチックスターラ
ーの配置下、軽比重に基づきフロリナートの液層の上に
水層が形成された状態で常温下、撹拌を開始して20分
間撹拌処理を行い、精製液を得た。Example 1 Average molecular weight 340, boiling point 56 in a 500 ml flask
Fluorinert (tetradecafluorohexane) 1 °C
00 ml and 70 ml of water were placed, and under the arrangement of a magnetic stirrer, stirring was started at room temperature with a water layer formed on top of the Fluorinert liquid layer based on its light specific gravity, and the stirring process was performed for 20 minutes to purify. I got the liquid.
実施例2
実施例1に準じて精製液を得、それを液体窒素による凍
結法で2回脱気処理したのち蒸留して蒸留液からなる精
製液を得た。Example 2 A purified liquid was obtained according to Example 1, degassed twice by freezing with liquid nitrogen, and then distilled to obtain a purified liquid consisting of a distillate.
実施例3
マグネチックスターラーによる撹拌方式に代えて、超音
波振動装置による振動方式で10分間処理したほかは実
施例1に準じて精製液を得た。Example 3 A purified liquid was obtained in the same manner as in Example 1, except that instead of the stirring method using a magnetic stirrer, the treatment was performed using a vibration method using an ultrasonic vibrator for 10 minutes.
実施例4 水を用いないほかは実施例3に準じて精製液を得た。Example 4 A purified liquid was obtained according to Example 3 except that water was not used.
実施例5
実施例3に準じて精製液を得、それを液体窒素による凍
結法で2回脱気処理したのち蒸留して蒸留液からなる精
製液を得た。Example 5 A purified liquid was obtained according to Example 3, which was degassed twice by freezing with liquid nitrogen, and then distilled to obtain a purified liquid consisting of a distillate.
比較例1
実施例1と同じフロリナート100m1を液体窒素によ
る凍結法で6回脱気処理して精製液を得た。Comparative Example 1 100 ml of the same Fluorinert as in Example 1 was degassed six times by freezing with liquid nitrogen to obtain a purified liquid.
比較例2
実施例1と同じフロリナート100m1を温度−20℃
、真空度30Torrで平衡蒸気圧法により脱気処理し
て精製液を得た。Comparative Example 2 Fluorinert 100ml same as Example 1 was heated to -20°C.
A purified liquid was obtained by degassing using the equilibrium vapor pressure method at a vacuum degree of 30 Torr.
評価試験
実施例、比較例で得た精製液20m1を外径15.88
順、内径14 、3 mm 、長さ840 mmで内部
溝付きの銅パイプに、真空度8 XIO” Torrに
て真空注入し、封止してヒートパイプを形成し、入力6
0Wでの熱抵抗を調べた。20ml of the purified liquid obtained in the evaluation test example and comparative example was prepared with an outer diameter of 15.88
A copper pipe with an inner diameter of 14.3 mm and a length of 840 mm and an internal groove was vacuum injected at a vacuum level of 8 XIO" Torr and sealed to form a heat pipe.
The thermal resistance at 0W was investigated.
結果を表に示した。The results are shown in the table.
なお表には、実施例、比較例の精製液を得るのに要した
処理所要時間を併記した。The table also shows the processing time required to obtain purified liquids in Examples and Comparative Examples.
添付図面は、本発明方法を例示した説明図である。 1:パーフルオロカーボンの液層 2:不溶の液層 3:マグネチックスターラー 4:容器 5:分岐管 6:コック The accompanying drawings are explanatory diagrams illustrating the method of the present invention. 1: Perfluorocarbon liquid layer 2: Insoluble liquid layer 3: Magnetic stirrer 4: Container 5: Branch pipe 6: Cook
Claims (1)
動処理することを特徴とするパーフルオロカーボンの精
製方法。1. A method for purifying perfluorocarbon, which comprises subjecting a liquid layer of perfluorocarbon to stirring or vibration treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19341490A JPH0482845A (en) | 1990-07-20 | 1990-07-20 | Purification of perfluorocarbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19341490A JPH0482845A (en) | 1990-07-20 | 1990-07-20 | Purification of perfluorocarbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0482845A true JPH0482845A (en) | 1992-03-16 |
Family
ID=16307566
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19341490A Pending JPH0482845A (en) | 1990-07-20 | 1990-07-20 | Purification of perfluorocarbon |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0482845A (en) |
-
1990
- 1990-07-20 JP JP19341490A patent/JPH0482845A/en active Pending
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU94046087A (en) | Method of purified terephthalic acid production and apparatus for water steam injection used in method of purified terephthalic acid production | |
| KR930008193A (en) | Method of cleaning silicon ingot | |
| JPS61200194A (en) | Removal of gas from liquid crystal material | |
| JPH0482845A (en) | Purification of perfluorocarbon | |
| JPS60239491A (en) | Method for stabilizing silicon-containing methacrylic acid ester | |
| JPH0482846A (en) | Purification of perfluorocarbon | |
| JPH0482847A (en) | Purification of perfluorocarbon | |
| JPH0975601A (en) | Low temperature fractionating apparatus by ultrasonic wave and production of alcoholic drinks using the apparatus | |
| CN1668542A (en) | Sol-gel process for the preparation of vitreous films possessing high adhesion properties and stable colloidal solutions suitable for its carrying out the same | |
| JPS58175473A (en) | Clarification of soy | |
| JPH06107796A (en) | Purification of modified silicone oil | |
| JPS5959644A (en) | Process for concentration of eicosapentaenoic acid in fish oil | |
| CN223416749U (en) | A rapid distillation system for highly viscous materials | |
| TWM535714U (en) | Sulfur removal device and improvement structure of distillation apparatus containing the same | |
| JPH05171481A (en) | Degreasing and cleaning method and its apparatus | |
| US2008955A (en) | Process for reducing the water content of liquids | |
| RU2230094C1 (en) | Residual petroleum product distillation method | |
| SU1332132A1 (en) | Method of cleaning equipment from carbon deposits | |
| SU1634660A1 (en) | Method for removing dissolved oxygen from organic solvents based on aromatic or saturated aliphatic hydrocarbons | |
| JPH0543699A (en) | Method for purifying silicone oil | |
| US625650A (en) | bryan | |
| JP3281841B2 (en) | Treatment method of maleimide distillation residue | |
| JPH03249917A (en) | Method for recovering solvent | |
| SU724157A1 (en) | Mercury purificating plant | |
| GB189703483A (en) | Improved Methods of and Apparatus for Cooling and Evaporating. |