JPH0236155A - Method for treating fluorinated product - Google Patents
Method for treating fluorinated productInfo
- Publication number
- JPH0236155A JPH0236155A JP18370488A JP18370488A JPH0236155A JP H0236155 A JPH0236155 A JP H0236155A JP 18370488 A JP18370488 A JP 18370488A JP 18370488 A JP18370488 A JP 18370488A JP H0236155 A JPH0236155 A JP H0236155A
- Authority
- JP
- Japan
- Prior art keywords
- fluorinated product
- heating
- fluorination
- hydrogen fluoride
- perfluorotrialkylamine
- 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.)
- Granted
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (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、トリアルキルアミンのフッ素化により得られ
たパーフルオロトリアルキルアミンを含むフッ素化生成
物1に%定の温度で加熱処理することによって、フッ化
水素の発生ノ少すいパーフルオロトリアルキルアミンを
得る方法に関する。Detailed Description of the Invention [Industrial Field of Application] The present invention provides a method for heat-treating a fluorinated product 1 containing a perfluorotrialkylamine obtained by fluorination of a trialkylamine at a certain temperature. This invention relates to a method for obtaining a perfluorotrialkylamine that generates less hydrogen fluoride.
〔従来技術及び発明が解決しようとする課題〕トリアル
キルアミンのフッ素化により得らレタパーフルオロトリ
アルキルアミンは、化学的に安定であり、熱伝導性が高
く、不燃性であり、また無毒であるため、電子部品信頼
性テスト用媒体、m子機器の直接冷却の為の媒体、気相
ハンダ付は用熱媒体等として利用されている。しかしな
がら、パーフルオロトリアルキルアミンを気相ハンダ付
は用熱媒体等として用いるためにその沸点まで加熱して
気化させろか、又は紫外線を照射すると、フッ化水素が
発生するという問題があった。加熱した場合のフッ化水
素の発生量は加熱初期に多く、その後、徐々に減少する
が、ある程度まで減少すると沸点での加熱を長時間性な
っても最早それ以上は減少しない。フッ化水素は腐食性
が高いために極わずか発生しても電子部品の損傷や装置
材質の腐食の原因となるため、フッ化水素の発生しない
パーフルオロトリアルキルアミンが求められていた。[Prior art and problems to be solved by the invention] Retaperfluorotrialkylamines obtained by fluorination of trialkylamines are chemically stable, have high thermal conductivity, are nonflammable, and are nontoxic. Therefore, it is used as a medium for reliability testing of electronic components, a medium for direct cooling of electronic devices, and a heating medium for vapor phase soldering. However, since perfluorotrialkylamine is used as a heat medium for vapor phase soldering, there is a problem in that hydrogen fluoride is generated when it is heated to its boiling point to vaporize it or when it is irradiated with ultraviolet rays. The amount of hydrogen fluoride generated during heating is large at the beginning of heating, and then gradually decreases, but once it has decreased to a certain point, it no longer decreases even if heating at the boiling point is continued for a long time. Hydrogen fluoride is highly corrosive, so even a small amount of hydrogen fluoride can cause damage to electronic components and corrosion of equipment materials.Therefore, a perfluorotrialkylamine that does not generate hydrogen fluoride has been desired.
そこで1本発明者らは、沸点まで加熱してもフッ化水素
が発生せず、気相ハンダ付は用熱媒体等として好適に使
用し得るパーフルオロトリアルキルアミンを得ることを
目的として鋭意研究を続けてきた。その結果、トリアル
キルアミンのフッ素化で得られたフッ素化生成物を特定
の温度範囲で加熱処理することよって上記の目的を達成
し得ることを見出し、本発明を完成させるに至った。Therefore, the present inventors conducted intensive research with the aim of obtaining a perfluorotrialkylamine that does not generate hydrogen fluoride even when heated to the boiling point and can be suitably used as a heat medium for vapor phase soldering. I have continued to do so. As a result, the inventors discovered that the above object can be achieved by heat-treating a fluorinated product obtained by fluorination of trialkylamine in a specific temperature range, and completed the present invention.
即ち、本発明は、トリアルキルアミンのフッ素化により
得られたパーフルオロトリアルキルアミンを含むフッ素
化生成物を、次式1式%
を満足する温度に加熱することを特徴とするフッ素化生
成物の処理方法である。That is, the present invention provides a fluorinated product characterized by heating a fluorinated product containing a perfluorotrialkylamine obtained by fluorination of a trialkylamine to a temperature satisfying the following formula 1. This is a processing method.
本発明で使用し得るトリアルキルアミンは、公知のもの
が何ら制限なく使用し得る。一般にフッ素化によって得
られるパーフルオロトリアルキルアミンを電子機器の直
接冷却の為の媒体や気相ハンダ付は用熱媒体等として用
いる場合には沸点を適当な値とするために、トリアルキ
ルアミンの炭素数は4〜21.さらに9〜18であるこ
とが好ましい。本発明に於いて好適に用いられるトリア
ルキルアミンを具体的に示すと、例えは、トリプロピル
アミン、ジプロピルブチルアミン、プロピルジブチルア
ミン、トリブチルアミン、ジブチルペンチルアミン、プ
チルジペンチルアミン。As the trialkylamine that can be used in the present invention, any known trialkylamine can be used without any restriction. Generally, when perfluorotrialkylamine obtained by fluorination is used as a medium for direct cooling of electronic equipment or as a heating medium for vapor phase soldering, it is necessary to use trialkylamine to maintain the boiling point at an appropriate value. Carbon number is 4-21. Furthermore, it is preferable that it is 9-18. Specific examples of trialkylamines preferably used in the present invention include tripropylamine, dipropylbutylamine, propyldibutylamine, tributylamine, dibutylpentylamine, and butyldipentylamine.
ジブチルエチルアミン、トリペンチルアミン。Dibutylethylamine, tripentylamine.
ジベンチルヘキシルアミン、ペンチルジヘキシルアミン
、ジペンチルメチルアミン、トリへ千ジルアミン等であ
る。These include dibentylhexylamine, pentyldihexylamine, dipentylmethylamine, trihexylamine, and the like.
上記したトリアルキルアミンのフッ素化方法としては、
パーフル40トリアル牛ルアミンを生成することのでき
る公知のフッ素化方法が伺ら制限なく採用することがで
きる。例えば、フッ素ガスによる直接フツ素化方法。As a method for fluorinating the above-mentioned trialkylamine,
Any known fluorination method capable of producing Perflu 40 trial bovine luamine can be employed without limitation. For example, direct fluorination method using fluorine gas.
電解フツ素化方法及び高原子価金属フッ素化物によるフ
ッ素化方法、或いは、これらを適宜組合わせたフッ素化
方法等が好適に採用される。An electrolytic fluorination method, a fluorination method using a high-valent metal fluoride, or a fluorination method that is an appropriate combination of these methods is preferably employed.
本発明に於いては、こうして得られたフッ素化生成物、
好ましくはさらに中和、蒸留或いは公知の方法により精
製されたフッ素化生成物が加熱の対象となる。加熱の温
度は、次式
%式%
を満足する温度である。上記の下限温度よりも低い場合
には、フッ化水素発生の問題が解決できず、逆に高い場
合には、パーフルオロトリアルキルアミンの分解を生じ
ろために好ましくない。フッ化水素発生の低減及びパー
フルオロトリアルキルアミンの分解防止の観点から、加
熱の温度は次式
%式%
〔ここで、T及びNは前記式と同様である。〕で示され
る温度範囲であることが好ましい。In the present invention, the fluorinated product thus obtained,
Preferably, the fluorinated product, which has been further purified by neutralization, distillation or other known methods, is subjected to heating. The heating temperature is a temperature that satisfies the following formula: %. If the temperature is lower than the above-mentioned lower limit temperature, the problem of hydrogen fluoride generation cannot be solved, and if it is higher than the lower limit temperature, the perfluorotrialkylamine may be decomposed, which is not preferable. From the viewpoint of reducing the generation of hydrogen fluoride and preventing the decomposition of perfluorotrialkylamine, the heating temperature is determined by the following formula (%) [Here, T and N are the same as in the above formula. ] is preferably within the temperature range.
例えは、加熱処理の対象が、パーフルオロトリペンチル
アミンを含むフッ素化生成物の場合には、加熱温度は、
240〜420℃の範囲でなければならず、270〜3
80℃の範囲であることが好ましい。For example, when the object of heat treatment is a fluorinated product containing perfluorotripentylamine, the heating temperature is
Must be in the range of 240-420℃, 270-3
Preferably, the temperature is in the range of 80°C.
加熱の時間は特に制限されず、通常は数秒〜数を時開の
範囲から選択される。The heating time is not particularly limited, and is usually selected from a range of several seconds to several hours.
加熱の方法は特に制限されず、圧力容器を用いて処理対
象のフッ素化生成物を液状態で加熱しても良く、また、
処理対象のフッ素化生成物を気化させて気体状態で加熱
しても良(・0加熱時の雰囲気は特に制限されず、N2
ガスやArガスなどを用いた不活性雰囲気で加熱しても
良く、また、空気等を用いた酸化性雰囲気で加熱しても
良い。The heating method is not particularly limited, and the fluorinated product to be treated may be heated in a liquid state using a pressure vessel;
The fluorinated product to be treated may be vaporized and heated in a gaseous state (the atmosphere at the time of heating is not particularly limited, and N2
Heating may be performed in an inert atmosphere using gas, Ar gas, or the like, or may be heated in an oxidizing atmosphere using air or the like.
トリアルキルアミンのフッ素化により得られたパーフル
オロトリアルキルアミンを含むフッ素化生成物をそのま
ま沸点まで加熱するか又は紫外線な照射するとフッ化水
素が発生し、沸点での加熱や紫外線の照射を長時間統け
ても7ツ化水素は発生し続ける。ところが、本発明の方
法により加熱処理されたフッ素化生成物は、沸点までの
加熱や光の照射によってもほとんどフッ化水素を発生し
ない。この理由は明確ではないが、本発明者らは次のよ
うに推測している。即ち、トリアルキルアミンのフッ素
化により得られたフッ素化生成物中にはパーフルオロト
リアルキルアミンのみならず不完全フッ素化物も含まれ
ており、フッ素化生成物を沸点まで加熱すると、この不
完全フッ素化物が分解してフッ化水素が発生するが、本
発明の方法により加熱処理することにより不完全フッ素
化物のほとんどが分解し、そのためにフッ化水素の発生
が低減されろものと思われる。When a fluorinated product containing perfluorotrialkylamine obtained by fluorination of trialkylamine is heated directly to the boiling point or irradiated with ultraviolet rays, hydrogen fluoride is generated. Hydrogen heptadide continues to be generated even if time passes. However, the fluorinated product heat-treated by the method of the present invention hardly generates hydrogen fluoride even when heated to the boiling point or irradiated with light. Although the reason for this is not clear, the present inventors speculate as follows. That is, the fluorinated product obtained by fluorination of trialkylamine contains not only perfluorotrialkylamine but also incompletely fluorinated products, and when the fluorinated product is heated to the boiling point, this incompletely fluorinated product is removed. Fluorinated substances are decomposed to generate hydrogen fluoride, but most of the incompletely fluorinated substances are decomposed by heat treatment according to the method of the present invention, and therefore the generation of hydrogen fluoride is thought to be reduced.
フッ素化生成物が、炭素数5以上のアル中ル基を分子中
に有するパーフルオロ) IJアル千シルアミン含む場
合、沸点での加熱により毒性化合物であるパーフルオロ
インブテンな発生するが、本発明の方法で加熱処理を行
なうことにより、その発生を完全に防止することができ
る。When the fluorinated product contains a perfluorinated alkylamine having an alkyl group having 5 or more carbon atoms in its molecule, perfluoroinbutene, a toxic compound, is generated by heating at the boiling point. By performing heat treatment using this method, this occurrence can be completely prevented.
本発明の方法により処理されたフッ素化生成物は、7ツ
化水素の発生がほとんどないため、気相ハンダ材用熱媒
体等として好適に使用し得る他、電子部品の試験用媒体
や電子機器の絶縁冷却剤等としても使用することができ
る。Since the fluorinated product treated by the method of the present invention hardly generates hydrogen heptadide, it can be suitably used as a heating medium for vapor phase soldering materials, and can also be used as a testing medium for electronic components and for electronic equipment. It can also be used as an insulating coolant, etc.
本発明をさらに具体的に説明するために以下実施例及び
比較例を掲げるが、本発明はこれらの実施例に限定され
るものではない。EXAMPLES Examples and comparative examples are listed below to further specifically explain the present invention, but the present invention is not limited to these examples.
実施例1
無水7フ化水素酸とトリペンチルアミンを原料とし、後
者の濃度をIO重量%として、ニッケル製電解槽(電極
面積10dイ、電流20A、容量3.51りを用いて電
解フッ素化を開始した。無水フッ化水素酸とトリペンチ
ルアミンを連続的に供給しながら、生・成するフッ素化
物を電解槽の下部より間欠的に抜きたした。これを40
重1%のカセイソーダ水溶液とジイソブチルアミンの等
容量混合物中で120時間還流して脱フツ化水素し、水
洗後蒸留を行なうことにより、パーフルオロトリペンチ
ルアミンを主体とするフッ素化生成物を得た。Example 1 Electrolytic fluorination was carried out using anhydrous 7-hydrofluoric acid and tripentylamine as raw materials and using a nickel electrolytic bath (electrode area 10 d, current 20 A, capacity 3.51 While continuously supplying anhydrous hydrofluoric acid and tripentylamine, the produced fluoride was intermittently extracted from the bottom of the electrolytic cell.
A fluorinated product mainly consisting of perfluorotripentylamine was obtained by dehydrofluorination by refluxing for 120 hours in an equal volume mixture of a 1% by weight aqueous solution of caustic soda and diisobutylamine, washing with water, and then distilling. .
得られたフッ素化生成物200.9を400紅容置のS
US製オートクレーブに入れ、窒素ガスにより不活性雰
囲気としたのち、表1に示す条件で加熱処理した。なお
、300℃で加熱処理した時、容器内部の圧力は45製
となった。The obtained fluorinated product 200.9 was placed in a 400ml container.
The sample was placed in a US autoclave, and after creating an inert atmosphere with nitrogen gas, it was heat-treated under the conditions shown in Table 1. Note that when the heat treatment was performed at 300°C, the pressure inside the container was 45.
加熱処理したフッ素化生成物100Fを、還流器を上部
に配した200mのナス型フラスコにいれて液を加熱し
、5時間大気圧下で?S臆させた。液温度は215℃で
あった。この間、80 lLt/ m流量の窒素ガスを
液に吹き込み、発生するフッ化水素を150−の0.0
1mo1/l水酸化カリウム水溶液に吸収させた。The heat-treated fluorinated product 100F was placed in a 200 m eggplant-shaped flask equipped with a reflux device at the top, and the liquid was heated under atmospheric pressure for 5 hours. S made me scared. The liquid temperature was 215°C. During this time, nitrogen gas was blown into the liquid at a flow rate of 80 lLt/m, and the generated hydrogen fluoride was
It was absorbed into a 1 mo1/l aqueous potassium hydroxide solution.
この水酸化カリウム水溶液に含まれるフッ素イオン濃度
をイオンクロマトアナライザー(横河北辰電機製、モデ
ルIC100)で測定することにより7ツ化水素発生量
を求め、フッ素化生成物単位重量当りのフッ化水素発生
量(mg−(HF) /ゆ−(フッ素化生成物)〕に換
算した。結果を表1に記した。なお、この値を沸騰時7
ツ化水素発生量と呼ぶことにする。By measuring the fluorine ion concentration contained in this potassium hydroxide aqueous solution with an ion chromato analyzer (manufactured by Yokogawa Hokushin Electric, model IC100), the amount of hydrogen heptadium generated was determined, and the amount of hydrogen fluoride generated per unit weight of the fluorinated product was determined. The amount generated was converted to mg-(HF)/Y-(fluorinated product)].The results are shown in Table 1.This value was calculated as
This will be referred to as the amount of hydrogen tsuride generated.
表1には比較のために本発明の温度範囲外で加熱した場
合の結果も併せて記した。なお、比較例/Wh2〜鳥4
は大気圧下の沸点(215℃)で加熱処理したものであ
る。また、比較例ノに5は加熱処理することなく、沸騰
時フッ化水素発生量を求めた結果である。For comparison, Table 1 also shows the results of heating outside the temperature range of the present invention. In addition, comparative example/Wh2 to Bird 4
is heat-treated at the boiling point (215° C.) under atmospheric pressure. Further, Comparative Example No. 5 shows the results of determining the amount of hydrogen fluoride generated during boiling without heat treatment.
また、表1の実施例A3及び、比較例ム5における沸騰
時7ツ化水素発生量の測定において、測定開始3時間後
の窒素ガス中に含まれるパーフルオロインブテンの濃度
を電子捕獲型検出器付きガスクロマトグラフ(柳本創作
所、G−2800EN)にて測定したところ、実施例/
I&3の場合には検出限界@ (o、oox卿)以下で
あり、比較例ノに5の場合には0905騨であった。In addition, in the measurement of the amount of hydrogen heptadide generated during boiling in Example A3 and Comparative Example M5 in Table 1, the concentration of perfluoroinbutene contained in the nitrogen gas 3 hours after the start of the measurement was detected by electron capture detection. When measured with an equipped gas chromatograph (Yanagimoto Sosakusho, G-2800EN), Example/
In the case of I&3, it was below the detection limit @ (o, oox sir), and in the case of Comparative Example No. 5, it was 0905.
さらに、表1の実施例A3の加熱処理条件で得たフッ素
化生成物6gと加熱処理前のフッ素化生成物6Iを各々
1cm角の透明石英セルに入れ、紫外線照射器(ウシオ
電機製[JSH−250D、20万LX)を用いて二つ
同時に紫外線を照射した。24時間後に各々の石英セル
を観察したところ、加熱処理したフッ素化生成物を入れ
た石英セルは何等の変化も認められなかったのに対し、
加熱処理前のフッ素化生成物を入れた石英セルは7ツ化
水素の発生により白濁した。Further, 6 g of the fluorinated product obtained under the heat treatment conditions of Example A3 in Table 1 and 6 I of the fluorinated product before heat treatment were placed in a 1 cm square transparent quartz cell, and an ultraviolet irradiator (manufactured by Ushio Inc. [JSH -250D, 200,000LX) were used to simultaneously irradiate two ultraviolet rays. When each quartz cell was observed after 24 hours, no changes were observed in the quartz cell containing the heat-treated fluorinated product;
The quartz cell containing the fluorinated product before heat treatment became cloudy due to the generation of hydrogen heptadide.
実施例2
反応原料としてトリブチルアミンを用いたほかは実施例
1と同様にして電解フッ素化、及び、後処理を行ないパ
ーフルオロトリブチルアミンを主体とするフッ素化生成
物を得た。Example 2 Electrolytic fluorination and post-treatment were carried out in the same manner as in Example 1, except that tributylamine was used as the reaction raw material, to obtain a fluorinated product mainly consisting of perfluorotributylamine.
これを実施例1と同様な装置で270℃にて7時間加熱
処理したところ、回収率は9&6%、沸騰時7ツ化水素
発生量は0.1mg−(HF)/kg−(7ツ素化生成
物)以下であった。When this was heat-treated at 270°C for 7 hours using the same equipment as in Example 1, the recovery rate was 9% and 6%, and the amount of hydrogen heptadide generated during boiling was 0.1 mg-(HF)/kg-(sulfur heptadide). reaction products) were as follows.
実施例3
反応原料としてトリヘキシルアミンを用いたほかは実施
例1と同様にして電解フッ素化、及び、後処理を行ない
パーフルオロトリヘキシルアミンを主体とするフッ素化
生成物を得た。これを空気を用いた雰囲気下で330℃
にて7時間加熱処理したところ、回収率は9&7%、沸
騰時フッ化水素発生量は0.1119− (HF)/ゆ
−(フッ素化生成物)であった。Example 3 Electrolytic fluorination and post-treatment were carried out in the same manner as in Example 1 except that trihexylamine was used as a reaction raw material to obtain a fluorinated product mainly consisting of perfluorotrihexylamine. This was heated at 330°C in an atmosphere using air.
When the mixture was heat-treated for 7 hours, the recovery rate was 9% and 7%, and the amount of hydrogen fluoride generated during boiling was 0.1119-(HF)/Y-(fluorinated product).
Claims (1)
ーフルオロトリアルキルアミンを含むフッ素化生成物を
、次式 14N+30≦T≦420 [ここで、T=温度(℃) N=トリアルキルアミンの全炭素数] を満足する温度に加熱することを特徴とするフッ素化生
成物の処理方法。(1) The fluorinated product containing perfluorotrialkylamine obtained by fluorination of trialkylamine is expressed using the following formula: 14N+30≦T≦420 [where, T=temperature (°C), N=total of trialkylamine] A method for treating a fluorinated product, characterized by heating it to a temperature that satisfies [carbon number].
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18370488A JPH078840B2 (en) | 1988-07-25 | 1988-07-25 | Method for treating fluorinated products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18370488A JPH078840B2 (en) | 1988-07-25 | 1988-07-25 | Method for treating fluorinated products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0236155A true JPH0236155A (en) | 1990-02-06 |
| JPH078840B2 JPH078840B2 (en) | 1995-02-01 |
Family
ID=16140494
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18370488A Expired - Fee Related JPH078840B2 (en) | 1988-07-25 | 1988-07-25 | Method for treating fluorinated products |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH078840B2 (en) |
-
1988
- 1988-07-25 JP JP18370488A patent/JPH078840B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH078840B2 (en) | 1995-02-01 |
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