JPH115813A - Low molecular weight fluorine-containing resin powder and its production - Google Patents

Low molecular weight fluorine-containing resin powder and its production

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Publication number
JPH115813A
JPH115813A JP15953497A JP15953497A JPH115813A JP H115813 A JPH115813 A JP H115813A JP 15953497 A JP15953497 A JP 15953497A JP 15953497 A JP15953497 A JP 15953497A JP H115813 A JPH115813 A JP H115813A
Authority
JP
Japan
Prior art keywords
fluorine
molecular weight
containing resin
gas
resin powder
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
JP15953497A
Other languages
Japanese (ja)
Inventor
Takashi Suenaga
隆 末永
Norimichi Nogami
謙道 野上
Keizo Kojima
敬三 児島
Mitsuya Ohashi
満也 大橋
Hiromi Sugimoto
博美 杉本
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.)
Central Glass Co Ltd
Original Assignee
Central Glass 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 Central Glass Co Ltd filed Critical Central Glass Co Ltd
Priority to JP15953497A priority Critical patent/JPH115813A/en
Publication of JPH115813A publication Critical patent/JPH115813A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To obtain low molecular weight fluorine-containing resin powder excellent in lubricating property, water-repelling and oil-repelling property, etc., and provide a method for producing the powder. SOLUTION: This low molecular weight fluorine-containing resin powder is obtained by cooling reaction-produced gas of melted fluorinecontaining resin with fluorine gas and completely fluorinated and has 700-4,000 molecular weight. The powder does not moisten with acetone and has high water-repelling and oil-repelling property. This method for producing the resin powder comprises retaining fluorine concentration in atmospheric gas to >=0.1 vol.% until the atmospheric temperature becomes <=50 deg.C from a reactor to a recovering vessel in a method for heating the fluorine containing resin powder in the temperature range from a melting point of the resin powder to 600 deg.C to melt the resin, subjecting the melted resin powder to contact reaction with at least one kind of molecular fluorine, nitrogen trifluoride, halogen fluoride and fluoride of rare gas, cooling gas produced by reaction to <=50 deg.C by a cooler and recovering the particles of the deposited low molecular weight fluorine-containing resin by a recovering vessel.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、撥水撥油性に優れ
る低分子量含フッ素樹脂粉末およびその製造方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a low molecular weight fluorine-containing resin powder having excellent water and oil repellency and a method for producing the same.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】従
来、潤滑剤や離型剤等に広く利用される低分子量含フッ
素樹脂は、種々の方法で製造されているが、なかでもポ
リテトラフルオロエチレン(PTFE)は、テトラフル
オロエチレン(TFE)のテロメリゼーションによる方
法、PTFEの熱分解による方法、PTFEの放射線
(X線、γ線)照射による分解による方法などがある。
2. Description of the Related Art Conventionally, low molecular weight fluororesins widely used as lubricants and mold release agents have been produced by various methods. (PTFE) includes a method by telomerization of tetrafluoroethylene (TFE), a method by thermal decomposition of PTFE, and a method by decomposition of PTFE by irradiation of radiation (X-ray, γ-ray).

【0003】上記従来法には、高温、高圧を使用するな
どの種々の問題点を含んでいるため、本出願人は、より
簡易な新規製造法を種々検討した結果、含フッ素樹脂を
分子状フッ素、三フッ化窒素、ハロゲン化フッ化物およ
び希ガスのフッ化物の少なくとも一種と接触反応させる
ことにより、高収率で、かつコントロールされた分子量
分布を持つ含フッ素樹脂の低分子量物が得られることを
見いだした(特公平1−49404号公報)。
The above-mentioned conventional method involves various problems such as the use of high temperature and high pressure, and as a result of various studies on a simpler new production method, the present applicant has found that a fluorine-containing resin has a molecular By contacting and reacting with at least one of fluorine, nitrogen trifluoride, halogenated fluoride and rare gas fluoride, a low-molecular-weight fluororesin having a high yield and a controlled molecular weight distribution can be obtained. (JP-B 1-449404).

【0004】また、PTFEをはじめとする含フッ素樹
脂の低分子量物は、表面エネルギーが小さいために、潤
滑性、非粘着性に優れており、潤滑剤や離型剤、またフ
ッ素樹脂系塗料として広く使用されている。最近、撥水
性や着雪防止を目的とした塗料やメッキへの添加剤とし
て利用されている。
[0004] Also, low molecular weight products of fluorine-containing resins such as PTFE are excellent in lubricity and non-adhesiveness due to low surface energy, and are used as lubricants, mold release agents, and fluororesin paints. Widely used. Recently, it has been used as an additive to paints and plating for the purpose of water repellency and prevention of snow formation.

【0005】しかし、従来の低分子量PTFEを添加し
たフッ素樹脂系塗料やメッキでは、塗布、メッキした直
後は高い撥水撥油性能を持つものもあるが、短期間の内
に撥水撥油性が低下し、実用に耐えるものがないのが現
状であり、そのためより撥水撥油性の高い低分子量PT
FE樹脂が望まれている。
However, some conventional fluororesin paints and platings to which low-molecular-weight PTFE is added have high water and oil repellency immediately after coating and plating. At present, there is no material that can be used for practical purposes.
FE resins are desired.

【0006】[0006]

【課題を解決するための具体的手段】本発明者らは、か
かる問題点について鋭意検討の結果、フッ素濃度を特定
濃度に保持することにより、より撥水撥油性の高い低分
子量含フッ素樹脂粉末を製造できることを見いだしたも
のである。
The inventors of the present invention have conducted intensive studies on such problems, and as a result, by keeping the fluorine concentration at a specific concentration, a low molecular weight fluorine-containing resin powder having higher water and oil repellency has been obtained. Can be manufactured.

【0007】すなわち本発明は、溶融した含フッ素樹脂
とフッ素系ガスとの反応生成ガスを冷却して得られたフ
ッ素化が完全に行われた分子量700〜4000の含フ
ッ素樹脂粉末であって、アセトンに濡れない高い撥水撥
油性を有する低分子量含フッ素樹脂粉末であって、反応
器で含フッ素樹脂を融点以上〜600℃に加熱して溶融
し、雰囲気温度200〜550℃において、分子状フッ
素、三フッ化窒素、ハロゲン化フッ化物および希ガスの
フッ化物の少なくとも1種と接触反応させ、発生する反
応生成ガスを冷却器で50℃以下に冷却して析出した低
分子量含フッ素樹脂の粒子を回収容器で回収する方法に
おいて、反応器から回収容器の間で雰囲気温度が50℃
以下になるまでの間、雰囲気ガス中のフッ素濃度を0.
1vol%以上に保持することを特徴とする低分子量含
フッ素樹脂粉末の製造方法を提供するものである。
That is, the present invention relates to a fluorine-containing resin powder having a molecular weight of 700 to 4000, which is obtained by cooling a reaction product gas of a molten fluorine-containing resin and a fluorine-based gas, and which is completely fluorinated. A low molecular weight fluorine-containing resin powder having high water / oil repellency which is not wetted by acetone. The fluorine-containing resin is heated to a melting point or higher to 600 ° C. in a reactor to be melted. Contact reaction with at least one of fluorine, nitrogen trifluoride, halogenated fluoride and rare gas fluoride, and the resulting reaction product gas is cooled to 50 ° C. or less by a cooler to deposit a low molecular weight fluorine-containing resin. In the method of collecting particles in a collection container, the ambient temperature is 50 ° C. between the reactor and the collection container.
Until it becomes less than or equal to, the fluorine concentration in the atmosphere gas is reduced to 0.
An object of the present invention is to provide a method for producing a low-molecular-weight fluorine-containing resin powder, which is maintained at 1 vol% or more.

【0008】本発明は、原料のフッ素樹脂と分子状フッ
素ガス等と反応させ、低分子量含フッ素樹脂を生成させ
て雰囲気温度を50℃以下に冷却するまでの間、雰囲気
ガス中のフッ素濃度を0.1vol%以上に保持するも
ので、フッ素濃度が、0.1vol%以上であれば、よ
り撥水撥油性の高い低分子量含フッ素樹脂(分子量:7
00〜4000)を製造できる。フッ素濃度が、0.1
vol%以上であれば特に限定されないが、経済性等か
ら0.1〜20vol%の範囲が好ましく、最適には
0.1〜10vol%の範囲が好ましい。フッ素濃度
が、0.1vol%未満だとフッ素化が完全に行われず
二重結合を生じたり他の原子が結合したりするため撥水
撥油性能が不十分となり好ましくない。
According to the present invention, the fluorine concentration in the atmosphere gas is reduced until the fluorine resin as a raw material is reacted with a molecular fluorine gas or the like to produce a low molecular weight fluorine-containing resin and cool the atmosphere temperature to 50 ° C. or less. When the fluorine concentration is 0.1 vol% or more, a low-molecular-weight fluorine-containing resin having a higher water / oil repellency (molecular weight: 7)
00 to 4000). When the fluorine concentration is 0.1
The volume is not particularly limited as long as it is at least vol%, but is preferably in the range of 0.1 to 20 vol%, and most preferably in the range of 0.1 to 10 vol%, from the viewpoint of economy. If the fluorine concentration is less than 0.1 vol%, fluorination is not completely performed, and a double bond is generated or another atom is bonded.

【0009】[0009]

【発明の実施の形態】以下、本発明を詳述する。図1
は、本発明における低分子量含フッ素樹脂粉末の製造工
程の概略図である。まず、2.5m3のニッケル製反応
器1に、原料2として分子量数十万〜数千万のPTFE
チップを例えば500Kg仕込み、窒素ガスで5%に希
釈したフッ素ガス3を供給しながら外部加熱により雰囲
気温度500℃まで昇温する。そのままの状態に数十時
間保持すると反応器の底部の溶融した原料2の表面層と
フッ素ガス3との反応により低分子量化したガス状のP
TFEが約500g/Hrの速度で生成する。ガス状と
なったPTFEは、他のガス成分、ここでは主に窒素ガ
スと、一部未反応フッ素ガス及び副生したフルオロカー
ボンガス等と共に反応器外に取り出され、つぎに反応器
3の出口に設けたガス冷却器4内において、50℃以下
に冷却する。冷却され低分子量化PTFEは1〜3μm
のPTFE粒子としてガス中より析出し、バッグフィル
ター5などの回収容器で捕集し回収される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. FIG.
FIG. 1 is a schematic view of a process for producing a low molecular weight fluororesin powder in the present invention. First, PTFE having a molecular weight of hundreds of thousands to tens of millions was placed in a 2.5 m 3 nickel reactor 1 as a raw material 2.
The chip is charged, for example, at 500 kg, and the temperature is raised to an ambient temperature of 500 ° C. by external heating while supplying a fluorine gas 3 diluted to 5% with nitrogen gas. When held as it is for several tens of hours, gaseous P whose molecular weight has been reduced by the reaction between the surface layer of the molten raw material 2 at the bottom of the reactor and the fluorine gas 3
TFE is produced at a rate of about 500 g / Hr. The gaseous PTFE is taken out of the reactor together with other gas components, here, mainly nitrogen gas, partially unreacted fluorine gas, by-product fluorocarbon gas, and the like. The gas is cooled to 50 ° C. or lower in the provided gas cooler 4. Cooled low molecular weight PTFE is 1-3 μm
Precipitates out of the gas as PTFE particles, and is collected and collected in a collection container such as the bag filter 5.

【0010】この一連の反応において、原料のPTFE
がフッ素ガスと反応し低分子量PTFEを生成し、冷却
器などで雰囲気温度を50℃以下にするまでの間、雰囲
気ガス中のフッ素濃度を0.1vol%以上に保持す
る。また、雰囲気ガス中のフッ素濃度は、バッグフィル
ター上部からの排ガスの分析により求めることができ、
反応器に供給するフッ素ガス量により任意に制御するこ
とができる。
In this series of reactions, the starting material PTFE
Reacts with fluorine gas to generate low molecular weight PTFE, and keeps the fluorine concentration in the atmosphere gas at 0.1 vol% or more until the atmosphere temperature is reduced to 50 ° C. or less by a cooler or the like. Also, the fluorine concentration in the atmosphere gas can be obtained by analyzing the exhaust gas from the upper part of the bag filter,
It can be arbitrarily controlled by the amount of fluorine gas supplied to the reactor.

【0011】本発明方法により製造した低分子量含フッ
素樹脂粉末は、潤滑剤や離型剤として優れた性能を持つ
ほか、従来にない高い撥水撥油性を持つため、長期間撥
水撥油性が低下しない塗膜やメッキの添加剤として優れ
た性能を持つものが得られるものである。
The low-molecular-weight fluorine-containing resin powder produced by the method of the present invention has excellent performance as a lubricant and a mold release agent, and has an unprecedented high water and oil repellency. An additive which does not decrease and has excellent performance as a coating or plating additive can be obtained.

【0012】[0012]

【実施例】以下、実施例により本発明を説明するが、か
かる実施例に限定されるものではない。
Hereinafter, the present invention will be described with reference to examples, but the present invention is not limited to these examples.

【0013】撥水撥油性の評価方法については、以下の
方法により実施した。本製造法によって製造した低分子
量PTFE粒子0.2gを試験管に入れ、これにアセト
ン100ccを加え、30秒間振動後1分間静置し、ア
セトンへの濡れ性を調べることにより低分子量PTFE
粒子の撥水撥油性を評価した。
The method for evaluating the water and oil repellency was as follows. 0.2 g of the low-molecular-weight PTFE particles produced by this production method is placed in a test tube, 100 cc of acetone is added to the test tube, and the mixture is shaken for 30 seconds and allowed to stand for 1 minute, and the wettability to acetone is examined.
The water / oil repellency of the particles was evaluated.

【0014】撥水撥油性の高い低分子量PTFE粒子
は、アセトンには濡れないため液面上に浮遊分離してし
まうが、撥水撥油性の低い低分子量PTFE粒子はアセ
トンに濡れ、沈殿する。
The low-molecular-weight PTFE particles having high water- and oil-repellency do not wet with acetone and thus float and separate on the liquid surface, but the low-molecular-weight PTFE particles having low water- and oil-repellency wet and precipitate with acetone.

【0015】また、本製造法によって製造した低分子量
PTFEの分子量は、質量分析(日立製 M-2500)によ
って測定し、また比較として用いたテロメリゼーション
で製造した低分子量PTFEの分子量は、米国特許第3
067262号で示されている融点と分子量の関係、分
子量=200/(685(1/融点(°K)−1/60
0))に従って算出した。
The molecular weight of the low molecular weight PTFE produced by this production method was measured by mass spectrometry (M-2500 manufactured by Hitachi), and the molecular weight of the low molecular weight PTFE produced by telomerization used as a comparison Patent No. 3
Relationship between melting point and molecular weight shown in No. 067262, molecular weight = 200 / (685 (1 / melting point (° K) −1/60)
0)).

【0016】実施例1 発明の実施の形態に記載した方法で、反応温度470℃
において、5vol%フッ素ガス30l/分を反応器に
供給し、低分子量含フッ素樹脂粉末を製造した。この
時、バッグフィルターに捕集された低分子量PTFEの
撥水撥油性及び分子量を前記方法により測定した。平均
の分子量は、3000で、この時のバッグフィルター上
部からの排ガス分析の結果を表1に示す。
Example 1 A reaction temperature of 470 ° C. was obtained by the method described in the embodiment of the present invention.
In the above, 30 l / min of 5 vol% fluorine gas was supplied to the reactor to produce a low molecular weight fluorine-containing resin powder. At this time, the water and oil repellency and the molecular weight of the low molecular weight PTFE collected in the bag filter were measured by the above method. The average molecular weight is 3000, and the results of exhaust gas analysis from the upper part of the bag filter at this time are shown in Table 1.

【0017】[0017]

【表1】 [Table 1]

【0018】実施例2 発明の実施の形態に記載した方法で、反応温度470℃
において、5vol%フッ素ガス40l/分を反応器に
供給し、低分子量含フッ素樹脂粉末を製造した。この
時、バッグフィルターに捕集された低分子量PTFEの
撥水撥油性及び分子量を前記方法により測定した。平均
の分子量は、3000で、この時のバッグフィルター上
部からの排ガス分析の結果を表2に示す。
Example 2 The reaction temperature was 470 ° C. according to the method described in the embodiment of the invention.
In the above, 40 l / min of 5 vol% fluorine gas was supplied to the reactor to produce a low molecular weight fluorine-containing resin powder. At this time, the water and oil repellency and the molecular weight of the low molecular weight PTFE collected in the bag filter were measured by the above method. The average molecular weight was 3000, and the results of exhaust gas analysis from the upper part of the bag filter at this time are shown in Table 2.

【0019】[0019]

【表2】 [Table 2]

【0020】比較例1 発明の実施の形態に記載した方法で、反応温度470℃
において、5vol%フッ素ガス10l/分を反応器に
供給し、低分子量含フッ素樹脂粉末を製造した。この
時、バッグフィルターに捕集された低分子量PTFEの
撥水撥油性及び分子量を前記方法により測定した。平均
の分子量は、3000で、この時のバッグフィルター上
部からの排ガス分析の結果を表3に示す。
Comparative Example 1 The reaction temperature was 470 ° C. according to the method described in the embodiment of the invention.
In the above, 10 l / min of 5 vol% fluorine gas was supplied to the reactor to produce a low molecular weight fluorine-containing resin powder. At this time, the water and oil repellency and the molecular weight of the low molecular weight PTFE collected in the bag filter were measured by the above method. The average molecular weight was 3000, and the results of exhaust gas analysis from the upper part of the bag filter at this time are shown in Table 3.

【0021】[0021]

【表3】 [Table 3]

【0022】比較例2 発明の実施の形態に記載した方法で、反応温度470℃
において、5vol%フッ素ガス20l/分を反応器に
供給し、低分子量含フッ素樹脂粉末を製造した。この
時、バッグフィルターに捕集された低分子量PTFEの
撥水撥油性及び分子量を前記方法により測定した。平均
の分子量は、3000で、この時のバッグフィルター上
部からの排ガス分析の結果を表4に示す。
Comparative Example 2 The reaction temperature was 470 ° C. according to the method described in the embodiment of the invention.
In the above, 20 l / min of 5 vol% fluorine gas was supplied to the reactor to produce a low molecular weight fluorine-containing resin powder. At this time, the water and oil repellency and the molecular weight of the low molecular weight PTFE collected in the bag filter were measured by the above method. The average molecular weight was 3000, and the results of exhaust gas analysis from the upper part of the bag filter at this time are shown in Table 4.

【0023】[0023]

【表4】 [Table 4]

【0024】実施例1、2、比較例1、2およびテロメ
リゼーションで製造した低分子量PTFE(平均分子
量:10000)の撥水撥油性評価を前記方法に従って
実施した。その結果を表5に示した。
Examples 1 and 2, Comparative Examples 1 and 2, and low-molecular-weight PTFE (average molecular weight: 10,000) produced by telomerization were evaluated for water / oil repellency according to the above-mentioned method. Table 5 shows the results.

【0025】[0025]

【表5】 [Table 5]

【0026】[0026]

【発明の効果】本発明方法により製造した低分子量含フ
ッ素樹脂粉末は、潤滑剤や離型剤として優れた性能を持
つほか、従来にない高い撥水撥油性を持つため、長期間
撥水撥油性が低下しない塗膜を持つフッ素樹脂系塗料や
メッキが得られるものである。
The low-molecular-weight fluorine-containing resin powder produced by the method of the present invention has excellent performance as a lubricant and a mold release agent, and has an unprecedentedly high water and oil repellency. A fluororesin-based paint or plating having a coating film whose oiliness does not decrease can be obtained.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明における低分子量含フッ素樹脂粉末の製
造工程の概略図を示す。
FIG. 1 is a schematic view of a process for producing a low molecular weight fluororesin powder according to the present invention.

【符号の説明】[Explanation of symbols]

1.反応器 2.原料(PTFE) 3.フッ素ガス 4.ガス冷却器 5.バッグフィルター 1. Reactor 2. Raw material (PTFE) 3. Fluorine gas 4. Gas cooler 5. Bag filter

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大橋 満也 埼玉県川越市今福中台2805番地 セントラ ル硝子株式会社化学研究所内 (72)発明者 杉本 博美 埼玉県川越市今福中台2805番地 セントラ ル硝子株式会社化学研究所内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Mitsuya Ohashi 2805 Imafukunakadai, Kawagoe City, Saitama Prefecture Central Research Laboratory of Glass Co., Ltd. (72) Inventor Hiromi Sugimoto 2805 Imafukunakadai, Kawagoe City, Saitama Prefecture Glass Research Laboratory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 溶融した含フッ素樹脂とフッ素系ガスと
の反応生成ガスを冷却して得られたフッ素化が完全に行
われた分子量700〜4000の含フッ素樹脂粉末であ
って、アセトンに濡れない高い撥水撥油性を有する低分
子量含フッ素樹脂粉末。
1. A fluorine-containing resin powder having a molecular weight of 700 to 4000, which is obtained by cooling a reaction product gas of a molten fluorine-containing resin and a fluorine-based gas, and which is completely fluorinated and wetted with acetone. Low molecular weight fluorine-containing resin powder with high water and oil repellency.
【請求項2】 反応器で含フッ素樹脂を融点以上〜60
0℃に加熱して溶融し、雰囲気温度200〜550℃に
おいて、分子状フッ素、三フッ化窒素、ハロゲン化フッ
化物および希ガスのフッ化物の少なくとも1種と接触反
応させ、発生する反応生成ガスを冷却器で50℃以下に
冷却して析出した低分子量含フッ素樹脂の粒子を回収容
器で回収する方法において、反応器から回収容器の間で
雰囲気温度が50℃以下になるまでの間、雰囲気ガス中
のフッ素濃度を0.1vol%以上に保持することを特
徴とする請求項1記載の低分子量含フッ素樹脂粉末の製
造方法。
2. The method according to claim 1, wherein the fluorine-containing resin is heated to a melting point of not lower than 60
A reaction product gas generated by heating and melting at 0 ° C. and causing a contact reaction with at least one of molecular fluorine, nitrogen trifluoride, halogenated fluoride and rare gas fluoride at an ambient temperature of 200 to 550 ° C. Is cooled in a cooler to 50 ° C. or less, and the precipitated low molecular weight fluorine-containing resin particles are collected in a collection vessel, and the atmosphere is kept at 50 ° C. or less between the reactor and the collection vessel. 2. The method according to claim 1, wherein the fluorine concentration in the gas is maintained at 0.1 vol% or more.
JP15953497A 1997-06-17 1997-06-17 Low molecular weight fluorine-containing resin powder and its production Pending JPH115813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15953497A JPH115813A (en) 1997-06-17 1997-06-17 Low molecular weight fluorine-containing resin powder and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15953497A JPH115813A (en) 1997-06-17 1997-06-17 Low molecular weight fluorine-containing resin powder and its production

Publications (1)

Publication Number Publication Date
JPH115813A true JPH115813A (en) 1999-01-12

Family

ID=15695879

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15953497A Pending JPH115813A (en) 1997-06-17 1997-06-17 Low molecular weight fluorine-containing resin powder and its production

Country Status (1)

Country Link
JP (1) JPH115813A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103665215A (en) * 2013-11-29 2014-03-26 中昊晨光化工研究院有限公司 PTFE suspension resin end group fluorination treatment method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103665215A (en) * 2013-11-29 2014-03-26 中昊晨光化工研究院有限公司 PTFE suspension resin end group fluorination treatment method

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