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JPH0567595B2 - - Google Patents
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JPH0567595B2 - - Google Patents

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Publication number
JPH0567595B2
JPH0567595B2 JP63167127A JP16712788A JPH0567595B2 JP H0567595 B2 JPH0567595 B2 JP H0567595B2 JP 63167127 A JP63167127 A JP 63167127A JP 16712788 A JP16712788 A JP 16712788A JP H0567595 B2 JPH0567595 B2 JP H0567595B2
Authority
JP
Japan
Prior art keywords
resin
impregnation
carbonaceous material
tank
temperature
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.)
Expired - Lifetime
Application number
JP63167127A
Other languages
Japanese (ja)
Other versions
JPH0218358A (en
Inventor
Nobuyuki Yamanashi
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.)
Tokai Carbon Co Ltd
Original Assignee
Tokai Carbon 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 Tokai Carbon Co Ltd filed Critical Tokai Carbon Co Ltd
Priority to JP63167127A priority Critical patent/JPH0218358A/en
Publication of JPH0218358A publication Critical patent/JPH0218358A/en
Publication of JPH0567595B2 publication Critical patent/JPH0567595B2/ja
Granted legal-status Critical Current

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  • Ceramic Products (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は、液体、気体、などに対して不浸透性
を備える不浸透性炭素材の製造方法に関する。 〔従来の技術〕 従来、耐食性が要求される熱交換器部材や各種
のシール材などに有用されている不浸透性炭素材
は、炭素質素材の気孔空隙に液状の熱硬化性樹脂
を減圧および/または加圧下に含浸充填したの
ち、大気中もしくは加圧雰囲気中で加熱硬化する
ことによつて製造されている。 ところが、上記の方法による場合には樹脂を炭
素質素材の深部まで含浸させることができず、そ
のうえ、加熱硬化の過程で一旦充填した樹脂が未
反応成分あるいは重縮合生成水などの揮散に伴つ
て素材の気孔空隙中から外部に流出する現象が生
じ、これが充填樹脂の重縮合に基づく体積収縮と
相俟つて気孔空隙の完全な閉塞化を著しく困難と
している。 このため、現状では予め炭素質素材を出来るだ
け最終形態に近い形状に加工したうえで、樹脂含
浸および加熱硬化の処理を複数回反復するといつ
た煩雑なプロセスが良策とされている。 〔発明が解決しようとする課題〕 このような事情から、現状の方法では、製品形
状が確定するまで製作に着手できない関係で製作
期間が長期化(2〜3ケ月)するという工期的な
問題、また複数回の樹脂含浸と加熱処理を施して
も、樹脂充填層が薄いため表面切削加工をすると
容易に不浸透性が損なわれるといつた技術面での
問題もあつた。 本発明は、これら従来技術の問題点を解消する
目的でなされたもので、1回の樹脂含浸および加
熱硬化により素材の深部まで樹脂を確実に充填で
き、よつて未加工素材のまま含浸処理することを
可能にした不浸透性炭素質素材の製造方法を提供
するものである。 〔課題を解決するための手段〕 すなわち、本発明に係る不浸透性炭素質素材の
製造方法は、炭素質素材を含浸槽に入れ、減圧下
で液状の熱硬化性樹脂に浸漬し、ついで系内を加
圧状態に切り換えて液状樹脂が初期硬化するまで
30℃以上の温度で加熱処理することを構成上の特
徴とする。 まず、未加工の炭素質素材をその素材が丁度入
る形態の含浸槽に入れ、所定の真空度に減圧した
のち液状の熱硬化性樹脂を素材が浸漬する状態に
流入する。 含浸に供される熱硬化性樹脂としては、通常、
炭素材の含浸に汎用されているフエノール系ある
いはフラン系の初期縮合樹脂液(粘度90ポアズ以
下)が用いられる。 ついで含浸槽内を1Kg/cm2以上の加圧状態に切
り換え、30℃以上の温度に外周加熱して樹脂粘度
を下げながら気孔空隙の深部まで十分に含浸処理
を施す。加熱処理は、含浸槽内の液状樹脂が初期
硬化するまで続ける。この際、加熱温度30℃を下
廻ると樹脂の初期硬化が円滑に進行しないため含
浸素材の取り出しが著しく困難となる。また、
100℃を越える加熱は、樹脂の初期硬化を早め、
深部までの含浸を阻害する要因となるので好まし
くない。したがつて、加熱温度は、30〜100℃の
範囲で設定することが望ましい。 このようにして含浸・初期硬化処理をおこなつ
た炭素質素材は、含浸槽ごと大気中180℃までの
温度に加熱して樹脂を完全に硬化する。 処理後の炭素質素材は含浸槽を冷却してから取
り出し、外周に付着した樹脂を除去する。この
際、炭素質素材は冷却過程の熱膨張率の差によつ
て剥離し、含浸槽の硬化樹脂から容易に取り出す
ことができる。 〔作用〕 上記のプロセスによれば、含浸工程が加熱加圧
下で行なわれるため粘度が低下し、樹脂は素材深
部の気孔空隙まで円滑に充填される。そして、加
熱加圧は初期硬化の段階まで含浸槽中で同様にお
こなわれているので、素材は常に外周部を樹脂に
よつて押圧された状態に保持される。この作用を
介して含浸樹脂が気孔空隙中から外部に流出する
現象は効果的に阻止されるとともに、含浸樹脂の
体積収縮に伴う充填不足は外周部に存在する樹脂
の新たな浸透によつて十分に補充される。 このような機構に基づいて、1回の含浸処理に
よる炭素質素材の完全な不浸透性の付与が可能と
なる。 〔実施例〕 外径640mm、厚さ600mmの円柱形状を有する未加
工の炭素質素材(見掛比重17g/cm2、気孔率24
%)を素材が丁度収容できる密封構造の含浸槽に
入れ、系内を5torrに減圧したのち45ポアズのフ
エノールホルムアルデヒド樹脂液を素材が浸漬す
るまで流入した。 ついで、系内を7Kg/cm2に加圧するとともに70
℃に外周加熱しながら24時間保持して、含浸、ゲ
ル化および初期硬化の処理をおこなつた。処理後
の含浸槽を大気中180℃の温度で10時間加熱して
樹脂を完全に硬化したのち、含浸素材を槽から取
り出した。 このようにして得られた不浸透性炭素材から、
外径560mm、厚さ170mmの板状体1枚、外径120mm、
内径75mm、長さ200mmの円筒10本、および外径90
mm、内径50mm、長さ200mmの円筒8本を切削加工
して形成し、これら材料に4Kg/cm2の窒素ガス圧
をかけて10分間漏洩テストをおこなつた。このテ
ストを同一炭素質素材10個について実施した結果
を、処理条件と漏洩テスト合格率(リークなしが
合格)と対比して下表に示した。 なお、比較のために従来の樹脂含浸および加熱
硬化操作を1〜3回おこなつた例を従来例として
併載した。
[Industrial Application Field] The present invention relates to a method for manufacturing an impermeable carbon material that is impermeable to liquids, gases, and the like. [Prior Art] Impermeable carbon materials, which have been used in heat exchanger components and various sealing materials that require corrosion resistance, are produced by applying liquid thermosetting resin to the pore spaces of carbonaceous materials under reduced pressure. /Or manufactured by impregnating and filling under pressure and then heating and curing in the air or a pressurized atmosphere. However, when using the above method, it is not possible to impregnate the resin deep into the carbonaceous material, and furthermore, during the heating and curing process, the resin once filled may evaporate as unreacted components or water produced by polycondensation. A phenomenon occurs in which the material flows out from the pore spaces of the material, and this, together with volumetric shrinkage due to polycondensation of the filled resin, makes it extremely difficult to completely close the pore spaces. For this reason, currently, a complicated process that involves processing a carbonaceous material in advance into a shape as close to its final form as possible, and then repeating resin impregnation and heat curing processes multiple times, is considered a good solution. [Problems to be solved by the invention] Under these circumstances, with the current method, the production period becomes long (2 to 3 months) because production cannot begin until the product shape is determined; Furthermore, even after multiple resin impregnations and heat treatments, there were technical problems in that the resin filling layer was thin and its impermeability was easily lost when surface cutting was performed. The present invention was made with the aim of solving these problems of the conventional technology, and it is possible to reliably fill the deep part of the material with resin by one-time resin impregnation and heat curing, and therefore, the impregnation treatment can be performed while the unprocessed material is intact. The present invention provides a method for manufacturing an impermeable carbonaceous material that makes it possible to do this. [Means for Solving the Problems] That is, the method for producing an impermeable carbonaceous material according to the present invention involves placing a carbonaceous material in an impregnation tank, immersing it in a liquid thermosetting resin under reduced pressure, and then soaking the carbonaceous material in a liquid thermosetting resin. Switch to pressurized state until the liquid resin initially hardens.
The structural feature is that it is heat treated at a temperature of 30°C or higher. First, an unprocessed carbonaceous material is placed in an impregnation tank that is shaped to accommodate the material, and after the pressure is reduced to a predetermined degree of vacuum, a liquid thermosetting resin is poured into the tank to immerse the material. The thermosetting resin used for impregnation is usually
A phenol-based or furan-based initial condensation resin liquid (viscosity of 90 poise or less), which is commonly used for impregnating carbon materials, is used. Next, the inside of the impregnation tank is pressurized to 1 kg/cm 2 or higher, and the outer periphery is heated to a temperature of 30° C. or higher to lower the resin viscosity while sufficiently impregnating the deep part of the pores. The heat treatment is continued until the liquid resin in the impregnation tank is initially cured. At this time, if the heating temperature is lower than 30°C, the initial curing of the resin will not proceed smoothly, making it extremely difficult to take out the impregnated material. Also,
Heating over 100℃ accelerates the initial hardening of the resin.
This is not preferable because it becomes a factor that inhibits deep impregnation. Therefore, it is desirable to set the heating temperature in the range of 30 to 100°C. The carbonaceous material that has been impregnated and initially hardened in this way is heated in the impregnating tank to a temperature of up to 180°C in the atmosphere to completely harden the resin. After the treatment, the carbonaceous material is taken out from the impregnation bath after being cooled, and the resin attached to the outer periphery is removed. At this time, the carbonaceous material is peeled off due to the difference in coefficient of thermal expansion during the cooling process, and can be easily taken out from the cured resin in the impregnation bath. [Function] According to the above process, the impregnation step is carried out under heat and pressure, so the viscosity is reduced and the resin is smoothly filled into the pores deep within the material. Since the heating and pressurization is carried out in the same way in the impregnation tank up to the stage of initial hardening, the outer peripheral portion of the material is always kept in a state where it is pressed by the resin. Through this action, the phenomenon of the impregnated resin flowing out from the pore space is effectively prevented, and the lack of filling caused by the volumetric contraction of the impregnated resin is sufficiently prevented by new penetration of the resin existing in the outer periphery. will be replenished. Based on such a mechanism, complete impermeability can be imparted to the carbonaceous material through a single impregnation treatment. [Example] Unprocessed carbonaceous material having a cylindrical shape with an outer diameter of 640 mm and a thickness of 600 mm (apparent specific gravity 17 g/cm 2 , porosity 24
%) was placed in an impregnating tank with a sealed structure that could accommodate the material, and after reducing the pressure in the system to 5 torr, a 45 poise phenol formaldehyde resin solution was flowed in until the material was immersed. Next, the inside of the system was pressurized to 7 kg/cm 2 and 70
The sample was maintained for 24 hours while being heated at a temperature of 0.degree. C. for impregnation, gelation, and initial hardening. After the treatment, the impregnating tank was heated in the air at a temperature of 180°C for 10 hours to completely cure the resin, and then the impregnated material was taken out from the tank. From the impervious carbon material obtained in this way,
1 plate with an outer diameter of 560 mm and a thickness of 170 mm, an outer diameter of 120 mm,
10 cylinders with an inner diameter of 75 mm and a length of 200 mm, and an outer diameter of 90
Eight cylinders with a diameter of 50 mm, an inner diameter of 50 mm, and a length of 200 mm were formed by cutting, and a leak test was conducted for 10 minutes by applying a nitrogen gas pressure of 4 kg/cm 2 to these materials. This test was conducted on 10 pieces of the same carbonaceous material, and the results are shown in the table below, comparing the processing conditions and leakage test pass rate (no leaks pass). For comparison, examples in which conventional resin impregnation and heat curing operations were performed 1 to 3 times are also listed as conventional examples.

〔発明の効果〕〔Effect of the invention〕

以上のとおり、本発明に従えば未加工の炭素質
素材の深部まで1回の樹脂含浸および初期硬化処
理により確実に樹脂を充填することができるか
ら、これを所定形状に加工して製品化することが
可能となる。したがつて、熱交換器材あるいは各
種シール材などの不浸透性炭素部材を短工期で効
率的に製作することができ、工業上極めて有利で
ある。
As described above, according to the present invention, it is possible to reliably fill the unprocessed carbonaceous material deep into the deep part with resin through one-time resin impregnation and initial curing treatment, and this can be processed into a predetermined shape and manufactured into a product. becomes possible. Therefore, impermeable carbon members such as heat exchange equipment or various sealing materials can be manufactured efficiently in a short construction period, which is extremely advantageous industrially.

Claims (1)

【特許請求の範囲】[Claims] 1 炭素質素材を含浸槽に入れ、減圧下で液状の
熱硬化性樹脂に浸漬し、ついで系内を加圧状態に
切り換えて液状樹脂が初期硬化するまで30℃以上
の温度で加熱処理することを特徴とする不浸透性
炭素材の製造方法。
1 Place the carbonaceous material in an impregnation tank, immerse it in liquid thermosetting resin under reduced pressure, then switch the system to a pressurized state and heat treat it at a temperature of 30°C or higher until the liquid resin initially hardens. A method for producing an impermeable carbon material characterized by:
JP63167127A 1988-07-05 1988-07-05 Production of uninfiltrative carbonaceous material Granted JPH0218358A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63167127A JPH0218358A (en) 1988-07-05 1988-07-05 Production of uninfiltrative carbonaceous material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63167127A JPH0218358A (en) 1988-07-05 1988-07-05 Production of uninfiltrative carbonaceous material

Publications (2)

Publication Number Publication Date
JPH0218358A JPH0218358A (en) 1990-01-22
JPH0567595B2 true JPH0567595B2 (en) 1993-09-27

Family

ID=15843935

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63167127A Granted JPH0218358A (en) 1988-07-05 1988-07-05 Production of uninfiltrative carbonaceous material

Country Status (1)

Country Link
JP (1) JPH0218358A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002110188A (en) * 2000-09-29 2002-04-12 Hitachi Chem Co Ltd Fuel cell separator and fuel cell using fuel cell separator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011016744A (en) * 2009-07-07 2011-01-27 Toyoaki Sakurai Drug solution penetration apparatus

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53120711A (en) * 1977-03-31 1978-10-21 Hitachi Ltd Resinnimpregnated impermeable carbon product manufacture

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002110188A (en) * 2000-09-29 2002-04-12 Hitachi Chem Co Ltd Fuel cell separator and fuel cell using fuel cell separator

Also Published As

Publication number Publication date
JPH0218358A (en) 1990-01-22

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