JPS635348B2 - - Google Patents
Info
- Publication number
- JPS635348B2 JPS635348B2 JP58039199A JP3919983A JPS635348B2 JP S635348 B2 JPS635348 B2 JP S635348B2 JP 58039199 A JP58039199 A JP 58039199A JP 3919983 A JP3919983 A JP 3919983A JP S635348 B2 JPS635348 B2 JP S635348B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- vinyl chloride
- chloride resin
- manufacturing
- carbon
- 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
Links
- 239000011347 resin Substances 0.000 claims description 42
- 229920005989 resin Polymers 0.000 claims description 42
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 34
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical class ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 31
- 239000000203 mixture Substances 0.000 claims description 26
- 239000007849 furan resin Substances 0.000 claims description 23
- 238000004519 manufacturing process Methods 0.000 claims description 18
- 239000007833 carbon precursor Substances 0.000 claims description 17
- 229910052799 carbon Inorganic materials 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 15
- 238000010304 firing Methods 0.000 claims description 11
- 238000006116 polymerization reaction Methods 0.000 claims description 10
- 238000004898 kneading Methods 0.000 claims description 8
- 239000012298 atmosphere Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 238000000465 moulding Methods 0.000 claims description 3
- XPFVYQJUAUNWIW-UHFFFAOYSA-N furfuryl alcohol Chemical compound OCC1=CC=CO1 XPFVYQJUAUNWIW-UHFFFAOYSA-N 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 description 15
- 229910002804 graphite Inorganic materials 0.000 description 9
- 239000010439 graphite Substances 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 238000001723 curing Methods 0.000 description 6
- 238000003763 carbonization Methods 0.000 description 5
- 239000012299 nitrogen atmosphere Substances 0.000 description 5
- 230000035699 permeability Effects 0.000 description 5
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 3
- 239000003575 carbonaceous material Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910021397 glassy carbon Inorganic materials 0.000 description 3
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 3
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 229920006026 co-polymeric resin Polymers 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 229910021382 natural graphite Inorganic materials 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 229910021383 artificial graphite Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
Landscapes
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Description
本発明は不浸透炭素薄板の製造法に関する。詳
しくは本発明は通気率が小さく、高強度、高弾
性、高硬度を有し数十μ及至数mmの厚さの均一な
不浸透炭素薄板を容易に製造する方法に関する。
この様な炭素板はパツキン、ガスケツトへの応
用、あるいは電極、化学プラント等の遮蔽板等の
軽量化を可能にするもので、従来から種々の方法
で製造が試みられて来たが未だ上記の条件を満足
するごとき炭素薄板は得られていない。例えば、
不浸透黒鉛は、通常炭素材にフエノール樹脂また
はフラン樹脂等を含浸後硬化させたもの、さらに
含浸硬化後再焼成したもの、あるいは含浸、硬
化、焼成を繰返したものであるが、通気率が小さ
く(K=10-8cm2/s)、強度が基材の2倍以上あ
り、耐食性にも優れているけれども、製造工程が
複雑であるばかりでなく、製法上肉厚の製品に限
られ、軽量化は不可能に近い欠点を有する。すな
わち、通常炭素材はブロツク状に製造されており
これを薄板にするには切削に依らねばならない
が、1mm以下の厚さに切削するのは極めて困難
で、薄くとも数mmが限度である。仮に切削できて
も、割れやひびを生じさせないように樹脂含浸以
降の加工は至難であり、不浸透化後に薄板に切削
するにしても炭素材の硬度が飛躍的に増大してい
るので高価なカツターを使用せねばならず、しか
も高度の切削技術を必要とするので、仮にこのよ
うにして薄板が製造できたとしても、そのコスト
は極めて大きなものになる。炭素製品の薄板化に
成功した例としてはシート状可撓性黒鉛がある。
このシート状黒鉛は天然黒鉛を酸処理し、加熱し
て膨張黒鉛とした後圧延成形したもので数十μま
で薄くすることができるので軽量化が可能であ
り、しかも通気率も2×10-4cm2/sと小さい。し
かしながら、曲げ強度はぜろに等しく曲げ応力が
全く作用しない個所にしか利用できない欠点を有
する。また製造工程で強酸を大量に使用するため
装置の耐食性、排水処理などに充分注意を払わね
ばならず、コスト高にならざるを得ない。一方、
ガラスと同程度に不通気性であり(K=10-10〜
10-12cm2/s)、機械的強度が極めて大きく、等方
性で、表面積が極めて小さいガラス状炭素であ
る。このガラス状炭素は、フラン樹脂、フエノー
ル樹脂等の熱硬化性の合成樹脂を原料とし、これ
に適当な硬化剤を加えて、室温またはこれより僅
かに高い温度で1〜6週間の長時間をかけて硬化
し、熱分解によつて発生する揮発成分の突出によ
る亀烈防止のためにゆるやかな昇温速度で炭素化
させることによつて得られる。このように従来の
ガラス状炭素の製造は炭素化まで長期間を要する
のみならずその生成過程から見て薄板を得ること
は極めて困難であり、また硬度が極めて高くブロ
ツクからの薄板の切削は不浸透黒鉛の場合よりも
困難である。
本発明者等は、さきに、塩素化塩化ビニル樹脂
及び/または塩化ビニル樹脂をフラン樹脂と混合
し混練し、得られた混練物をフイルムまたはシー
ト状に成形し、成形物に炭素前駆体化処理を施し
た後、不活性雰囲気中で焼成することに想到し、
ガラス状炭素薄板の製造法を発明し、特許出願し
た。(特願昭57−128967)。
しかし乍ら、この方法は、混練物を成形するこ
とによつて製造したフイルム又はシートの引張強
度、引裂強度が充分でなく、取扱いに注意を要す
ること、炭素前駆体化処理及び焼成処理を施す過
程に於ても耐衝撃性に欠けクラツクが入り易く破
損し易い等の欠点を有していた。
従つて、本発明の目的は、このような欠点がな
く、通気率が小さく、高強度、高弾性、高硬度を
有し、数十μ乃至数mmの厚さの均一な不浸透炭素
薄板を極めて容易にかつ安価に製造する方法を提
供することである。
本願発明者等は、この目的を達成するた鋭意研
究の結果、黒鉛粉末の添加が成形安定性の向上、
焼成後の炭素薄板の寸法安定性や機械的強度の大
巾な上昇にも寄与することを発見し、塩素化塩化
ビニル樹脂及び/または塩化ビニル樹脂とフラン
樹脂及び黒鉛粉末を混合し、混練し、得られた混
練物をフイルム又はシート状に成形し、得られた
成形物に炭素前駆体化処理を施した後、不活性雰
囲気中で焼成することから成る不浸透炭素薄板の
製造法を達成し、前記の欠点を無くすることに成
功した。
本発明に使用される塩素化塩化ビニル樹脂は、
塩化ビニル樹脂を後塩素化することによつて得ら
れる(−CH2−CHCl)−と(−CHCl−CHCl)−との混
合組成のポリマーである。(CH2−CHCl)−と(−
CHCl―CHCl)−との比率は特に制限はないが、
モル比で56:44〜19:81、すなわち塩素含有率と
して64〜70重量%の範囲の塩素化塩化ビニル樹脂
がフラン樹脂との相溶性が良好である。重合度も
また特に制限はないが500〜2000の重合度が好ま
しい。500以下の場合は、フラン樹脂との混練物
をフイルムまたはシートに成形加工したとき引裂
抵抗が小さく、裂け易くなる欠点が生ずる。2000
以上になるとフラン樹脂との混練物に粘りが出す
ぎて平滑なフイルムまたはシートに加工すること
が困難になる。
塩化ビニル樹脂は重合法の相違によつてコンパ
ウンドとペーストに大別されるが、フラン樹脂と
の混練性からコンパウンドの方が好ましい。ま
た、ストレートポリマーと、アクリル酸エステ
ル、エチレンビニルアセテート等と共重合させた
樹脂とがあるが、共重合樹脂は共重合している樹
脂の収炭率が一般に小さいので、炭素化させて得
た薄板の通気率が大きくなり、強度も低下するの
で好ましくない。重合度は塩素化塩化ビニル樹脂
の場合と同様に特に制限はないが、500〜2000が
好ましく、500以下では成形フイルムのグリーン
強度が小さくて扱いにくく、2000以上では均一な
厚さに成形することが困難になる。
塩素化塩化ビニル樹脂及び塩化ビニル樹脂はそ
れぞれ単独で、あるいは目的に応じて両者をブレ
ンドしてからフラン樹脂と混練される。さらに、
重合度の異なる樹脂2種以上をフレンドして用い
てもよい。
該樹脂と混練されるフラン樹脂には、フルフリ
ルアルコール樹脂、フルフリルアルコール―フル
フラール共重合樹脂、フルフリルアルコール―フ
エノール共縮合樹脂、フルフリルアルコール―ケ
トン共縮合樹脂等があるが、そのいづれでもよく
勿論それらを混合して用いることもできる。
又、本発明に用いる黒鉛粉末は、天然黒鉛、人
造黒鉛のいづれを用いても良いが、配合組成物の
混練物をフイルム又はシート状に成形した際の機
械的強度を上げる為、炭素前駆体化処理、その後
の焼成処理を施す際の耐衝撃性の向上の為には、
結晶が発達した鱗状黒鉛の方が、非晶質の土状黒
鉛よりも好ましい。利用される粉体の粒径は平均
粒度0.5〜150μm程度迄がその目的とする面状体
の厚さによつて使い分けられるが0.5μmより微細
であると、強化作用に乏しく、脱気が困難とな
り、150μm以上であると複合体としてまとまり
難く、成形体表面が粗荒になり物性を低下させる
ので好ましくない。黒鉛粉末の添加量は、配合組
成物の2〜50重量%が良く、2重量%より少ない
添加量では強化作用が殆ど無く、50重量%以上で
は、結合剤の比率が小さくなり過ぎる為に、機械
的強度が低下し、脱気も困難となるので不浸透性
も低下するので好ましくない。
本発明の方法においては、まづ塩素化塩化ビニ
ル樹脂または塩化ビニル樹脂または両者の混合物
10〜88重量部とフラン樹脂5〜78重量部及び黒鉛
粉末2〜50重量部をヘンシエルミキサー等の混合
機で均一に混合する。次に、この混合された配合
組成物を加圧ニーダー2本ロール、3本ロール、
コニーダ等の高度の剪断力の混練機を用いて加熱
下に混練する。配合組成物は混練されると加熱下
で、もち状の粘弾性体になるが、塩素化塩化ビニ
ル樹脂、塩化ビニル樹脂は200℃を超えると急速
に劣化し塩化水素ガスを放出し、この塩化水素ガ
スがフラン樹脂の硬化剤となるので、混練中長時
間200℃以上にはしない方がよい。また、塩素化
塩化ビニル樹脂、塩化ビニル樹脂は熱劣化を防止
するための通常の安定剤を予め適宜加えておいて
もよい。さらに、これらのビニル樹脂とフラン樹
脂及び黒鉛粉末との混練を効果的に迅速に行わし
める目的でテトラヒドロフラン、シクロヘキサノ
ン、N―メチルピロリドン等の溶剤、DOP、
DBP、TCP等の可塑剤を配合組成物に加えてお
いてもよい。
次に、混練した配合組成物はカレンダロール、
押出成形機等を用いてフイルム状またはシート状
に成形する。成形加工性を向上させるために、配
合組成物に通常の滑剤を予め加えておいてもよ
い。
フイルム状またはシート状に成形された配合組
成物は、加熱空気雰囲気中で50〜300℃に加熱し
て炭素前駆体化処理を施す。この時、塩素化塩化
ビニル樹脂、塩化ビニル樹脂は塩化水素ガスを放
出してフラン樹脂の硬化を促進させる。フラン樹
脂は加熱と塩化水素ガスによつて3次元的に硬化
する。従つて特別の硬化剤の添加を必要としな
い。またこの炭素前駆体化処理において、必要に
応じて、塩素またはオゾンを雰囲気中に加えても
よい。さらに、塩素化塩化ビニル樹脂、塩化ビニ
ル樹脂とフラン樹脂及び黒鉛粉末との混練性を上
げるために添加した溶剤や可塑剤は、炭素前駆体
化処理中に揮散する。炭素前駆体化処理の時間は
配合組成物の組成及び成形物の厚さに依るが、6
〜72時間である。
炭素前駆体化処理を終了したフイルムまたはシ
ート状の賦形物は窒素、アルゴン等の不活性気中
で800℃以上、好ましくは1000℃以上まで加熱し
炭素化する。塩素化塩化ビニル樹脂、塩化ビニル
樹脂とフラン樹脂の炭化は、従来の焼成時間を大
巾に短縮することが可能で、炭素化するまで長く
とも100時間を超える様な緩慢な昇温速度を設定
する必要はない。
次に実施例により本発明をより具体的に説明す
る。
実施例 1
塩素含有率67%重合度740の塩素化塩化ビニル
樹脂((株)日本カーバイド製ニカテンプT―870)
40重量部、フラン樹脂((株)日立化成製ヒタフラン
VF302)30重量部及び平均粒度7μmの黒鉛粉末
((株)日本黒鉛製CSP)をヘンシエルミキサーを用
いて均一に混合した。
次いで配合組成物を加熱した2本ロールを用い
て十分に混練した。混練後、カレンダーロールを
用いて成形し、2mmの厚さのシートを得た。得ら
れたシートを加熱オーブンに入れ150℃で6時間、
次いで180℃10時間の炭素前駆体化処理を行つた
後に、窒素雰囲気中で300℃迄は20℃/h、500℃
迄は40℃/h、1000℃迄は100℃/hの昇温速度
で加熱し、冷却後炭素薄板を得た。
実施例 2
実施例1の2本ロール混練物を、ペレタイザー
にてペレツト化し、Tダイ法を用いて、厚さ0.1
mmのフイルムに押出成形した。次いで該フイルム
を加熱オーブンに入れ150℃3時間、180℃6時間
の炭素前駆体化処理を施した後に、窒素雰囲気中
で、実施例1と同条件にて焼成して炭素化し、冷
却後炭素薄板を得た。
実施例 3
重合度700のストレート塩化ビニル樹脂((株)三
井東圧製ビニクロン4000LL)30重量部、フラン
樹脂((株)日立化成製ヒタフランVF302)30重量
部、平均粒度7μmの黒鉛粉末((株)日本黒鉛製
CSP)40重量部をヘンシエルミキサーを用いて均
一に混合する。次いで配合組成物を加圧ニーダー
中に投入し、加熱加圧下で十分に混練し、カレン
ダーロールを用いて成形し、厚さ5mmのシートを
得た。該シートを加熱オーブンに入れ、120℃6
時間次いで5℃/hの昇温速度で300℃迄加熱し、
炭素前駆体化処理を施した。次に窒素雰囲気中で
500℃迄は20℃/h、1500℃迄は100℃/hの昇温
速度にて焼成、炭素化し冷却後炭素薄板を得た。
比較例 1
塩素含有率67%重合度740の塩素化塩化ビニル
樹脂((株)日本カーバイド製ニカテンプT―870)
60重量部、フラン樹脂((株)日立化成製ヒタフラン
VF302)40重量部をヘンシエルミキサーを用いて
均一に混合した。次いで配合組成物を加熱した2
本ロールを用いて十分に混練した。混練後、カレ
ンダーロールを用いて、成形し2mmの厚さのシー
トを得た。得られたシートを加熱オーブンに入れ
150℃6時間、次いで180℃10時間の炭素前駆体化
処理を行つた後に、窒素雰囲気中で300℃迄は20
℃/h、500℃迄は40℃/h、1000℃迄は100℃/
hの昇温速度で加熱し、1000℃で3時間保持し炭
素化し、冷却後炭素薄板を得た。
比較例 2
比較例1の2本ロール混練物を、ペレタイザー
にてペレツト化し、Tダイ法を用いて、厚さ0.1
mmのフイルムに押出成形した。次いで該フイルム
を、加熱オーブンに入れ、150℃3時間180℃6時
間の炭素前駆体化処理を施した後に、窒素雰囲気
中で、比較例1と同条件にて焼成して炭素化し、
冷却後炭素薄板を得た。
比較例 3
重合度700のストレート塩化ビニル樹脂〔(株)三
井東圧製ビニクロン4000LL〕50重量部、フラン
樹脂50重量部〔(株)日立化成製ヒタフランVF―
302〕をヘンシエルミキサーを用いて均一に混合
する。次いで配合組成物を加圧ニーダー中に投入
し、加熱加圧下で十分に混練し、カレンダーロー
ルを用いて成形し、厚さ5mmのシートを得た。該
シートを加熱オーブンに入れ、120℃6時間次い
で5℃/hの昇温速度で300℃迄加熱し、炭素前
駆体化処理を施した。次に窒素雰囲気中で、500
℃迄は20℃/h、1500℃迄は100℃/hの昇温速
度にて焼成、炭素化し、冷却後炭素薄板を得た。
以上の実施例及び比較例における試験結果及び
備考を第1表に取りまとめて示す。
The present invention relates to a method for manufacturing impermeable carbon sheets. Specifically, the present invention relates to a method for easily producing a uniform impermeable carbon thin plate having a low air permeability, high strength, high elasticity, and high hardness, and having a thickness of several tens of microns to several mm. Such carbon plates can be applied to packings and gaskets, and can be used to reduce the weight of electrodes and shielding plates for chemical plants, etc., and although attempts have been made to manufacture them using various methods, the methods described above have not yet been achieved. A carbon thin plate that satisfies the conditions has not been obtained. for example,
Impermeable graphite is usually made by impregnating a carbon material with phenolic resin or furan resin, etc. and then hardening it, or by impregnating and curing it and then re-baking it, or by repeating impregnation, curing, and firing, but it has a low air permeability. (K = 10 -8 cm 2 /s), has more than twice the strength of the base material, and has excellent corrosion resistance, but not only is the manufacturing process complicated, but it is limited to thick products due to the manufacturing method. It has the drawback that weight reduction is almost impossible. That is, carbon materials are usually manufactured in the form of blocks, and cutting them into thin plates is necessary, but it is extremely difficult to cut them to a thickness of 1 mm or less, and the thinner limit is several mm. Even if it were possible to cut the material, it would be extremely difficult to process it after impregnating it with resin to prevent cracks, and even if it were to be cut into thin sheets after being made impermeable, the hardness of the carbon material has increased dramatically, making it expensive. Since a cutter must be used and advanced cutting techniques are required, even if thin plates could be manufactured in this way, the cost would be extremely high. An example of successful thinning of carbon products is sheet-shaped flexible graphite.
This sheet-like graphite is made by acid-treating natural graphite, heating it to form expanded graphite, and then rolling it. It can be made as thin as several tens of microns, making it lightweight, and has an air permeability of 2 x 10 - It is as small as 4 cm 2 /s. However, the bending strength is equal to zero and has the disadvantage that it can only be used at locations where no bending stress acts. Furthermore, since a large amount of strong acid is used in the manufacturing process, sufficient attention must be paid to the corrosion resistance of the equipment, wastewater treatment, etc., which inevitably leads to higher costs. on the other hand,
It is as impermeable as glass (K=10 -10 ~
10 −12 cm 2 /s), is isotropic, has extremely high mechanical strength, and has an extremely small surface area. This glassy carbon is made from thermosetting synthetic resins such as furan resins and phenolic resins, and by adding an appropriate curing agent to this, it is cured for a long period of 1 to 6 weeks at room temperature or a slightly higher temperature. It is obtained by carbonizing at a slow heating rate to prevent cracking due to the protrusion of volatile components generated by thermal decomposition. As described above, the conventional production of glassy carbon not only takes a long time to carbonize, but also makes it extremely difficult to obtain thin plates from the production process, and the hardness is extremely high, making it impossible to cut thin plates from blocks. This is more difficult than with permeated graphite. The present inventors first mixed and kneaded chlorinated vinyl chloride resin and/or vinyl chloride resin with furan resin, molded the obtained kneaded product into a film or sheet shape, and added carbon precursor to the molded product. After the treatment, we came up with the idea of firing in an inert atmosphere.
Invented a method for manufacturing glassy carbon thin plates and applied for a patent. (Special application No. 57-128967). However, with this method, the tensile strength and tear strength of the film or sheet produced by molding the kneaded material are insufficient, care must be taken in handling, and carbon precursor treatment and sintering treatment are required. Even in the process, it had drawbacks such as lack of impact resistance and easy cracking and breakage. Therefore, the object of the present invention is to provide a uniform impermeable carbon thin plate having a thickness of several tens of microns to several millimeters, which does not have such drawbacks, has low permeability, high strength, high elasticity, and high hardness. It is an object of the present invention to provide a manufacturing method that is extremely easy and inexpensive. As a result of intensive research to achieve this objective, the inventors of the present application have found that the addition of graphite powder improves molding stability.
We discovered that this contributes to a significant increase in the dimensional stability and mechanical strength of carbon thin sheets after firing, and we have developed a method of mixing and kneading chlorinated vinyl chloride resin and/or vinyl chloride resin with furan resin and graphite powder. Achieved a method for producing an impermeable carbon thin plate, which consists of forming the obtained kneaded material into a film or sheet shape, subjecting the obtained molded product to a carbon precursor treatment, and then firing it in an inert atmosphere. However, we succeeded in eliminating the above-mentioned drawbacks. The chlorinated vinyl chloride resin used in the present invention is
It is a polymer having a mixed composition of ( -CH2 -CHCl)- and (-CHCl-CHCl)- obtained by post-chlorinating vinyl chloride resin. (CH 2 −CHCl)− and (−
There is no particular restriction on the ratio of CHCl−CHCl)−, but
A chlorinated vinyl chloride resin having a molar ratio of 56:44 to 19:81, that is, a chlorine content of 64 to 70% by weight, has good compatibility with the furan resin. The degree of polymerization is also not particularly limited, but a degree of polymerization of 500 to 2000 is preferred. If it is less than 500, when the kneaded product with the furan resin is molded into a film or sheet, there will be a drawback that the tear resistance will be low and it will easily tear. 2000
If it exceeds the above range, the mixture with the furan resin will become too sticky, making it difficult to process it into a smooth film or sheet. Vinyl chloride resins are broadly classified into compounds and pastes depending on the polymerization method, but compounds are preferable from the standpoint of kneadability with furan resins. There are also straight polymers and resins copolymerized with acrylic esters, ethylene vinyl acetate, etc. However, since the carbon yield of copolymerized resins is generally low, copolymer resins are obtained by carbonization. This is not preferable because the air permeability of the thin plate increases and the strength also decreases. The degree of polymerization is not particularly limited as in the case of chlorinated vinyl chloride resin, but it is preferably between 500 and 2000. If it is less than 500, the green strength of the molded film will be small and difficult to handle, and if it is more than 2000, it will be difficult to mold it to a uniform thickness. becomes difficult. The chlorinated vinyl chloride resin and the vinyl chloride resin are kneaded with the furan resin either alone or as a blend of the two depending on the purpose. moreover,
Two or more resins having different degrees of polymerization may be used as friends. Furan resins to be kneaded with the resin include furfuryl alcohol resin, furfuryl alcohol-furfural copolymer resin, furfuryl alcohol-phenol cocondensation resin, furfuryl alcohol-ketone cocondensation resin, etc. Of course, a mixture of them can also be used. Further, the graphite powder used in the present invention may be either natural graphite or artificial graphite, but in order to increase the mechanical strength when the kneaded mixture of the blended composition is molded into a film or sheet shape, a carbon precursor may be used. In order to improve impact resistance during chemical treatment and subsequent firing treatment,
Scale-like graphite with developed crystals is preferable to amorphous earth-like graphite. The particle size of the powder to be used ranges from 0.5 to 150 μm in average particle size, depending on the thickness of the intended planar object, but if it is finer than 0.5 μm, it will have poor reinforcing effect and will be difficult to degas. If it is 150 μm or more, it is difficult to assemble as a composite, the surface of the molded product becomes rough, and the physical properties are deteriorated, which is not preferable. The amount of graphite powder added is preferably 2 to 50% by weight of the blended composition. If the amount is less than 2% by weight, there is almost no reinforcing effect, and if it is more than 50% by weight, the ratio of the binder becomes too small. This is not preferable because mechanical strength decreases, degassing becomes difficult, and impermeability also decreases. In the method of the present invention, first, a chlorinated vinyl chloride resin, a vinyl chloride resin, or a mixture of both is used.
10 to 88 parts by weight, 5 to 78 parts by weight of furan resin, and 2 to 50 parts by weight of graphite powder are uniformly mixed using a mixer such as a Henschel mixer. Next, this mixed compounded composition is applied to a pressure kneader with two rolls, three rolls,
The mixture is kneaded under heat using a kneader with high shear force such as Konida. When the blended composition is kneaded and heated, it becomes a sticky viscoelastic body, but chlorinated vinyl chloride resin and vinyl chloride resin deteriorate rapidly when the temperature exceeds 200°C, releasing hydrogen chloride gas, and this chloride Since hydrogen gas acts as a curing agent for the furan resin, it is best not to heat it to over 200°C for a long period of time during kneading. In addition, a conventional stabilizer may be appropriately added to the chlorinated vinyl chloride resin or vinyl chloride resin in order to prevent thermal deterioration. Furthermore, in order to effectively and quickly knead these vinyl resins with furan resin and graphite powder, solvents such as tetrahydrofuran, cyclohexanone, N-methylpyrrolidone, DOP,
Plasticizers such as DBP, TCP, etc. may be added to the blended composition. Next, the kneaded compounded composition is placed in a calender roll,
It is molded into a film or sheet using an extruder or the like. In order to improve moldability, a conventional lubricant may be added to the compounded composition in advance. The blended composition formed into a film or sheet is heated to 50 to 300°C in a heated air atmosphere to undergo a carbon precursor treatment. At this time, the chlorinated vinyl chloride resin and the vinyl chloride resin release hydrogen chloride gas to accelerate the curing of the furan resin. Furan resin is cured three-dimensionally by heating and hydrogen chloride gas. Therefore, no special curing agent needs to be added. In addition, in this carbon precursor treatment, chlorine or ozone may be added to the atmosphere as necessary. Furthermore, the solvent and plasticizer added to improve the kneading properties of the chlorinated vinyl chloride resin, the vinyl chloride resin, the furan resin, and the graphite powder are volatilized during the carbon precursor treatment. The time for the carbon precursor treatment depends on the composition of the compounded composition and the thickness of the molded product, but
~72 hours. The film or sheet shaped excipient that has been subjected to the carbon precursor treatment is heated to 800° C. or higher, preferably 1000° C. or higher, in an inert atmosphere such as nitrogen or argon to carbonize it. For carbonization of chlorinated vinyl chloride resin, vinyl chloride resin, and furan resin, it is possible to significantly shorten the conventional firing time, and a slow heating rate is set so that carbonization takes more than 100 hours at most. do not have to. Next, the present invention will be explained in more detail with reference to Examples. Example 1 Chlorinated vinyl chloride resin with chlorine content of 67% and degree of polymerization of 740 (Nicatemp T-870 manufactured by Nippon Carbide Co., Ltd.)
40 parts by weight, furan resin (Hitafuran manufactured by Hitachi Chemical Co., Ltd.)
30 parts by weight of VF302) and graphite powder (CSP manufactured by Nippon Graphite Co., Ltd.) having an average particle size of 7 μm were uniformly mixed using a Henschel mixer. Next, the blended composition was sufficiently kneaded using two heated rolls. After kneading, the mixture was molded using a calendar roll to obtain a sheet with a thickness of 2 mm. Place the obtained sheet in a heating oven at 150℃ for 6 hours.
Next, after performing a carbon precursor treatment at 180°C for 10 hours, the temperature was increased to 20°C/h until 300°C at 500°C.
It was heated at a heating rate of 40°C/h up to 1000°C and 100°C/h up to 1000°C, and after cooling, a carbon thin plate was obtained. Example 2 The two-roll kneaded product of Example 1 was pelletized using a pelletizer, and the pellets were made into pellets with a thickness of 0.1 using the T-die method.
It was extruded into a mm film. Next, the film was placed in a heating oven and subjected to carbon precursor treatment at 150°C for 3 hours and 180°C for 6 hours, then fired in a nitrogen atmosphere under the same conditions as in Example 1 to carbonize, and after cooling, the film was carbonized. A thin plate was obtained. Example 3 30 parts by weight of straight vinyl chloride resin with a degree of polymerization of 700 (Vinicron 4000LL manufactured by Mitsui Toatsu Co., Ltd.), 30 parts by weight of furan resin (Hitafuran VF302 manufactured by Hitachi Chemical Co., Ltd.), graphite powder with an average particle size of 7 μm (( Nippon Graphite Co., Ltd.
Mix 40 parts by weight of CSP) uniformly using a Henschel mixer. Next, the blended composition was put into a pressure kneader, thoroughly kneaded under heat and pressure, and molded using a calendar roll to obtain a sheet with a thickness of 5 mm. Place the sheet in a heating oven at 120℃6
heating to 300°C at a temperature increase rate of 5°C/h,
Carbon precursor treatment was performed. Then in a nitrogen atmosphere
Firing and carbonization were performed at a heating rate of 20°C/h up to 500°C and 100°C/h up to 1500°C, and a carbon thin plate was obtained after cooling. Comparative Example 1 Chlorinated vinyl chloride resin with chlorine content of 67% and degree of polymerization of 740 (Nicatemp T-870 manufactured by Nippon Carbide Co., Ltd.)
60 parts by weight, furan resin (Hitafuran manufactured by Hitachi Chemical Co., Ltd.)
VF302) 40 parts by weight were uniformly mixed using a Henschel mixer. The blended composition was then heated 2
Thorough kneading was carried out using this roll. After kneading, the mixture was molded using a calendar roll to obtain a sheet with a thickness of 2 mm. Place the resulting sheet in a heated oven
After performing carbon precursor treatment at 150°C for 6 hours and then at 180°C for 10 hours, it was heated to 300°C for 20 hours in a nitrogen atmosphere.
℃/h, 40℃/h up to 500℃, 100℃/h up to 1000℃
The mixture was heated at a temperature increase rate of 1000° C. for 3 hours to carbonize, and after cooling, a thin carbon plate was obtained. Comparative Example 2 The two-roll kneaded product of Comparative Example 1 was pelletized using a pelletizer, and the pellets were made into pellets with a thickness of 0.1 using the T-die method.
It was extruded into a mm film. Next, the film was placed in a heating oven and subjected to carbon precursor treatment at 150°C for 3 hours and 180°C for 6 hours, and then carbonized by firing in a nitrogen atmosphere under the same conditions as Comparative Example 1.
After cooling, a carbon thin plate was obtained. Comparative Example 3 50 parts by weight of straight vinyl chloride resin with a degree of polymerization of 700 [Vinicron 4000LL manufactured by Mitsui Toatsu Co., Ltd.], 50 parts by weight of furan resin [Hitafuran VF manufactured by Hitachi Chemical Co., Ltd.]
302] using a Henschel mixer. Next, the blended composition was put into a pressure kneader, thoroughly kneaded under heat and pressure, and molded using a calendar roll to obtain a sheet with a thickness of 5 mm. The sheet was placed in a heating oven and heated at 120° C. for 6 hours, then at a temperature increase rate of 5° C./h to 300° C. to perform a carbon precursor treatment. Then in a nitrogen atmosphere, 500
Firing and carbonization were carried out at a heating rate of 20°C/h up to 1500°C and 100°C/h up to 1500°C, and after cooling, a carbon thin plate was obtained. The test results and notes for the above Examples and Comparative Examples are summarized in Table 1.
【表】【table】
Claims (1)
ル樹脂とフラン樹脂及び黒鉛粉末を混合し、混練
し、得られた混練物をフイルム又はシート状に成
形し、得られた成形物に炭素前駆体化処理を施し
た後、不活性雰囲気中で焼成することから成る不
浸透炭素薄板の製造法。 2 該塩素化塩化ビニル樹脂及び塩化ビニル樹脂
の重合度はいづれも500〜2000である第1項の製
造法。 3 該フラン樹脂はフルフリルアルコール樹脂、
フルフリールアルコール―フルフラール共縮合樹
脂、フルフリールアルコール―フエノール共縮合
樹脂またはその混合樹脂である第1項の製造法。 4 該黒鉛粉末の粒径は平均粒度0.5〜150μmで
ある第1項の製造法。 5 該黒鉛粉末の添加量は配合組成物の2〜50重
量%である第1項の製造法。 6 該混練は200℃以下の加熱下で行われる第1
項の製造法。 7 該炭素前駆体化処理は空気雰囲気中で50〜
300℃に加熱することによつて行われる第1項の
製造法。 8 該焼成は800℃以上で行われる第1項の製造
法。[Claims] 1. A molded product obtained by mixing and kneading chlorinated vinyl chloride resin and/or vinyl chloride resin, furan resin, and graphite powder, and molding the resulting kneaded product into a film or sheet shape. A method for producing an impermeable carbon thin plate, which comprises subjecting the material to a carbon precursor treatment and then firing it in an inert atmosphere. 2. The manufacturing method according to item 1, wherein the chlorinated vinyl chloride resin and the vinyl chloride resin each have a degree of polymerization of 500 to 2000. 3 The furan resin is furfuryl alcohol resin,
1. The method for producing furfuryl alcohol-furfural co-condensed resin, furfuryl alcohol-phenol co-condensed resin, or a mixed resin thereof. 4. The production method according to item 1, wherein the graphite powder has an average particle size of 0.5 to 150 μm. 5. The manufacturing method according to item 1, wherein the amount of graphite powder added is 2 to 50% by weight of the blended composition. 6 The first kneading is carried out under heating at 200°C or less.
Manufacturing method of section. 7 The carbon precursor treatment is carried out in an air atmosphere for 50~
The manufacturing method of paragraph 1, which is carried out by heating to 300°C. 8. The manufacturing method of paragraph 1, in which the firing is performed at 800°C or higher.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58039199A JPS59164674A (en) | 1983-03-11 | 1983-03-11 | Manufacture of non-permeable carbon thin plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58039199A JPS59164674A (en) | 1983-03-11 | 1983-03-11 | Manufacture of non-permeable carbon thin plate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59164674A JPS59164674A (en) | 1984-09-17 |
| JPS635348B2 true JPS635348B2 (en) | 1988-02-03 |
Family
ID=12546449
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58039199A Granted JPS59164674A (en) | 1983-03-11 | 1983-03-11 | Manufacture of non-permeable carbon thin plate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59164674A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5110516A (en) * | 1989-05-04 | 1992-05-05 | Mitsubishi Pencil Co., Ltd. | Process of making a lead wire of hard carbon |
| US5096633A (en) * | 1989-05-19 | 1992-03-17 | Mitsubishi Pencil Co., Ltd. | Process of making a diaphragm of carbonaceous material |
-
1983
- 1983-03-11 JP JP58039199A patent/JPS59164674A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59164674A (en) | 1984-09-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP2590328B2 (en) | Melt blend composition | |
| GB2117746A (en) | Fuel cell electrode substrates | |
| US5080743A (en) | Process for preparation of a wholly carbonaceous diaphragm for acoustic equipment use | |
| EP0364297A2 (en) | Porous carbon electrode substrates for fuel cells | |
| JP2725705B2 (en) | Cell separator for fuel cells | |
| EP3725824B1 (en) | Heat conduction sheet | |
| JP3205184B2 (en) | Fired pencil lead and method for producing the same | |
| US4855093A (en) | Process of making a diaphragm of carbonaceous materials for a speaker | |
| JPS635348B2 (en) | ||
| JP2939759B2 (en) | Carbon thin plate and method for producing the same | |
| JPS6059170B2 (en) | Manufacturing method of glassy carbon thin plate | |
| DE3220559C2 (en) | ||
| US20060125131A1 (en) | Carbonaceous porous material and method of manufacturing same | |
| US4882102A (en) | Process for producing hard carbonaceous sheets | |
| US5096633A (en) | Process of making a diaphragm of carbonaceous material | |
| JPS61251503A (en) | Carbon stick and production thereof | |
| JPH0135766B2 (en) | ||
| JP3600690B2 (en) | Carbon composite material and method for producing the same | |
| JPH042546B2 (en) | ||
| JPS60112609A (en) | Preparation of rigid molded article of carbon | |
| JPH027697A (en) | Manufacture of diaphragm for all carbon acoustic equipment | |
| JPS6090806A (en) | Impermeable molded carbon body and its manufacture | |
| JPH01146498A (en) | Manufacture of diaphragm for full carbonaceous speaker | |
| JPH0694363B2 (en) | Glassy carbon molding | |
| JP2012180428A (en) | Fired pencil lead |