JPS63182208A - Production of raw material for forming novel carbon article by forming - Google Patents
Production of raw material for forming novel carbon article by formingInfo
- Publication number
- JPS63182208A JPS63182208A JP62012200A JP1220087A JPS63182208A JP S63182208 A JPS63182208 A JP S63182208A JP 62012200 A JP62012200 A JP 62012200A JP 1220087 A JP1220087 A JP 1220087A JP S63182208 A JPS63182208 A JP S63182208A
- Authority
- JP
- Japan
- Prior art keywords
- molten salt
- lewis acid
- pitch
- raw material
- forming
- 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
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 22
- 239000002994 raw material Substances 0.000 title claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 150000003839 salts Chemical class 0.000 claims abstract description 20
- 239000011302 mesophase pitch Substances 0.000 claims abstract description 14
- 239000011295 pitch Substances 0.000 claims abstract description 12
- 239000011230 binding agent Substances 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims abstract description 7
- 239000011968 lewis acid catalyst Substances 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims abstract description 4
- 125000002091 cationic group Chemical group 0.000 claims abstract description 3
- 239000002841 Lewis acid Substances 0.000 claims abstract 3
- 150000007517 lewis acids Chemical class 0.000 claims abstract 3
- 239000000843 powder Substances 0.000 claims description 9
- 238000010304 firing Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 5
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims description 3
- 239000011337 anisotropic pitch Substances 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims description 2
- 238000010000 carbonizing Methods 0.000 claims 1
- 239000003054 catalyst Substances 0.000 claims 1
- 239000011261 inert gas Substances 0.000 claims 1
- 150000002894 organic compounds Chemical class 0.000 claims 1
- 239000002904 solvent Substances 0.000 claims 1
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 abstract description 18
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 abstract description 10
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract description 8
- 239000000203 mixture Substances 0.000 abstract description 8
- 238000002844 melting Methods 0.000 abstract description 5
- 230000008018 melting Effects 0.000 abstract description 5
- 239000011780 sodium chloride Substances 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 3
- 229910021382 natural graphite Inorganic materials 0.000 abstract description 3
- -1 alkyl pyridinium halide Chemical class 0.000 abstract 2
- 239000011833 salt mixture Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 description 8
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical group C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 5
- 229910002804 graphite Inorganic materials 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 239000010439 graphite Substances 0.000 description 4
- 239000006229 carbon black Substances 0.000 description 3
- 239000012778 molding material Substances 0.000 description 3
- 239000000376 reactant Substances 0.000 description 3
- 239000011269 tar Substances 0.000 description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 2
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000012300 argon atmosphere Substances 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000000280 densification Methods 0.000 description 2
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000004820 halides Chemical class 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000005457 ice water Substances 0.000 description 2
- YNPNZTXNASCQKK-UHFFFAOYSA-N phenanthrene Chemical compound C1=CC=C2C3=CC=CC=C3C=CC2=C1 YNPNZTXNASCQKK-UHFFFAOYSA-N 0.000 description 2
- 235000011164 potassium chloride Nutrition 0.000 description 2
- 239000001103 potassium chloride Substances 0.000 description 2
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- ABFDKXBSQCTIKH-UHFFFAOYSA-M 1-ethylpyridin-1-ium;bromide Chemical compound [Br-].CC[N+]1=CC=CC=C1 ABFDKXBSQCTIKH-UHFFFAOYSA-M 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical group COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- 108091006629 SLC13A2 Proteins 0.000 description 1
- PJANXHGTPQOBST-VAWYXSNFSA-N Stilbene Natural products C=1C=CC=CC=1/C=C/C1=CC=CC=C1 PJANXHGTPQOBST-VAWYXSNFSA-N 0.000 description 1
- 239000012615 aggregate Substances 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 150000001350 alkyl halides Chemical class 0.000 description 1
- 125000003710 aryl alkyl group Chemical group 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- RDHPKYGYEGBMSE-UHFFFAOYSA-N bromoethane Chemical compound CCBr RDHPKYGYEGBMSE-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006355 external stress Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 239000006253 pitch coke Substances 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- PJANXHGTPQOBST-UHFFFAOYSA-N stilbene Chemical compound C=1C=CC=CC=1C=CC1=CC=CC=C1 PJANXHGTPQOBST-UHFFFAOYSA-N 0.000 description 1
- 235000021286 stilbenes Nutrition 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、新炭素製品成形用原材料の製造方法に関する
。詳しくは、本発明は、極めて均質で、製品たる成形物
の寸法精度が高く、新炭素材料として要求される電気的
、熱的、及び化学的特性に優れ、かつその性能を予め設
計することが可能な機能性新炭素成形物を得るための原
料となるドーマントメソフェーズピッチ(Domant
MesophasePitch潜在異方性ピッチ)、
及び/又は等方性ピッチが全表面に均質に被覆された新
炭素製品成形用原材料の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing a raw material for forming new carbon products. Specifically, the present invention is extremely homogeneous, has high dimensional accuracy of the molded product, has excellent electrical, thermal, and chemical properties required as a new carbon material, and has the ability to design its performance in advance. Dormant mesophase pitch (Domant mesophase pitch) is a raw material for obtaining functional new carbon molded products.
MesophasePitch potential anisotropic pitch),
and/or relates to a method for producing a raw material for forming a new carbon product in which the entire surface is uniformly coated with isotropic pitch.
(従来の技術)
現在、炭素成形体は、一般に原料として石油コ−クス、
ピッチコークス、黒鉛、カーボンブラック等を骨材とし
、ピッチ、タール、合成樹脂などを粘結材として、両者
を混練・成形し焼成することによって作られる。そのた
め、一般には、大型ブロックとして製造され、その組織
も粗く、材質も十分な特性が発揮されず、所望の形状に
直接成形することは殆ど不可能であった。骨材に対して
粘結材を多く用いる関係で、焼成時の収縮や応力変形に
よる歪が多く発生する欠点を有していた。(Prior art) Currently, carbon molded bodies are generally produced using petroleum coke as a raw material.
It is made by using pitch coke, graphite, carbon black, etc. as an aggregate, pitch, tar, synthetic resin, etc. as a caking agent, and kneading, molding, and firing the two. Therefore, it is generally manufactured as a large block, and its structure is rough and the material does not exhibit sufficient properties, making it almost impossible to directly mold it into a desired shape. Since a large amount of caking material is used for the aggregate, it has the disadvantage that a large amount of distortion occurs due to shrinkage and stress deformation during firing.
従って、寸法精度を高める目的や緻密化を行わせるには
、大量の骨材を極めて少量の粘結材成分で結合するか、
又は原料骨材を10μm以下に微粉砕し、これに粘結材
を加えて、上記手順により製造される。従って、骨材/
粘結材比が大きかったり、骨材が微粉になればなる程骨
材と粘結材との混練は困難になり、粘結材の均一な分散
が計り難くなる。特に、極めて微粒で粒子同士が結合し
た高次構造を有するカーボンブラックや平均粒径が1μ
m程度の黒鉛粉末では、その比表面積が大きく、この様
な粉末を骨材とするときは二粘結材との混合分散及び混
練が一回の操作では困難で、多数回の操作を行うことを
余儀なくされている。大きな比表面積を持つ微粒炭素粉
末を用いる場合、或は大量の骨材を極めて少量の粘結材
成分によってその表面を均一に被覆することについては
、過去に、カーボンブランク表面にスチレンモノマーや
アクリルニトリル、ビニルベンゼン等の低分子物をグラ
フトさせるグラフトカーボンの製造や、微粒の天然黒鉛
粉末表面にメチルメタクリレートモノマーをグラフト重
合させる方法等についての知見があった。Therefore, in order to improve dimensional accuracy or achieve densification, a large amount of aggregate should be bound with a very small amount of binder component, or
Alternatively, it can be manufactured by pulverizing the raw material aggregate to 10 μm or less, adding a caking agent thereto, and following the above procedure. Therefore, aggregate/
The larger the caking agent ratio or the finer the aggregate, the more difficult it becomes to mix the aggregate and the caking agent, and the more difficult it becomes to uniformly disperse the caking agent. In particular, carbon black has extremely fine particles and has a higher-order structure in which particles are bonded together, and the average particle size is 1μ.
Graphite powder has a large specific surface area, and when such powder is used as aggregate, it is difficult to mix, disperse, and knead with the second caking agent in one operation, and it is necessary to repeat the operation multiple times. are forced to do so. When using fine-grained carbon powder with a large specific surface area, or when covering a large amount of aggregate uniformly with a very small amount of binder component, in the past, styrene monomer or acrylonitrile was used on the surface of the carbon blank. There was knowledge about the production of grafted carbon by grafting low-molecular substances such as vinylbenzene, and the method of graft polymerizing methyl methacrylate monomer onto the surface of fine natural graphite powder.
しかしながら、スチレン樹脂や、ポリメチルメタクリレ
ート、ポリアクリルニトリル、ビニルベンゼン重合体は
、炭素収率に乏しく、焼成による骨材と粘結材との結合
が不十分であり、炭化粘結材としては、不適当である。However, styrene resin, polymethyl methacrylate, polyacrylonitrile, and vinylbenzene polymers have poor carbon yields, and the bonding between aggregate and binder by firing is insufficient, so that they cannot be used as carbonized binders. It's inappropriate.
従って、そのようにして得られる最終炭素成形品は、目
的とする特性を発揮できず、更に緻密化や高結晶度化を
計るために、一旦1000℃程度に焼成した成形体に、
再度タールやピッチまたは合成樹脂を加熱加圧含浸させ
焼成する操作を数回以上も繰り返したり・3000℃近
い高温度まで加熱したりする処理が施されていた。Therefore, the final carbon molded product obtained in this way could not exhibit the desired properties, and in order to achieve further densification and higher crystallinity, the molded product was fired at a temperature of about 1000°C.
The process of impregnating tar, pitch, or synthetic resin under heat and pressure, and then firing it was repeated several times or heated to a high temperature of nearly 3000°C.
(発明が解決使用とする問題点)
本発明の目的は、この様な従来技術の欠点を改善すべく
炭素材料の有する機能特性を高度に発揮し、製造に際し
ては煩雑な工程を避け、特に、賦形時の形状を全く損な
うことなく焼成でき、かつ焼成に際して高い寸法精度が
期待できる新炭素成形体の原料として用いる新居素成形
用材料の製造方法を提供することである。(Problems to be Solved by the Invention) The purpose of the present invention is to improve the shortcomings of the prior art by highly demonstrating the functional characteristics of carbon materials, avoiding complicated manufacturing steps, and, in particular, It is an object of the present invention to provide a method for producing an Arai blank molding material that can be fired without impairing its shape at the time of shaping and is used as a raw material for a new carbon molded body that can be expected to have high dimensional accuracy during firing.
(問題点を解決するための手段)
本願発明者等は、室温溶融塩中における炭化水素のイオ
ン機構による低温炭素化を研究する過程において、通常
の炭素化反応よりも遥かに低温で生成するメソフェーズ
ピッチが、反応系内に既に存在する炭素粒子を核として
、その表面上に均一に析出する現象を発見した。ここに
、本明細書に言う「メソフェーズピッチ」とは、−見等
方性の様ではあるが、一方向に外部応力が作用すると、
それに応じて容易に配回して異方性組織を与える性質を
持つピッチのことである。そこで、溶融塩液中に骨材と
しての微粒黒鉛粉末を共存させた状態で、炭化水素を重
合反応させてピッチ化し、該微粒黒鉛粉末表面全体にメ
ソフェーズ状態のピッチが均一に付着するかどうかを試
み、結果として良好な被覆が成されていることを確認し
た。更に、このメソフェーズピッチ被覆炭素粉末を用い
て、これに粘結材を加えることなく、常法に従って加圧
成形後焼成した結果、極めて均質で、結晶性が高く緻密
なものから、所望の気孔率を有する等方的なものまで、
物理的、化学的性質を異にする材質の設計が可能で、寸
法精度に優れた新炭素成形体を自由に製造することが可
能であった。(Means for Solving the Problems) In the process of researching low-temperature carbonization of hydrocarbons in room-temperature molten salts through an ionic mechanism, the inventors of the present application discovered that a mesophase is produced at a much lower temperature than that of a normal carbonization reaction. We discovered a phenomenon in which pitch precipitates uniformly on the surface of carbon particles already present in the reaction system, using them as nuclei. Here, the "mesophase pitch" referred to in this specification is - Although it appears to be isotropic, when external stress acts in one direction,
It is a pitch that can be easily arranged accordingly and has the property of providing an anisotropic structure. Therefore, in the presence of fine graphite powder as an aggregate in a molten salt solution, hydrocarbons were polymerized to form pitch, and we investigated whether pitch in a mesophase state would uniformly adhere to the entire surface of the fine graphite powder. As a result, it was confirmed that a good coating was obtained. Furthermore, using this mesophase pitch-coated carbon powder, the powder was pressure-molded and fired in a conventional manner without adding a binder, resulting in extremely homogeneous, highly crystalline and dense powder with the desired porosity. up to isotropic ones with
It was possible to design materials with different physical and chemical properties, and it was possible to freely produce new carbon molded bodies with excellent dimensional accuracy.
ここで、本発明において使用の、室温、若しくは100
℃以下の低温度下で液状を呈する一種の溶融塩について
説明する。Here, the temperature used in the present invention is room temperature or 100%
A type of molten salt that becomes liquid at low temperatures below 0.degree. C. will be described.
まず、室温下で液状である有機カチオン性溶融塩として
は、アルキルハライドとピリジンから合成されたアルキ
ルピリジニウムハライドやジアルキルイミダゾリウムハ
ライド1当量に、ルイス酸触媒として、例えば塩化アル
ミニウム等を1当量以上加え加熱して、混合溶解せしめ
室温まで冷却することによって得られる。First, as an organic cationic molten salt that is liquid at room temperature, one equivalent of alkylpyridinium halide or dialkylimidazolium halide synthesized from an alkyl halide and pyridine is added with one equivalent or more of aluminum chloride, etc. as a Lewis acid catalyst. It is obtained by heating, mixing and dissolving, and cooling to room temperature.
I八
R,R” : 低級アルキル、又はアラルキルX :
ハロゲン
n ≧ 1
この溶液組成は、右辺に示すように、その大部分がイオ
ンであることと、塩化アルミニウムを多量に溶存してい
ることが特徴である。この溶融塩中に、アルゴンに混ぜ
てジクロロエタンやトリクロロエタンを吹き込んだとこ
ろ、いずれも100〜300℃で脱HCI反応を起こし
、多くの場合BI酸成分ベンゼン不溶成分)を80%以
上含むメソフェーズピッチが得られた。I8R,R”: Lower alkyl or aralkyl X:
Halogen n ≧ 1 As shown on the right side, this solution composition is characterized by being mostly ions and containing a large amount of dissolved aluminum chloride. When dichloroethane or trichloroethane is mixed with argon and blown into this molten salt, a de-HCI reaction occurs at 100 to 300°C, and in most cases, mesophase pitch containing 80% or more of BI acid component (benzene insoluble component) is obtained. It was done.
また、無機溶融塩としては、次式にその組成を示すよう
な塩化アルミニウム、塩化ナトリウム、塩化カリウムの
三元系溶融塩(融点が95℃)が−例として挙げられる
。Examples of the inorganic molten salt include a ternary molten salt of aluminum chloride, sodium chloride, and potassium chloride (melting point: 95° C.) whose composition is shown in the following formula.
0.60 AlCl3 + 0.26 NaC1+
0.14 MCI −0,26Na ” + 0
0.14 K ” +0.40 AlCl4.− +
0.20 AlCl:tこの溶融塩の中では、芳香族
炭化水素が容易に脱水素重縮合して、200〜300℃
において、高収率でタール、ピッチ、又はコーク(ro
w coke)を生じる。例えば、ナフタレンからは、
300℃10時間の処理で、黒色フレーク状の炭化物が
析出したが、そのBl含有率は92%で、BE酸成分H
/C原子比は0.42であった。この場合、生成物は、
反応温度と時間を制御することによって、コークス状態
からドーマントメソフェーズピッチ状態、等方性ピッチ
状態、タール状態とその状態を変えて得ることが出来る
。0.60 AlCl3 + 0.26 NaC1+
0.14 MCI −0,26Na ” + 0
0.14 K” +0.40 AlCl4.- +
0.20 AlCl:t In this molten salt, aromatic hydrocarbons are easily dehydrogenated and polycondensed at 200-300°C.
tar, pitch, or coke (RO) in high yield.
w coke). For example, from naphthalene,
After treatment at 300°C for 10 hours, black flake-like carbide was precipitated, but the Bl content was 92%, and the BE acid component H
/C atomic ratio was 0.42. In this case, the product is
By controlling the reaction temperature and time, it is possible to change the state from a coke state to a dormant mesophase pitch state, an isotropic pitch state, and a tar state.
反応温度と時間を制御することによって、コークス状態
からドーマントメソフェーズピッチ状態、タール状態と
その生成物を変えて得ることが出来る。By controlling the reaction temperature and time, it is possible to change the product from a coke state to a dormant mesophase pitch state to a tar state.
芳香族炭化水素の反応性序列は、
アントラセン〉ナフタレン〉フェナントレン〉スチルベ
ン〉ビフェニル〉ベンゼン〉キノリンの順であった。The order of reactivity of aromatic hydrocarbons was anthracene, naphthalene, phenanthrene, stilbene, biphenyl, benzene, and quinoline.
なお、本発明の目的に適した無機溶融塩の例としては、
上述の物の外に、塩化ナトリウムと塩化鉄(融点156
℃)の混合溶融塩、シュウ化ナトリウムと塩化アルミニ
ウム(融点90°C)の混合溶融塩等を挙げることがで
きる。In addition, examples of inorganic molten salts suitable for the purpose of the present invention include:
In addition to the above, sodium chloride and iron chloride (melting point 156
℃), a mixed molten salt of sodium oxalide and aluminum chloride (melting point: 90°C), and the like.
(実施例) 次に、本発明を実施例を挙げて説明する。(Example) Next, the present invention will be explained by giving examples.
大旌災−上
反応容器中で、アルゴン雰囲気下に、エチルブロマイド
とピリジンから合成したエチルピリジニウムブロマイド
1モル中に塩化アルミニウム2モルを加え、100℃ま
で加熱して完全に溶解させた後、室温まで冷却すること
によって、室温下で液状の溶融塩を得た。Great Calamity - In the upper reaction vessel, under an argon atmosphere, add 2 moles of aluminum chloride to 1 mole of ethylpyridinium bromide synthesized from ethyl bromide and pyridine, heat it to 100°C to completely dissolve it, and then leave it at room temperature. A liquid molten salt was obtained at room temperature.
この反応器中に、微粒天然黒鉛(日本黒鉛社製平均粒径
1μm)150gを投入し、全体が均一なサスペンショ
ン状態を呈するまで攪拌した。次に、ナフタレン(東京
化学社製)15gを攪拌しながら添加し、230℃まで
緩やかに昇温させ、この温度で5時間保持した後、加熱
を停止させ冷却してから、反応物を氷水中に注入し、水
洗した後濾別した。次に、これを乾燥させて目的とする
新炭製成形用材料である微粒黒鉛の表面にドーマントメ
ソフェーズピッチが均一に被覆された粉末163.7g
を得た。Into this reactor, 150 g of fine-grained natural graphite (manufactured by Nippon Graphite Co., Ltd., average particle size: 1 μm) was placed and stirred until the whole exhibited a uniform suspension state. Next, 15 g of naphthalene (manufactured by Tokyo Kagaku Co., Ltd.) was added with stirring, the temperature was slowly raised to 230°C, and after holding at this temperature for 5 hours, the heating was stopped and cooled, and the reactant was placed in ice water. After washing with water, the solution was filtered. Next, this was dried to produce 163.7 g of powder that uniformly coated the surface of fine graphite, which is the desired new coal molding material, with dormant mesophase pitch.
I got it.
寒施炎−又
反応容器中で、アルゴン雰囲気下に、塩化アルミニウム
2.40モル、塩化カリウム0.16モル、塩化ナトリ
ウム1.04モルの混合物を溶融(融点95℃)させた
。この溶融塩中に、膨張黒鉛(平均粒径10μm)50
g及びナフタレン50gを投入し、 100°Cに保
ち、全体が均質になるまで攪拌した。更に、230℃に
なるまで昇温させ、この温度を5時間保持して反応を継
続させた。反応終了後、加熱を停止し、冷却してから反
応物を取り出し、これを氷水中に注入し、洗浄した後、
濾別した。次に、これを乾燥させて、目的とする新炭製
成形用材料である膨張黒鉛の全表面にドーマントメソフ
ェーズピッチで均一に被覆された粉末98gを得た。A mixture of 2.40 moles of aluminum chloride, 0.16 moles of potassium chloride, and 1.04 moles of sodium chloride was melted (melting point: 95 DEG C.) in a cold flame reactor under an argon atmosphere. In this molten salt, 50% of expanded graphite (average particle size 10 μm) was added.
g and 50 g of naphthalene were added, the temperature was maintained at 100°C, and the mixture was stirred until the whole was homogeneous. Furthermore, the temperature was raised to 230° C., and this temperature was maintained for 5 hours to continue the reaction. After the reaction is complete, stop the heating, cool it down, take out the reactant, pour it into ice water, wash it,
It was filtered. Next, this was dried to obtain 98 g of powder in which the entire surface of expanded graphite, which was the intended new coal molding material, was uniformly coated with dormant mesophase pitch.
去旌拠−1
実施例1に使用した室温溶融塩500g中に、平均粒径
0.07μmのカーボンブランク50gを加え、室温下
で攪拌し、全体が均一なサスペンション状態を呈するよ
うにした。系全体を230°Cに加熱保持しつつ、アル
ゴンガスに混ぜてジクロロエタンを原料濃度200mg
/l、ガス流量151/時間で吹き込み、5時間反応を
継続させた。その後、反応を停止させ、室温まで冷却し
て反応物を取り出し、実施例1と同様に処理して、目的
とする新炭製成形用材料であるカーボンブラックの全表
面がドーマントメソフェーズピッチで均一に被覆された
粉末54gを得た。Testing Base-1 50 g of carbon blank having an average particle size of 0.07 μm was added to 500 g of the room temperature molten salt used in Example 1, and the mixture was stirred at room temperature to form a uniform suspension state. While heating and maintaining the entire system at 230°C, dichloroethane was mixed with argon gas to a raw material concentration of 200mg.
/l at a gas flow rate of 151/hour, and the reaction was continued for 5 hours. Thereafter, the reaction was stopped, cooled to room temperature, and the reactants were taken out and treated in the same manner as in Example 1, so that the entire surface of carbon black, which is the desired new carbon forming material, was uniformly coated with dormant mesophase pitch. 54 g of coated powder were obtained.
Claims (1)
相中で炭化焼成を行って高性能な新炭素成形体を製造す
るに際し、用いる成形用粉末材料を製造する方法におい
て、ルイス酸触媒を多量に含む混合溶融塩を溶媒兼触媒
として用い、この液中に炭素微粉末と低分子量有機化合
物とを投入し、撹拌下加熱処理を施すことによって、該
炭素微粉末の全表面に粘結材としてのドーマントメソフ
ェーズピッチ(潜在的異方性ピッチ)、及び/又は等方
性ピッチを被覆することを特徴とする新炭素製品成形用
原材料の製造方法。 2)該ルイス酸触媒を多量に含む混合溶融塩は、ルイス
酸を多量に溶存している有機カチオン性溶融塩、若しく
はルイス酸を多量に溶存している無機溶融塩であること
を特徴とする第1項に記載の新炭素製品成形用原材料の
製造方法。 3)炭素微粉末表面にメソフェーズピッチ、及び/又は
等方性ピッチを被覆させる際の加熱処理温度(反応温度
)は、300℃以下であることを特徴とする第1項に記
載の新炭素製品成形用原材料の製造方法。[Scope of Claims] 1) A molding powder material to be used when producing a high-performance new carbon molded body by carbonizing and firing it in an inert gas phase after shaping it into a pre-designed arbitrary shape. In the manufacturing method, a mixed molten salt containing a large amount of Lewis acid catalyst is used as a solvent and catalyst, fine carbon powder and a low molecular weight organic compound are added to this liquid, and the carbon is heated under stirring. A method for producing a raw material for forming a new carbon product, which comprises coating the entire surface of fine powder with dormant mesophase pitch (potentially anisotropic pitch) and/or isotropic pitch as a binding agent. 2) The mixed molten salt containing a large amount of Lewis acid catalyst is characterized in that it is an organic cationic molten salt containing a large amount of Lewis acid dissolved therein, or an inorganic molten salt containing a large amount of Lewis acid dissolved therein. A method for producing a raw material for forming a new carbon product as described in paragraph 1. 3) The new carbon product according to item 1, wherein the heat treatment temperature (reaction temperature) when coating the surface of the carbon fine powder with mesophase pitch and/or isotropic pitch is 300°C or less. Method for manufacturing raw materials for molding.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62012200A JPS63182208A (en) | 1987-01-23 | 1987-01-23 | Production of raw material for forming novel carbon article by forming |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62012200A JPS63182208A (en) | 1987-01-23 | 1987-01-23 | Production of raw material for forming novel carbon article by forming |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63182208A true JPS63182208A (en) | 1988-07-27 |
JPH0575690B2 JPH0575690B2 (en) | 1993-10-21 |
Family
ID=11798764
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62012200A Granted JPS63182208A (en) | 1987-01-23 | 1987-01-23 | Production of raw material for forming novel carbon article by forming |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63182208A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2643897A1 (en) * | 1989-02-23 | 1990-09-07 | Mitsubishi Pencil Co | PROCESS FOR THE MANUFACTURE OF A CARBON MATERIAL, WEAPON OF A COMPOSITE OF CARBON FIBERS |
FR2659962A1 (en) * | 1990-03-20 | 1991-09-27 | Agency Ind Science Techn | Process for the production of a high-performance C/C composite, and high-performance C/C composite produced by this process |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62283807A (en) * | 1986-05-29 | 1987-12-09 | Sugiro Otani | Impermeable carbon material and its production |
-
1987
- 1987-01-23 JP JP62012200A patent/JPS63182208A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62283807A (en) * | 1986-05-29 | 1987-12-09 | Sugiro Otani | Impermeable carbon material and its production |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2643897A1 (en) * | 1989-02-23 | 1990-09-07 | Mitsubishi Pencil Co | PROCESS FOR THE MANUFACTURE OF A CARBON MATERIAL, WEAPON OF A COMPOSITE OF CARBON FIBERS |
US5096519A (en) * | 1989-02-23 | 1992-03-17 | Mitsubishi Pencil Co., Ltd. | Process for preparation of carbon fiber composite reinforced carbonaceous material |
FR2659962A1 (en) * | 1990-03-20 | 1991-09-27 | Agency Ind Science Techn | Process for the production of a high-performance C/C composite, and high-performance C/C composite produced by this process |
US5306563A (en) * | 1990-03-20 | 1994-04-26 | Agency Of Industrial Science & Technology | High-performance C/C composite |
Also Published As
Publication number | Publication date |
---|---|
JPH0575690B2 (en) | 1993-10-21 |
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