JPS5823324B2 - Touhou Saker-Bon no Seizouhou - Google Patents

Touhou Saker-Bon no Seizouhou

Info

Publication number
JPS5823324B2
JPS5823324B2 JP50055470A JP5547075A JPS5823324B2 JP S5823324 B2 JPS5823324 B2 JP S5823324B2 JP 50055470 A JP50055470 A JP 50055470A JP 5547075 A JP5547075 A JP 5547075A JP S5823324 B2 JPS5823324 B2 JP S5823324B2
Authority
JP
Japan
Prior art keywords
carbon
seizouhou
touhou
saker
bon
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
Application number
JP50055470A
Other languages
Japanese (ja)
Other versions
JPS51131496A (en
Inventor
持田勲
竹下健次郎
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.)
Nippon Steel Chemical and Materials Co Ltd
Original Assignee
Nittetsu Chemical Industrial 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 Nittetsu Chemical Industrial Co Ltd filed Critical Nittetsu Chemical Industrial Co Ltd
Priority to JP50055470A priority Critical patent/JPS5823324B2/en
Publication of JPS51131496A publication Critical patent/JPS51131496A/en
Publication of JPS5823324B2 publication Critical patent/JPS5823324B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は石炭系ピッチ(コールクールピッチ)、石油系
ピッチ(ナフサクールピッチ、゛エチレンタ・−ルピツ
チ、原油熱分解残渣油等)、天然または合成高分子化合
物(ポリスチレン樹脂、ポリ塩化ビニール樹脂、ポリプ
ロピレン樹脂等)、または多環芳香核を有する炭化水素
類(ナフタジン、ピレン、アセナフテン、カルバゾール
等)を竿独、または混合、または適当な溶媒(ノルマル
ヘキサン、ジグライム等)と共に、アルカリ金属(ナト
リウム、カリウム等)を触媒として加熱して溶媒。
Detailed Description of the Invention The present invention is applicable to coal-based pitch (coal cool pitch), petroleum-based pitch (naphtha cool pitch, ethylene tar pitch, crude oil pyrolysis residue oil, etc.), natural or synthetic polymer compounds (polystyrene resin, etc.). , polyvinyl chloride resin, polypropylene resin, etc.), or hydrocarbons having polycyclic aromatic nuclei (naphthazine, pyrene, acenaphthene, carbazole, etc.) alone or in combination, or together with an appropriate solvent (n-hexane, diglyme, etc.) , a solvent heated with an alkali metal (sodium, potassium, etc.) as a catalyst.

及び揮発分を駆逐後炭化することを特徴とする等方性カ
ーボンの製造法に関する。
The present invention also relates to a method for producing isotropic carbon, which comprises carbonizing after expelling volatile matter.

一般に、木材や鼾殻等の非溶融性物質の炭化物は等方性
のカーボンを与えるが、石炭系ピッチや石油系ピッチ等
の溶融性物質は異方性の炭化物を与えることが知られて
いる。
In general, carbides of non-melting materials such as wood and grasshopper shells give isotropic carbon, but melting materials such as coal pitch and petroleum pitch are known to give anisotropic carbides. .

しかるに、本発明者らは後者の物質からもアルカリ金属
の存在下において加熱炭化することによ・す、高収率で
等方性カーボンを生成させることができることを発見し
、本発明を完成した。
However, the present inventors have discovered that isotropic carbon can be produced in high yield from the latter substance by heating and carbonizing it in the presence of an alkali metal, and have completed the present invention. .

しかも。本発明による等方性カーボンはこれ迄に知られ
ている木炭や活性炭、あるいはポリフルフリルアルコー
ルからのグラシイカーボン等の等方性カーボンとは異っ
た性質を有し、特殊な用途が期待される。
Moreover. The isotropic carbon according to the present invention has properties different from previously known isotropic carbons such as charcoal, activated carbon, or glassy carbon made from polyfurfuryl alcohol, and is expected to have special uses. Ru.

次に本発明の原理と方法について説明する。Next, the principle and method of the present invention will be explained.

一般に有機物が炭化する過程において、分解、脱水・脱
水素、環化、縮合、重合等の化学反応が;溶融状態で進
行した場合には、後処理として2500℃以上の黒鉛化
処理を施すと異方性にすぐれた黒鉛を与える。
Generally, in the process of carbonization of organic substances, chemical reactions such as decomposition, dehydration/dehydrogenation, cyclization, condensation, and polymerization proceed in a molten state, and if they proceed in a molten state, graphitization treatment at a temperature of 2500°C or higher may be applied as a post-treatment. Provides graphite with excellent orientation.

これに対して、アルカリ金属(カリウム、ナトリウム等
)を触媒とした場合の炭化過程では100〜200℃で
一旦溶融状態、を経るが、その縮合、集合、脱水系等の
反応が急速に進行し、7,8M平面芳香族化合物となり
不融状態となる。
On the other hand, in the carbonization process when an alkali metal (potassium, sodium, etc.) is used as a catalyst, it is once in a molten state at 100 to 200°C, but reactions such as condensation, aggregation, and dehydration proceed rapidly. , a 7,8M planar aromatic compound and becomes infusible.

このため、2500℃以上の黒鉛化処理によっても結晶
の成長や分子の配向がほとんど進行せず、したがって等
方性カーボンを生成;するものと考えられる。
For this reason, it is thought that even by graphitization treatment at 2500° C. or higher, crystal growth and molecular orientation hardly progress, and therefore isotropic carbon is produced.

アルカリ金属の活性は。カリウム〉ナトリウム〉リチウ
ムの順序の強力な触媒作用を有する。
What is the activity of alkali metals? It has a strong catalytic effect in the order of potassium>sodium>lithium.

触媒を均一に分散させることは、ヘキサン、ジグライム
等の溶媒を使用すれば可能である。
Uniform dispersion of the catalyst is possible by using a solvent such as hexane or diglyme.

さらに溶媒の沸点付近において短時i間保持することに
よって、電荷移動錯体の形成を促進し、ある程度の縮合
を進行させればアルカリ金属の使用量を低減しても高い
炭素収率が可能となる。
Furthermore, by holding the solvent near the boiling point for a short period of time, the formation of a charge transfer complex is promoted, and if condensation progresses to a certain extent, a high carbon yield can be achieved even if the amount of alkali metal used is reduced. .

すなわち加熱手段として300℃以下の温度で加熱し、
さらに300℃以上の高温加熱することにより、原料中
に触媒が均一に分散し好ましい結果が得られる。
That is, heating at a temperature of 300°C or less as a heating means,
Further, by heating at a high temperature of 300° C. or higher, the catalyst is uniformly dispersed in the raw material, and favorable results can be obtained.

但し溶媒を使用しなくても炭化は進行する。However, carbonization proceeds even without using a solvent.

**次に各種の原料
から得られる炭素材(等方性カーボン)の収率と性状を
第1表に示す。
**Next, Table 1 shows the yield and properties of carbon materials (isotropic carbon) obtained from various raw materials.

この炭素材の特徴は極めて小さい表面積と結晶径にあり
、不侵透性炭素材への応用が考えられる。
This carbon material is characterized by its extremely small surface area and crystal size, and its application as an impermeable carbon material is considered.

次に本発明の実施例について説明する。Next, examples of the present invention will be described.

実施例 1 還流冷却器付フラスコにナフタレン10g、カリウム3
g及び溶媒として約5mlの正ヘキサンを装入し、窒素
気流中にて約1時間加熱する。
Example 1 10 g of naphthalene and 3 potassium in a flask with a reflux condenser
g and about 5 ml of normal hexane as a solvent, and heated in a nitrogen stream for about 1 hour.

次に還流冷却器をはずして溶媒を除去しなから径々に昇
温し、500℃にて約2時間加熱炭化する。
Next, the reflux condenser was removed and the solvent was removed, and then the temperature was gradually raised and carbonized by heating at 500° C. for about 2 hours.

得られた炭化物をメタノール、水で順次処理し、乾燥後
さらに2000℃以上の高温で熱処理し、目的の等方性
カーボンを製造する。
The obtained carbide is sequentially treated with methanol and water, and after drying, it is further heat-treated at a high temperature of 2000° C. or higher to produce the desired isotropic carbon.

この時の炭素収率は70係である。The carbon yield at this time was 70%.

実施例 2 還流冷却器付フラスコにアントラセン10g、カリウム
2.5gを装入し、昇温速度150℃/ h rで58
0℃迄加熱2時間保持後昇温速度10℃/minで25
00℃迄加熱30分保持して目的の等方性カーボンを製
造する。
Example 2 10 g of anthracene and 2.5 g of potassium were placed in a flask equipped with a reflux condenser, and the temperature was raised to 58 °C at a heating rate of 150 °C/hr.
After heating to 0℃ and holding for 2 hours, increase temperature to 25℃ at a heating rate of 10℃/min.
The target isotropic carbon is produced by heating to 00° C. and maintaining it for 30 minutes.

この時炭素収率は80%である。At this time, the carbon yield was 80%.

実施例 3 石炭タールピッチ50g、カリウム7gをフラスコに入
れ、約200℃にて約1時間加熱したのち徐々に昇温し
、500℃〜600℃にて約2時間加熱炭化する。
Example 3 50 g of coal tar pitch and 7 g of potassium are placed in a flask and heated at about 200° C. for about 1 hour, then gradually raised to temperature, and heated and carbonized at 500° C. to 600° C. for about 2 hours.

次に前記実施例2と同様の処理をし、目的の等方性カー
ボンを製造する。
Next, the same treatment as in Example 2 is performed to produce the desired isotropic carbon.

この時の炭素収率は80係である。The carbon yield at this time was 80%.

Claims (1)

【特許請求の範囲】[Claims] 1 石炭系ピッチ、石油系ピッチ、合成樹脂、天然高分
子化合物、または多環芳香核を有する炭化水素類を牟独
、または混合、または他の溶媒と共・にアルカリ金属の
存在下に加熱炭化することを特徴とする等方性カーボン
の製造法。
1 Coal-based pitch, petroleum-based pitch, synthetic resin, natural polymer compound, or hydrocarbons having a polycyclic aromatic nucleus are heated and carbonized in the presence of an alkali metal, singly or as a mixture, or together with other solvents. A method for producing isotropic carbon characterized by:
JP50055470A 1975-05-13 1975-05-13 Touhou Saker-Bon no Seizouhou Expired JPS5823324B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50055470A JPS5823324B2 (en) 1975-05-13 1975-05-13 Touhou Saker-Bon no Seizouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50055470A JPS5823324B2 (en) 1975-05-13 1975-05-13 Touhou Saker-Bon no Seizouhou

Publications (2)

Publication Number Publication Date
JPS51131496A JPS51131496A (en) 1976-11-15
JPS5823324B2 true JPS5823324B2 (en) 1983-05-14

Family

ID=12999481

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50055470A Expired JPS5823324B2 (en) 1975-05-13 1975-05-13 Touhou Saker-Bon no Seizouhou

Country Status (1)

Country Link
JP (1) JPS5823324B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105280918B (en) * 2014-10-27 2018-04-10 湖南摩根海容新材料有限责任公司 A kind of preparation method of isotropic graphite material

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5092889A (en) * 1973-12-20 1975-07-24

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5092889A (en) * 1973-12-20 1975-07-24

Also Published As

Publication number Publication date
JPS51131496A (en) 1976-11-15

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