JPS6024043B2 - Method for producing isotropic carbon - Google Patents
Method for producing isotropic carbonInfo
- Publication number
- JPS6024043B2 JPS6024043B2 JP52160676A JP16067677A JPS6024043B2 JP S6024043 B2 JPS6024043 B2 JP S6024043B2 JP 52160676 A JP52160676 A JP 52160676A JP 16067677 A JP16067677 A JP 16067677A JP S6024043 B2 JPS6024043 B2 JP S6024043B2
- Authority
- JP
- Japan
- Prior art keywords
- present
- carbon
- catalyst
- heavy oil
- oxide
- 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
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- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Description
【発明の詳細な説明】 本発明は等万性カーボンの製造方法に関する。[Detailed description of the invention] The present invention relates to a method for producing isomerly carbon.
更に詳細には石炭系重質油または石油系車質油を触媒の
存在下に加熱することにより等方性カーボンを製造する
ものである。一般に非溶融物質の炭化物は等方性カーボ
ンとなり、溶融性物質の炭化物は異方性カーボンとなる
ことが知られている。More specifically, isotropic carbon is produced by heating coal-based heavy oil or petroleum-based vehicle oil in the presence of a catalyst. It is generally known that carbide of non-melting substances becomes isotropic carbon, and carbide of melting substances becomes anisotropic carbon.
すなわち炭化過程の400〜600qoの段階で熔融状
態が存在しない場合には等方性カーボン、溶融状態が存
在すれば異方性カーボンとなる。前者の例といま木炭、
活性炭、グラッシーカーボン等があり、後者の例として
は石油系重質油、石炭系車質油等がある。本発明は溶融
性物質から等方性カーボンを製造する方法を提供するも
のである。That is, if a molten state does not exist at the stage of 400 to 600 qo in the carbonization process, it becomes isotropic carbon, and if a molten state exists, it becomes anisotropic carbon. An example of the former is charcoal,
Examples of the latter include activated carbon and glassy carbon, and examples of the latter include petroleum-based heavy oil and coal-based vehicle oil. The present invention provides a method for producing isotropic carbon from a meltable substance.
すなわち、本発明は通常の加熱炭化によれば異方性カー
ボンを与える溶融性物質を特定の触媒の存在下に加熱を
行なうと400〜600qCの段階で溶融状態を起さず
に等万怪力ーボンを生成させることができことを見出し
、本発明を完成したものである。すなわち、本発明はニ
ッケル、コバルト、モリブデン、タングステン、クロム
およびバナジウムよりなる群から選ばれる金属、該金属
の酸化物または該金属の複酸化物の1種または2種以上
を触媒として用い、該触媒の存在下に石炭系重質油また
は石油系重質油を加熱することにより等方性カーボンを
製造するものである。In other words, the present invention proposes that when a meltable substance that produces anisotropic carbon by ordinary heating carbonization is heated in the presence of a specific catalyst, it can be heated to 10,000 ton of force without causing a molten state at a temperature of 400 to 600 qC. The present invention has been completed based on the discovery that it is possible to generate the following. That is, the present invention uses as a catalyst one or more of a metal selected from the group consisting of nickel, cobalt, molybdenum, tungsten, chromium, and vanadium, an oxide of the metal, or a double oxide of the metal; Isotropic carbon is produced by heating coal-based heavy oil or petroleum-based heavy oil in the presence of .
以下に本発明を詳述する。The present invention will be explained in detail below.
本発明においては原料重質油に触媒を添加し、常圧また
は加圧にて不活性ガス雰囲気下で加熱する。In the present invention, a catalyst is added to raw material heavy oil and heated under an inert gas atmosphere at normal pressure or pressurization.
原料電質油は350〜450q0の温度領域で加熱溶融
性をもつピッチ状物質となり、約600℃になると加熱
溶融をもたない固体状物質となる。この団体状物質を更
に加熱し25000C以上にして黒鉛化することとによ
り本発明の等万性カーボンが得られる。この際、黒鉛化
処理前の固体状物質から予め触媒を除去することもでき
る。もちろん固体状物質に含まれる触媒を除去して黒鉛
化しても、また除去せずに黒鉛化して等万性に変化は見
られない。すなわち、本発明においては加熱炭化の初期
段階である約60000以下の温度領域において原料重
質油と本発明の触媒を共存させることにより等方性カー
ボンの前駆体が形成され、それを600℃から更に25
00qo以上の温度に加熱することにより等方性カーボ
ンが生成されるものと思われる。本発明において加熱方
法は特に限定されるものではないが、ピッチ状物質が生
成する温度領域までは徐々に昇温することが好ましく、
例えば0.01〜1ooo/minの昇温速度にて行な
うのが好ましい。またピッチ状物質が生成するまでは頚
拝しながら加熱するのが好ましい。もちろん灘梓を行な
わなくとも本発明は達成される。ピッチ状物質が生成す
る温度領域以降は、前記昇温速度で昇温してもよいし、
また更に昇温速度を速くしてもかまわないものでなあり
、特に限定されるものではない。本発明で用いる石炭系
重質油としては、例えばコールタール、石炭溶剤抽出油
等をあげることができる。The raw electrolyte oil becomes a pitch-like substance that melts when heated in a temperature range of 350 to 450 q0, and becomes a solid substance that does not melt when heated at about 600°C. By further heating this collective substance to 25,000 C or higher and graphitizing it, the isomertile carbon of the present invention can be obtained. At this time, the catalyst can also be removed in advance from the solid material before the graphitization treatment. Of course, even if the catalyst contained in the solid substance is removed and graphitized, or if it is graphitized without removal, no change is observed in isomerality. That is, in the present invention, an isotropic carbon precursor is formed by coexisting the raw material heavy oil and the catalyst of the present invention in a temperature range of about 60,000 °C or less, which is the initial stage of heating carbonization, and isotropic carbon precursor is formed from 600 °C to 600 °C. 25 more
It is believed that isotropic carbon is produced by heating to a temperature of 00qo or higher. In the present invention, the heating method is not particularly limited, but it is preferable to gradually raise the temperature to a temperature range where pitch-like substances are generated.
For example, it is preferable to carry out the heating at a rate of 0.01 to 100/min. Further, it is preferable to heat the mixture while worshiping it until a pitch-like substance is generated. Of course, the present invention can be achieved even without performing Nada Azusa. After the temperature range where pitch-like substances are generated, the temperature may be increased at the temperature increase rate, or
Furthermore, the temperature increase rate may be further increased, and is not particularly limited. Examples of the coal-based heavy oil used in the present invention include coal tar, coal solvent extracted oil, and the like.
石油系重質油としてはナフサタール、流動接触分解ター
ル、原油熱分解残溜池、原油常圧蒸留残油、原油減圧蒸
留残油をあげることができる。本発明において用いられ
るニッケル、コバルト、モリブデン、タングステン、ク
ロムおよびバナジウムの酸化物または複酸化物としては
、。Petroleum-based heavy oils include naphtha tar, fluid catalytic cracking tar, crude oil thermal cracking residue, crude oil atmospheric distillation residue, and crude oil vacuum distillation residue. The oxides or double oxides of nickel, cobalt, molybdenum, tungsten, chromium and vanadium used in the present invention include:
例えば酸化ニッケル(Ni○)、酸化コバルト(Coo
、Co304)、酸化モリブデン(Moo3)、ニッケ
ルモリブデン複酸化物(NjO・Moo3)、コバルト
モリブデン複酸化物(Coo・Moo3)、などを具体
的に例示できる。本発明においては、ニッケル、コバル
ト、モリブデン、タングステン、クロムおよびバナジウ
ムよりなる群から選ばれる金属、該金属の酸化物または
該金属の複酸化物は、、担体に坦持させて用いることも
できる。For example, nickel oxide (Ni○), cobalt oxide (Coo)
, Co304), molybdenum oxide (Moo3), nickel molybdenum double oxide (NjO.Moo3), cobalt molybdenum double oxide (Coo.Moo3), and the like. In the present invention, a metal selected from the group consisting of nickel, cobalt, molybdenum, tungsten, chromium, and vanadium, an oxide of the metal, or a double oxide of the metal can be supported on a carrier.
担体としてはアルミナ、シリカーアルミナ、シリカ、け
いそう土等をあげることができる。本発明において用い
る触媒の使用量は、有機物に対して0.1〜3の重量%
、好ましくは1〜1の重量%である。Examples of the carrier include alumina, silica alumina, silica, and diatomaceous earth. The amount of the catalyst used in the present invention is 0.1 to 3% by weight based on the organic matter.
, preferably from 1 to 1% by weight.
触媒が少なすぎると本発明の効果は期待できず、多すぎ
ても何らより以上の効果があげられるというものではな
く、単に無駄となるばかりか、必要に応じて行なわれる
触媒除去の際より多くの労力が必要となり好ましくない
。本発明の触媒を用いることにより等方性カーボンが得
られれる理由は厳密には明らかではないが、次のように
考えられる。If the catalyst is too small, the effect of the present invention cannot be expected, and if the catalyst is too large, no better effect can be achieved; it is not only wasted, but also more than necessary when removing the catalyst as necessary. This is not desirable as it requires a lot of effort. The reason why isotropic carbon can be obtained by using the catalyst of the present invention is not strictly clear, but it is thought to be as follows.
即ち、石炭系車質油、石油系重質油等を加熱してゆくと
分解、脱水、脱水素、環化、縮合、重合等の化学反応が
進行するが、本発明の触媒が存在しない通常の加熱では
これらの反応が比較的緩やかに進行する結果、反応系の
溶融状態が40000以上まで維持される。この場合、
各分子は系内を自由に移動することが可能で、その結果
、エネルギー的に最も安定な多環芳香核の平面が積層し
た構造ができやすく、これが異万性発現の主原因となっ
ていると思われる。しかるに、本発明の方法による場合
には、350qo以下で分解、脱水、脱水素、環化、縮
合、重合等の反応が急激に進行する結果、40000以
上の温度において溶融状態が現われず、各分子の動きが
束縛された状態となり、多環芳香核の平面が積層した構
造ができにくいので、等方性となるものと考えられる。
またこのようにして得られた等方性の固体状物質を、さ
らに250000以上の高温で、いわゆる黒鉛化しても
、結晶の成長や分子の配向がほとんど進行せず等万性は
保持され、本発明の等万性カーボンが得られる。本発明
の触媒のうちでは、ニッケル、コバルト、モリブデンか
らなる群から選ばれる金属又はその酸化物、又はこれら
の金属の複酸化物が本発明の効果が特に著しい。以下に
実施例をあげ本発明を具体的に説明するが本発明はこれ
らに制限されるものではない。That is, when coal-based car oil, petroleum-based heavy oil, etc. are heated, chemical reactions such as decomposition, dehydration, dehydrogenation, cyclization, condensation, and polymerization proceed. As a result of heating these reactions relatively slowly, the molten state of the reaction system is maintained up to 40,000 or more. in this case,
Each molecule can move freely within the system, and as a result, a structure in which planes of polycyclic aromatic nuclei, which are the most energetically stable, are stacked is likely to be formed, and this is the main cause of the manifestation of anisotropy. I think that the. However, in the case of the method of the present invention, reactions such as decomposition, dehydration, dehydrogenation, cyclization, condensation, and polymerization proceed rapidly at temperatures below 350 qo, and as a result, no molten state appears at temperatures above 40,000 qo, and each molecule It is thought that the structure becomes isotropic because the movement of the polycyclic aromatic nucleus is restricted and a structure in which the planes of polycyclic aromatic nuclei are stacked is difficult to form.
Furthermore, even if the isotropic solid material obtained in this way is further turned into so-called graphitization at a high temperature of 250,000 or higher, the isomerality is maintained with almost no progress in crystal growth or molecular orientation. The isomerogenic carbon of the invention is obtained. Among the catalysts of the present invention, metals selected from the group consisting of nickel, cobalt, and molybdenum, oxides thereof, or double oxides of these metals are particularly effective in the present invention. The present invention will be specifically explained below with reference to Examples, but the present invention is not limited thereto.
実施例 1ナフサタール100夕、酸化ニッケル3夕を
蝿枠機付きのフラスコに入れ300/minの昇温速度
で350ooまで、揮発分を系外に除去しながら加熱し
、350qoで1時間保持した。Example 1 100 qo of naphsatal and 3 qo of nickel oxide were placed in a flask equipped with a fly frame and heated at a heating rate of 300/min to 350 qo while removing volatile components from the system, and held at 350 qo for 1 hour.
次に得られたピッチ状物質を200の‘のステンレス製
容器に入れて3℃/minの昇温速度にて窒素雰囲気下
で600こ0まで揮発分を除去しながら加熱し600q
Cで2時間保持した。Next, the obtained pitch-like material was placed in a 200 ml stainless steel container and heated at a heating rate of 3°C/min under a nitrogen atmosphere to 600 ml while removing volatile matter.
It was held at C for 2 hours.
次いで得られた炭化物を2700qo′で黒鉛化したも
ののX線回折測定によればLc=20A、C。Then, the obtained carbide was graphitized at 2700 qo', and according to X-ray diffraction measurement, Lc=20A,C.
!6.80Aであり、等方性にすぐれたカーボンが得ら
れた。比較例 1
酸化ニッケルを使用しなかった以外は実施例1と同様の
方法で加熱し、黒鉛化して得たカーボンのX線回折測定
によればLc=630A、C。! 6.80A, and carbon with excellent isotropy was obtained. Comparative Example 1 According to X-ray diffraction measurement of carbon obtained by heating and graphitizing in the same manner as in Example 1 except that nickel oxide was not used, Lc = 630A, C.
=6.75Aであった。実施例 2原油原圧残油(アラ
ンビアンライト)100夕、酸化コバルト一酸化モリブ
デン複酸化物(Co/Mo=1/3:重量比)3夕を鷹
梓機付きのフラスコに入れ、3℃/minの昇温速度で
380午0まで揮発分を系外に除去しながら加熱し、斑
oooで1び分間保持した。=6.75A. Example 2 100 hours of crude oil residual oil (alambian light) and 3 hours of cobalt oxide and molybdenum monoxide double oxide (Co/Mo=1/3: weight ratio) were placed in a flask equipped with a hawker and heated at 3°C. The mixture was heated at a heating rate of /min until 380:00 pm while removing volatile matter from the system, and held for 1 minute at a temperature of ooo.
次に得られたピッチ状物質を200叫のステンレス製容
器に入れて300/minの昇温速度にて窒素雰囲気下
で600ooまで揮発分を除去しながら加熱し、600
ooで2時間保持した。Next, the obtained pitch-like substance was placed in a 200°C stainless steel container and heated at a heating rate of 300°/min to 600°C under a nitrogen atmosphere while removing volatile matter.
It was held at oo for 2 hours.
次いで得られた炭化物を270000で黒鉛化したもの
のX線回折測定によればLc=20A、C。Then, the obtained carbide was graphitized at 270,000° C. According to X-ray diffraction measurement, Lc=20A,C.
=6.81Aであり、等万性カーボンであることが確認
された。比較例 2
酸化コバルト・酸化モリブデン複酸化物を使用しなかっ
た以外は実施例2と同様の方法で加熱黒鉛化して得たカ
ーボンのX線回折測定によれば、LC:360A、C。= 6.81A, and it was confirmed that the carbon was isomerial carbon. Comparative Example 2 According to X-ray diffraction measurement of carbon obtained by thermal graphitization in the same manner as in Example 2 except that cobalt oxide/molybdenum oxide double oxide was not used, LC: 360A, C.
=6.74Aであった。実施例 3〜11原料童質油お
よび触媒を変え本発明を実施した。=6.74A. Examples 3 to 11 The present invention was carried out by changing the starting crude oil and catalyst.
その結果を表に示した。表 実施例 12〜14 原料車質油および触媒を変え本発明を実施した。The results are shown in the table. table Examples 12-14 The present invention was carried out by changing the raw material car oil and catalyst.
表table
Claims (1)
ンを製造する方法において、ニツケル、コバルト、モリ
ブデン、タングステン、クロムおよびバナジウムよりな
る群から選ばれる金属、該金属の酸化物または該金属の
複酸化物の1種または2種以上の存在下に、石炭系重質
油または石油重質油を加熱することを特徴とする方法。1. A method for producing isotropic carbon from coal-based heavy oil or petroleum-based heavy oil, in which a metal selected from the group consisting of nickel, cobalt, molybdenum, tungsten, chromium, and vanadium, an oxide of the metal, or the metal A method characterized by heating coal-based heavy oil or petroleum heavy oil in the presence of one or more types of double oxides.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52160676A JPS6024043B2 (en) | 1977-12-28 | 1977-12-28 | Method for producing isotropic carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52160676A JPS6024043B2 (en) | 1977-12-28 | 1977-12-28 | Method for producing isotropic carbon |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5492590A JPS5492590A (en) | 1979-07-21 |
| JPS6024043B2 true JPS6024043B2 (en) | 1985-06-11 |
Family
ID=15720054
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52160676A Expired JPS6024043B2 (en) | 1977-12-28 | 1977-12-28 | Method for producing isotropic carbon |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6024043B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0735250B2 (en) * | 1984-12-03 | 1995-04-19 | 三菱油化株式会社 | Method for producing carbon-based composite molded body |
-
1977
- 1977-12-28 JP JP52160676A patent/JPS6024043B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5492590A (en) | 1979-07-21 |
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