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JPS6158401B2 - - Google Patents
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JPS6158401B2 - - Google Patents

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Publication number
JPS6158401B2
JPS6158401B2 JP57046149A JP4614982A JPS6158401B2 JP S6158401 B2 JPS6158401 B2 JP S6158401B2 JP 57046149 A JP57046149 A JP 57046149A JP 4614982 A JP4614982 A JP 4614982A JP S6158401 B2 JPS6158401 B2 JP S6158401B2
Authority
JP
Japan
Prior art keywords
carbon
carbon material
metal
compound
heating
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
JP57046149A
Other languages
Japanese (ja)
Other versions
JPS58167413A (en
Inventor
Shigeharu Naka
Shinichi Hirano
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP57046149A priority Critical patent/JPS58167413A/en
Publication of JPS58167413A publication Critical patent/JPS58167413A/en
Publication of JPS6158401B2 publication Critical patent/JPS6158401B2/ja
Granted legal-status Critical Current

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  • Carbon And Carbon Compounds (AREA)
  • Catalysts (AREA)
  • Hard Magnetic Materials (AREA)
  • Developing Agents For Electrophotography (AREA)

Description

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

本発明は内部に金属又は金属化合物を均一に分
散したカーボン粒子から成るカーボン材料および
その製造法に関するものである。 金属又は金属酸化物とカーボン粉末との混合物
から成るカーボン材料は従来よりトナー、触媒等
に利用されている。この混合物より成るカーボン
材料は比重の小さいカーボン粉末に比重が大きな
鉄粉等の金属を混合するため均一に分散した混合
物を得ることができず、そのためこのような混合
物よりなるカーボン材料をトナーとして用いた場
合、均一な印刷が困難となる欠点があつた。また
カーボンブラツクに金属塩を混合して加熱分解し
カーボンブラツク表面に金属を析出させ触媒とし
て利用することも知られている。しかしながら、
このものは生成した金属が表面で凝集し易く又金
属が活性過ぎるため容易に酸化され触媒活性の低
下する欠点があつた。 本発明はこれらの欠点を解決するためになされ
たものであり、炭化可能な有機化合物と有機金属
化合物の混合物又は液状物を1〜3000Kg/cm2の圧
力下で350〜900℃に加圧加熱することにより内部
に金属又は金属化合物を均一に分散したカーボン
粒子からなるカーボン材料を始めて得たことに基
づくものである。 本発明の構成をさらに詳しく説明すると炭化可
能な有機化合物、すなわち加圧加熱により炭素を
生成するたとえばスチレン、アントラセン、ナフ
タリン、塩化ビニール等の易黒鉛化性有機化合
物、又はジビニルベンゼン、パラターフエニー
ル、ビフエニール、フエノールホルムアルデヒド
等の難黒鉛化性有機化合物のように重合可能なモ
ノマーよりなる炭化可能な有機化合物、具体的に
はスチレン、ジビニルベンゼン等のモノマーある
いは種類の異なつた炭化可能な有機化合物を2種
以上合わせた有機化合物を用い、これに有機金属
化合物、すなわち加圧加熱によつて揮散せず金属
元素を含む固形状の生成物を形成するFe,Co,
Ni,Pt,Rh等の遷移金属元素を含む重合可能な
モノマーより具体的にはビニルフエロセンモノマ
ー、ビニルニツケルセンモノマー、ビニルコバル
トセンモノマーあるいは金属元素が異なる有機金
属化合物の2種以上を組合わせたものを混合して
混合物を調製する。この場合、炭化可能な有機化
合物と有機金属化合物との配合割合は目的に応じ
て任意に選択できるものであるが、一般的にはモ
ル比で10:90〜99.9:0.1好ましくは50:50〜
90:1に混合する。 なお、炭化可能な有機化合物および有機金属化
合物がいずれも常温常圧下で固体である場合に
は、両者をトルエン、ベンゼン、キシレン等の溶
剤に均一に溶解した後、溶剤を除去して混合物と
し又一方が液状である場合には、他方をこれに溶
解して液状物とする。そして金属容器中にこれら
の混合物又は液状物を封入して1〜3000Kg/cm2
ましくは20〜2000Kg/cm2の圧力下で350〜900℃好
ましくは400〜800℃で1〜200分間程度加圧加熱
を行なう。 炭化可能な有機化合物および有機金属化合物が
いずれも重合可能なモノマーである場合には、そ
れらの混合物又は液状物を加圧加熱する前に共重
合して用いる方がより均質な生成物を得ることが
できるため好ましい。なお、加圧加熱する時の雰
囲気としてアルゴン、ヘリウム等の不活性ガス雰
囲気、CO,H2等の還元雰囲気又は窒素雰囲気の
いずれでもよい。 そして、加圧加熱することにより、稠密なカー
ボン粒子内部に金属又は金属化合物が均一に分散
したカーボン材料が得られ、生成するカーボン材
料の形態は、加圧加熱条件、有機金属化合物の割
合によつて変化し球状又はセン毛状あるいは個々
の粒子が連結することにより多面体状、多孔質状
となる。いずれの場合でも金属又は金属化合物が
カーボン粒子内部に20Å〜500Åの大きさで均一
に分散したカーボン材料が得られる。このカーボ
ン材料中のカーボン粒子内の金属化合物の種類
は、加圧加熱時の雰囲気、炭化可能な有機化合物
の種類により影響を受け、たとえば不活性ガス雰
囲気、還元ガス雰囲気下では一般に金属または金
属炭化物が生成するのに対し窒素雰囲気下では金
属元素の種類、加圧加熱条件により金属窒化物も
生成する。 また水の存在下で加圧加熱することにより水が
原料化合物の炭素−炭素結合の切断に作用し、熱
分解で生成する炭化水素の粘性と体積率を変化さ
せ炭化過程における炭素−炭素の結合状態に影響
を及ぼすためカーボンの形状制御が容易となる。
その場合、金属又は金属酸化物がカーボン粒子内
に生成する。また有機金属化合物としてビニルフ
エロセンを用いた場合、炭化可能な有機化合物が
ジビニルベンゼンでは加圧加熱によりセメンタイ
ト(Fe3C)が生成するのに対しスチレンではFe
金属が生成する。 カーボン粒子が球状の場合、そのカーボン粒子
の大きさは加圧加熱条件炭化可能な有機化合物の
種類、割合等により200Åから20μ程度までの範
囲内の粒径のものをつくることができる。そし
て、必要に応じて加圧加熱生成物を酸素含有雰囲
気中で300〜1000℃に1時間程度熱処理すること
により生成カーボンが酸素と反応してCOガスと
して揮散するため多孔質状のカーボン材料を得る
ことができる。たとえば、水の共存下で加圧加熱
して得られたマグネタイトが分散する球状カーボ
ン材料を酸素含有雰囲気中で800℃以下の温度で
熱処理すると、カーボン粒子表面から内部に連通
した開気孔を有する多孔質のマグネタイト含有カ
ーボン球状粒子を得ることができる。 なお、炭化可能な有機化合物と有機金属化合物
を加圧加熱することにより、カーボン粒子内に金
属又は金属化合物が均一に分散生成する理由は、
明確ではないが次のように考えられる。すなわ
ち、加圧加熱により原料化合物の分解、炭素−炭
素結合の生成、カーボン生成と反応が進行する
が、両者を同時に加圧加熱することにより、炭素
−炭素結合が有機化合物と有機金属化合物間に生
成し金属元素をとりこみながらカーボン化がおこ
つてゆくため、均一に分散した金属又は金属化合
物を含むカーボン粒子が生成するものと考えられ
る。 次に本発明の数値範囲の限定理由を述べれば、
加圧加熱時の圧力が1Kg/cm2より低い場合には、
得られるカーボン材料の収率が悪く、3000Kg/cm2
より高い圧力では圧力容器が大型となり高価なも
のとなるため経済的に不利で工業上好ましくな
い。また、300℃より低い温度では炭化が十分に
おこらず、又900℃以上では加熱装置が高価にな
る割には生成物の特性が大きく変化しないからで
ある。 次に本発明を実施例により説明する。 実施例 1 炭化可能な有機化合物としてジビニルベンゼン
又はスチレンと有機金属化合物としてモノビニル
フエロセン、モノビニルニツケルセン、又はモノ
ビニルコバルトセンとを第1表に示す割合で秤量
し、ベンゼンに溶解後ベンゼンを蒸発除去した
後、アルゴンガス中で金カプセルに封入し、水熱
合成装置を用いて1000Kg/cm2の圧力下で300℃に
加熱して2時間共重合を行つた。そして共重合体
を一旦カプセルよりとり出し、次いで第1表に記
載した雰囲気および加圧加熱条件のもとで再びカ
プセル中で加熱加圧を行つて本発明のカーボン材
料を得た。なお、比較例として、ジビニルベンゼ
ンと塩化鉄との混合物を加圧加熱してカーボン材
料を得た。そしてこれらのカーボン材料につい
て、生成炭素の形態、分散粒子の種類、大きさ分
散状態等を比較測定し、結果を第1表に示した。
なお、生成炭素の形態は走査型電子顕微鏡、分散
粒子の種類はX線回折装置、分散粒子の大きさ、
分散状態は電子顕微鏡を用いて観察測定を行つ
た。 そして、試料No.2についての電子顕微鏡写真を
第1図に、又第1図の球状カーボン材料の表面近
傍の電子顕微鏡写真を第2図に示す。第1表およ
び第2図から明らかなように、本発明の方法で得
られるカーボン材料は200Å以下の大きさの金属
又は金属化合物(第2図のAに相当する)がカー
ボン材料中に均一に分散しているのに対し比較例
で得られたものは金属鉄の粒子が1000Å以上の大
きさでカーボン粒子表面に不均一に凝集してい
た。
The present invention relates to a carbon material made of carbon particles in which a metal or a metal compound is uniformly dispersed, and a method for producing the same. Carbon materials made of a mixture of metal or metal oxide and carbon powder have conventionally been used in toners, catalysts, and the like. Carbon materials made of this mixture are made by mixing carbon powder with a low specific gravity with metals such as iron powder with a high specific gravity, so it is impossible to obtain a uniformly dispersed mixture. Therefore, carbon materials made of such a mixture cannot be used as toners. However, there was a drawback that uniform printing was difficult. It is also known that carbon black is mixed with a metal salt and then thermally decomposed to deposit the metal on the surface of the carbon black for use as a catalyst. however,
This method has the disadvantage that the metal produced tends to aggregate on the surface, and because the metal is too active, it is easily oxidized and the catalytic activity decreases. The present invention has been made to solve these drawbacks, and involves heating a mixture or liquid material of a carbonizable organic compound and an organometallic compound to 350 to 900°C under a pressure of 1 to 3000 kg/ cm2 . This is based on the fact that, for the first time, a carbon material consisting of carbon particles in which a metal or a metal compound is uniformly dispersed can be obtained. To explain the structure of the present invention in more detail, carbonizable organic compounds, such as easily graphitized organic compounds such as styrene, anthracene, naphthalene, and vinyl chloride, which produce carbon by pressure heating, or divinylbenzene and paraterphenyl Carbonizable organic compounds made of polymerizable monomers such as non-graphitizable organic compounds such as biphenyl and phenol formaldehyde, specifically monomers such as styrene and divinylbenzene, or different types of carbonizable organic compounds. A combination of two or more organic compounds is used to form an organometallic compound, that is, Fe, Co,
More specifically, combinations of two or more types of polymerizable monomers containing transition metal elements such as Ni, Pt, and Rh include vinyl ferrocene monomers, vinyl nickelsene monomers, vinyl cobalt cene monomers, or organometallic compounds containing different metal elements. Mix the ingredients together to prepare a mixture. In this case, the blending ratio of the carbonizable organic compound and the organometallic compound can be arbitrarily selected depending on the purpose, but generally the molar ratio is 10:90 to 99.9:0.1, preferably 50:50 to
Mix 90:1. In addition, if both the carbonizable organic compound and the organometallic compound are solid at room temperature and normal pressure, they can be dissolved uniformly in a solvent such as toluene, benzene, or xylene, and then the solvent can be removed to form a mixture. When one is liquid, the other is dissolved therein to form a liquid. Then, the mixture or liquid substance is sealed in a metal container and heated at 350 to 900°C, preferably 400 to 800°C, for about 1 to 200 minutes under a pressure of 1 to 3000 kg/ cm2 , preferably 20 to 2000 kg/cm2 . Perform pressure heating. If both the carbonizable organic compound and the organometallic compound are polymerizable monomers, a more homogeneous product can be obtained by copolymerizing the mixture or liquid material before pressurizing and heating. This is preferable because it allows for Note that the atmosphere during pressurization and heating may be any of an inert gas atmosphere such as argon and helium, a reducing atmosphere such as CO and H 2 , or a nitrogen atmosphere. Then, by pressurizing and heating, a carbon material in which metals or metal compounds are uniformly dispersed inside dense carbon particles is obtained, and the morphology of the produced carbon material depends on the pressurizing and heating conditions and the proportion of organometallic compounds. As the particles change, they change into spherical or hair-like shapes, or when individual particles are connected, they become polyhedral or porous. In either case, a carbon material can be obtained in which the metal or metal compound is uniformly dispersed within the carbon particles with a size of 20 Å to 500 Å. The type of metal compound in the carbon particles in this carbon material is influenced by the atmosphere during pressure heating and the type of organic compound that can be carbonized. For example, in an inert gas atmosphere or a reducing gas atmosphere, metal or metal carbide is generally formed. However, under a nitrogen atmosphere, metal nitrides may also be formed depending on the type of metal element and the pressure and heating conditions. In addition, by pressurizing and heating in the presence of water, water acts to break the carbon-carbon bonds of the raw material compound, changing the viscosity and volume fraction of the hydrocarbons produced by thermal decomposition, and changing the carbon-carbon bonds during the carbonization process. Since it affects the state, it becomes easy to control the shape of carbon.
In that case, metals or metal oxides are formed within the carbon particles. Furthermore, when vinylferrocene is used as an organometallic compound, the organic compound that can be carbonized is divinylbenzene, which produces cementite (Fe 3 C) when heated under pressure, whereas styrene produces cementite (Fe 3 C).
metal is produced. When the carbon particles are spherical, the size of the carbon particles can range from about 200 Å to about 20 μm depending on the type and proportion of organic compounds that can be carbonized under pressure and heating conditions. Then, if necessary, the pressurized and heated product is heat-treated at 300 to 1000°C for about 1 hour in an oxygen-containing atmosphere, so that the generated carbon reacts with oxygen and evaporates as CO gas, creating a porous carbon material. Obtainable. For example, when a spherical carbon material in which magnetite is dispersed, obtained by pressurizing and heating in the coexistence of water, is heat-treated at a temperature of 800°C or less in an oxygen-containing atmosphere, it becomes porous with open pores communicating from the carbon particle surface to the inside. High quality magnetite-containing carbon spherical particles can be obtained. The reason why metals or metal compounds are uniformly dispersed and generated within carbon particles by pressurizing and heating carbonizable organic compounds and organometallic compounds is as follows.
Although it is not clear, it can be considered as follows. In other words, the decomposition of the raw material compound, the formation of carbon-carbon bonds, and the formation of carbon occur due to pressurized heating, but by pressurizing and heating both at the same time, carbon-carbon bonds are formed between the organic compound and the organometallic compound. It is considered that carbon particles containing uniformly dispersed metals or metal compounds are generated because carbonization occurs while generating and incorporating metal elements. Next, the reason for limiting the numerical range of the present invention is as follows:
If the pressure during pressure heating is lower than 1Kg/ cm2 ,
The yield of the carbon material obtained was poor, 3000Kg/cm 2
Higher pressures make the pressure vessel larger and more expensive, which is economically disadvantageous and industrially unfavorable. Further, at temperatures lower than 300°C, carbonization does not occur sufficiently, and at temperatures above 900°C, the properties of the product do not change significantly, although the heating equipment becomes expensive. Next, the present invention will be explained by examples. Example 1 Divinylbenzene or styrene as a carbonizable organic compound and monovinylferrocene, monovinylnitkelsene, or monovinylcobaltocene as an organometallic compound are weighed in the proportions shown in Table 1, dissolved in benzene, and then the benzene is evaporated. After removal, it was sealed in a gold capsule in an argon gas atmosphere, and copolymerized for 2 hours by heating to 300° C. under a pressure of 1000 kg/cm 2 using a hydrothermal synthesizer. The copolymer was once taken out from the capsule, and then heated and pressurized again in the capsule under the atmosphere and pressure/heating conditions listed in Table 1 to obtain the carbon material of the present invention. As a comparative example, a carbon material was obtained by pressurizing and heating a mixture of divinylbenzene and iron chloride. The morphology of the carbon produced, the type of dispersed particles, the size and dispersion state, etc. of these carbon materials were compared and measured, and the results are shown in Table 1.
The form of the generated carbon was determined using a scanning electron microscope, the type of dispersed particles was determined using an X-ray diffraction device, the size of the dispersed particles,
The dispersion state was observed and measured using an electron microscope. FIG. 1 shows an electron micrograph of sample No. 2, and FIG. 2 shows an electron micrograph of the vicinity of the surface of the spherical carbon material in FIG. As is clear from Table 1 and Figure 2, the carbon material obtained by the method of the present invention has a metal or metal compound (corresponding to A in Figure 2) with a size of 200 Å or less uniformly contained in the carbon material. In contrast, in the comparative example, metallic iron particles had a size of 1000 Å or more and were nonuniformly aggregated on the carbon particle surface.

【表】 実施例 2 実施例1の試料No.7のカーボン材料の一部を
400℃の温度で2時間空気中で熱処理を行つた。
この熱処理により、10重量%の重量減少がみられ
た。そして熱処理前後のカーボン材料について走
査型電子顕微鏡により比較観察を行つた結果、カ
ーボン粒子の大きさはいずれも8μであり粒径の
変化はみられなかつたが熱処理を行つたものはカ
ーボン粒子表面に無数の気孔がみられ、多孔質球
状粒子となつているのが観察された。 この金属ニツケルを含有する多孔質球状粒子の
触媒性能を検討するため比較試料としてカーボン
のみから成る8μの大きさのカーボン粒子表面に
ニツケルを担持したものを用意し共に400℃にお
ける一酸化炭素および水素の混合ガスからメタン
への転化率を測定した結果、本発明の多孔質球状
カーボン粒子を用いたものは95%の転化率が得ら
れたのに対し比較試料を用いたものは約50%であ
つた。 以上述べたように本発明のカーボン材料は、炭
化可能な有機化合物と有機金属化合物とを加圧下
で加熱することにより、カーボン粒子内部に極め
て微細な金属又は金属化合物が均一に分散したも
のであり、又、所要の場合に熱処理をすることに
より、多孔質のカーボ材料も得ることができるも
のであり、得られるカーボン材料はトナー、触媒
又は磁性材料として利用できるものであつて産業
上極めて有用なカーボン材料およびその製造法で
ある。
[Table] Example 2 A part of the carbon material of sample No. 7 of Example 1 was
Heat treatment was carried out in air at a temperature of 400°C for 2 hours.
This heat treatment resulted in a weight reduction of 10% by weight. As a result of comparative observation using a scanning electron microscope of the carbon materials before and after heat treatment, the size of the carbon particles was 8μ in each case, and no change in particle size was observed. Numerous pores were observed, forming porous spherical particles. In order to examine the catalytic performance of this porous spherical particle containing the metal nickel, we prepared a comparative sample in which nickel was supported on the surface of 8μ carbon particles consisting only of carbon. As a result of measuring the conversion rate of the mixed gas into methane, it was found that the conversion rate using the porous spherical carbon particles of the present invention was 95%, while the conversion rate was approximately 50% using the comparative sample. It was hot. As described above, the carbon material of the present invention has extremely fine metals or metal compounds uniformly dispersed inside carbon particles by heating a carbonizable organic compound and an organometallic compound under pressure. In addition, by heat treatment if necessary, a porous carbon material can be obtained, and the obtained carbon material can be used as a toner, a catalyst, or a magnetic material, and is extremely useful industrially. A carbon material and its manufacturing method.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は実施例1試料No.2の本発明の鉄分散球
状カーボン材料の走査型電子顕微鏡写真、第2図
は第1図の本発明のカーボン材料の粒子表面近傍
を示す電子顕微鏡写真である。
Fig. 1 is a scanning electron micrograph of the iron-dispersed spherical carbon material of the present invention as Sample No. 2 of Example 1, and Fig. 2 is an electron micrograph showing the vicinity of the particle surface of the carbon material of the present invention of Fig. 1. be.

Claims (1)

【特許請求の範囲】 1 内部に金属又は金属化合物を均一に分散した
カーボン粒子から成ることを特徴とするカーボン
材料。 2 カーボン粒子が球状である特許請求の範囲第
1項記載のカーボン材料。 3 金属又は金属化合物の金属元素が遷移金属か
ら選ばれる少なくとも1つである特許請求の範囲
第1項又は第2項に記載のカーボン材料。 4 いずれも重合可能なモノマーよりなる炭化可
能な有機化合物と有機金属化合物の混合物又は液
状物を1〜3000Kg/cm2の圧力下で350〜900℃に加
圧加熱することを特徴とするカーボン材料の製造
法。 5 加圧加熱生成物を酸素含有雰囲気中で熱処理
を行う特許請求の範囲第4項記載のカーボン材料
の製造法。 6 炭化可能な有機化合物と有機金属化合物の混
合物又は液状物を加熱する前に共重合する特許請
求の範囲第4項記載のカーボン材料の製造法。 7 有機金属化合物の金属元素が遷移金属から選
ばれる少なくとも1つである特許請求の範囲第4
項、第5項又は第6項記載のカーボン材料の製造
法。 8 炭化可能な有機化合物がジビニルベンゼン又
はスチレンの少なくとも一つであり、有機金属化
合物がビニルフエロセンモノマーである特許請求
の範囲第6項又は第7項に記載のカーボン材料の
製造法。 9 加圧加熱を水の共存下で行なう特許請求の範
囲第4項乃至第8項のいずれかに記載のカーボン
材料の製造法。
[Claims] 1. A carbon material comprising carbon particles in which a metal or a metal compound is uniformly dispersed. 2. The carbon material according to claim 1, wherein the carbon particles are spherical. 3. The carbon material according to claim 1 or 2, wherein the metal element of the metal or metal compound is at least one selected from transition metals. 4. A carbon material characterized by heating a mixture or liquid material of a carbonizable organic compound and an organometallic compound, both of which are made of polymerizable monomers, to 350 to 900°C under a pressure of 1 to 3000 Kg/ cm2 . manufacturing method. 5. The method for producing a carbon material according to claim 4, wherein the pressurized and heated product is heat-treated in an oxygen-containing atmosphere. 6. The method for producing a carbon material according to claim 4, wherein the mixture or liquid material of a carbonizable organic compound and an organometallic compound is copolymerized before heating. 7 Claim 4, wherein the metal element of the organometallic compound is at least one selected from transition metals.
6. A method for producing a carbon material according to item 5, item 6, or item 6. 8. The method for producing a carbon material according to claim 6 or 7, wherein the carbonizable organic compound is at least one of divinylbenzene or styrene, and the organometallic compound is a vinylferrocene monomer. 9. The method for producing a carbon material according to any one of claims 4 to 8, wherein the pressurized heating is performed in the presence of water.
JP57046149A 1982-03-23 1982-03-23 Carbonaceous material and preparation thereof Granted JPS58167413A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57046149A JPS58167413A (en) 1982-03-23 1982-03-23 Carbonaceous material and preparation thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57046149A JPS58167413A (en) 1982-03-23 1982-03-23 Carbonaceous material and preparation thereof

Publications (2)

Publication Number Publication Date
JPS58167413A JPS58167413A (en) 1983-10-03
JPS6158401B2 true JPS6158401B2 (en) 1986-12-11

Family

ID=12738914

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57046149A Granted JPS58167413A (en) 1982-03-23 1982-03-23 Carbonaceous material and preparation thereof

Country Status (1)

Country Link
JP (1) JPS58167413A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH066483B2 (en) * 1984-11-26 1994-01-26 日本カ−ボン株式会社 Method for producing fine metal carbide particles
JP2669486B2 (en) * 1992-07-21 1997-10-27 工業技術院長 Method for producing ferromagnetic carbon
JP2725736B2 (en) * 1994-03-11 1998-03-11 工業技術院長 Method for producing ferromagnetic carbonaceous material
JP5861206B2 (en) * 2012-09-27 2016-02-16 独立行政法人国立高等専門学校機構 Method for producing carbonaceous composite
JP6891017B2 (en) * 2017-03-24 2021-06-18 日鉄ケミカル&マテリアル株式会社 Porous carbon material and its manufacturing method

Also Published As

Publication number Publication date
JPS58167413A (en) 1983-10-03

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