JPS61266398A - Method for manufacturing graphite whiskers - Google Patents
Method for manufacturing graphite whiskersInfo
- Publication number
- JPS61266398A JPS61266398A JP60104998A JP10499885A JPS61266398A JP S61266398 A JPS61266398 A JP S61266398A JP 60104998 A JP60104998 A JP 60104998A JP 10499885 A JP10499885 A JP 10499885A JP S61266398 A JPS61266398 A JP S61266398A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- treated
- whiskers
- activated carbon
- active 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.)
- Granted
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 98
- 229910002804 graphite Inorganic materials 0.000 title claims abstract description 21
- 239000010439 graphite Substances 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims description 18
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000002253 acid Substances 0.000 claims abstract description 38
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 17
- 239000011707 mineral Substances 0.000 claims abstract description 17
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 7
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 229910052799 carbon Inorganic materials 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 6
- 238000010908 decantation Methods 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 abstract description 2
- 238000003756 stirring Methods 0.000 abstract 1
- 235000011149 sulphuric acid Nutrition 0.000 abstract 1
- 239000013078 crystal Substances 0.000 description 18
- 235000010755 mineral Nutrition 0.000 description 11
- 239000002245 particle Substances 0.000 description 11
- 150000007513 acids Chemical class 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000003245 coal Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000003513 alkali Substances 0.000 description 5
- 230000000704 physical effect Effects 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 238000010306 acid treatment Methods 0.000 description 4
- 230000004913 activation Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000006229 carbon black Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 235000015241 bacon Nutrition 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910000734 martensite Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241000872198 Serjania polyphylla Species 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000001239 high-resolution electron microscopy Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 210000000936 intestine Anatomy 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000012916 structural analysis Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000004627 transmission electron microscopy Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C30—CRYSTAL GROWTH
- C30B—SINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
- C30B25/00—Single-crystal growth by chemical reaction of reactive gases, e.g. chemical vapour-deposition growth
- C30B25/005—Growth of whiskers or needles
-
- C—CHEMISTRY; METALLURGY
- C30—CRYSTAL GROWTH
- C30B—SINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
- C30B29/00—Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
- C30B29/02—Elements
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は活性炭をあらかじめ鉱酸で処理した後、約20
00℃以上で熱処理することにより、物性の優れた黒鉛
ホイスカーを製造する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is characterized in that activated carbon, after being previously treated with mineral acid, has a
The present invention relates to a method for producing graphite whiskers with excellent physical properties by heat treatment at 00°C or higher.
従来の技術と問題点
ホイスカーは繊維状単結晶であす1.理論物性に近い機
械的物性を持つことから、種々のホイスカーが製造され
ている。黒鉛ホイスカーについても、いくつかの方法が
提案されている。その代表的なものは高温、高圧下で黒
鉛電極をアーク放電させ析出させる方法である〔アール
・ベーコン(R。Conventional technology and problems Whiskers are fibrous single crystals1. A variety of whiskers are manufactured because they have mechanical properties close to theoretical properties. Several methods have also been proposed for graphite whiskers. A typical method is a method in which a graphite electrode is deposited by arc discharge under high temperature and pressure [R. Bacon (R.
Bacon )。ジャーナル・オブ・アプライド・フィ
ジックス(J、 App l i、 Phys)第31
巻、283ページ、1960年〕。この方法によって得
られたホイスカーの物性は、引張強度的2000kg
/ m” 、引張弾性率的72ton / am”とい
う非常に優れたものである。その他、β−3iC結晶の
(111)面の積層不整および回転双晶上にCOzガス
を熱分解させて析出させる方法〔エッチ・ビー・ハーン
ストラ(H,B、■aanstra)ら、ジャーナル・
オブ・クリスタル・グロース(J、 Cryst、 G
rowwth)、第16巻、71ページ、1972年〕
やマルテンサイトの電解析出により得られた無定形炭素
を2800℃で加熱処理して生成させる方法〔シェー・
ギo −(J、 G11lotl ら、カーポ・ン(
Carbon) 、第6巻、381ページ、1968年
〕がある。Bacon). Journal of Applied Physics (J, Appli, Phys) No. 31
Volume, 283 pages, 1960]. The physical properties of the whisker obtained by this method are as follows: tensile strength of 2000 kg
/m'' and tensile modulus of 72 tons/am''. In addition, there is a method of depositing COz gas by thermal decomposition on stacking misalignment and rotation twins of the (111) plane of β-3iC crystal [H, B, ■aanstra et al., Journal
Of Crystal Growth (J, Crystal, G
rowwth), Volume 16, Page 71, 1972]
A method of producing amorphous carbon obtained by electrolytic deposition of martensite and martensite by heat treatment at 2800°C [Shae et al.
Gio-(J, G11lotl et al., Kapo-N(
Carbon), Volume 6, Page 381, 1968].
しかし、これらの方法はいずれも生成操作が複雑である
ため、工業的製造法としては多くの難点を有している。However, since all of these methods require complicated production operations, they have many drawbacks as industrial production methods.
一方、工業的製造法として、約13i園以下の粒子径を
持つカーボンブラックを2000℃以上で熱処理するこ
とよにって、黒鉛ホイスカーを製造する方法がある(特
公昭57−8762号公報)。この方法は簡単な操作で
黒鉛ホイスカーを製造できる点は非常に優れた方法であ
るが、原料のカーボンブラックは約13n@以下の非常
に小さい粒子径のものを使用しなければならないことと
、このような小さい粒子径のカーボンブラックは必ずし
も安価ではない点に難点がある。On the other hand, as an industrial production method, there is a method of producing graphite whiskers by heat-treating carbon black having a particle size of about 13I or less at 2000° C. or higher (Japanese Patent Publication No. 8762/1987). This method is very good in that graphite whiskers can be produced with simple operations, but the raw material carbon black must have a very small particle size of about 13n@ or less, and this The drawback is that carbon black with such a small particle size is not necessarily inexpensive.
上記の点からみて、黒鉛ホイスカーを生成させる方法は
特公昭58−8762号公報記載の方法が工業的製造法
としては最も優れていると考えられるので、この方法を
採用し、その際、原料カーボンブラックに代わる炭素材
を検索した結果、微細細孔を有する炭素質物質(活性炭
)からも黒鉛ホイスカーを生成させ得ることが判明した
(特願昭6O−47752)。しかしながら、このホイ
スカーの大部分は下記のAに属する結晶構造であるなめ
、この構造から考えられる物性はBに属するものと比較
して必ずしも優れたものとはいえない。In view of the above points, the method described in Japanese Patent Publication No. 58-8762 is considered to be the best industrial manufacturing method for producing graphite whiskers. As a result of searching for a carbon material to replace black, it was found that graphite whiskers can also be produced from a carbonaceous material (activated carbon) having fine pores (Japanese Patent Application No. 6O-47752). However, since most of these whiskers have a crystal structure belonging to A below, the physical properties that can be considered from this structure are not necessarily superior to those belonging to B.
今まで知られている黒鉛ホイスカーの構造には大別して
、(A)黒鉛結晶のC軸がホイスカーの長軸方向と同方
向、(B)黒鉛結晶のC軸がホイスカーの長軸方向と垂
直方向、の2つがある。更に、(A)は(A −1)黒
鉛結晶のC軸がホイスカーの中心軸に対して約20℃傾
いて積層しているもの(cone −helix)、(
A−2)黒鉛結晶C軸がホイスカーの長軸方向に平行配
列し、積層しているもの(hezlgonal 1ay
er)があり、(B)は(B−1)帯状黒鉛結晶がラセ
ン状に巻きながら、連続的に積層しているもの(scr
oll 1ayer)、(B −2)帯状黒鉛結晶がホ
イスカーの中心に対して同心円状に巻いているもの(e
oneentric 5ireles)である@したが
って、物性的には已に属するもの、すなわち、R,Ba
conが得たものと同様の結晶構造を持つものが、実用
的価値を有すると考えられる。The structures of graphite whiskers known so far can be roughly divided into: (A) the C-axis of the graphite crystal is in the same direction as the long axis of the whisker; (B) the C-axis of the graphite crystal is in the direction perpendicular to the long axis of the whisker. There are two. Furthermore, (A) is (A-1) one in which the C axis of the graphite crystal is stacked at an angle of about 20°C with respect to the central axis of the whisker (cone-helix), (
A-2) The graphite crystal C-axis is arranged parallel to the long axis direction of the whisker, and the graphite crystals are stacked (hezlgonal 1ay
er), and (B) is (B-1) where band-shaped graphite crystals are wound in a spiral shape and continuously laminated (scr
oll 1ayer), (B-2) A band-shaped graphite crystal wound concentrically around the center of the whisker (e
oneentric 5ireles)@Therefore, in terms of physical properties, it belongs to 已, that is, R, Ba
A crystal structure similar to that obtained by con is considered to have practical value.
発明の目的
本発明は上記の点から、活性炭を高温で処理したとき、
生成するホイスカーはAに属する構造のものでなく、B
に属するホイスカーを生成させる必要があり、その方法
として、活性炭をあらかじめ鉱酸で処理すればよいこと
が判明したのでその方法を提供することを目的とする。Purpose of the Invention From the above points, the present invention provides that when activated carbon is treated at high temperature,
The generated whiskers are not of a structure belonging to A, but are of a structure belonging to B.
There is a need to generate whiskers belonging to the above group, and it has been found that activated carbon can be treated with a mineral acid in advance.
発明の構成
本発明は次の工程より成る。すなわち、■ 約5001
11″/g以上の比表面積を有する木質系、植物系、石
炭系の活性炭の選択。Structure of the Invention The present invention consists of the following steps. That is, ■ about 5001
Selection of wood-based, vegetable-based, or coal-based activated carbon with a specific surface area of 11″/g or more.
■ これらの活性炭の鉱酸による処理。■ Treatment of these activated carbons with mineral acids.
■ 約2000℃以上での熱処理。■ Heat treatment at approximately 2000℃ or higher.
これらの工程のうち、■の工程が本発明での主要な点で
ある。以下、これらの工程について詳細に記す。Among these steps, step (2) is the main point in the present invention. These steps will be described in detail below.
ホイスカーを生成させる原料である活性炭は約500m
” / 8以上の比表面積を持つことが必要である。こ
れ以下のものはホイスカーの生成量が少ないので原料と
して適当でない。また、賦活法は薬品賦活、ガス賦活の
いずれでもよいし、形状は粉末、粒状のいずれでもよい
。なお、ここでいう比表面積は液体窒素温度(77K)
での窒素ガス吸着による吸着等混線からBET式により
求めた値である。Approximately 500m of activated carbon is the raw material for producing whiskers.
” / It is necessary to have a specific surface area of 8 or more. If it is less than this, the amount of whiskers produced is small, so it is not suitable as a raw material. Also, the activation method may be either chemical activation or gas activation, and the shape can be changed. It may be in powder or granular form.The specific surface area here refers to liquid nitrogen temperature (77K).
This is the value determined by the BET equation from the adsorption equidistant line due to nitrogen gas adsorption at .
ついで、これらの活性炭を鉱酸で処理する。本発明の目
的に有効な鉱酸は塩酸、硫酸、硝酸あるいはこれらの混
酸である。リン酸は特に効果はなく、この酸で処理して
もAに属するホイスカーが生成する。なお、アルカリで
ある力性ソーダ水溶液やアンモニア水で処理することも
効果は認められず、Aに属するホイスカーが生成する。These activated carbons are then treated with mineral acids. Mineral acids useful for the purposes of this invention are hydrochloric acid, sulfuric acid, nitric acid, or mixed acids thereof. Phosphoric acid has no particular effect, and whiskers belonging to A are produced even when treated with this acid. Note that treatment with an aqueous solution of aqueous sodium hydroxide or aqueous ammonia, which are alkaline, has no effect, and whiskers belonging to A are generated.
これらの酸で処理する場合の条件は次の通りである。酸
の濃度は約05規定息上であればよい。また、混酸の場
合は各酸はいかなる割合のものでもよい。The conditions for treatment with these acids are as follows. The concentration of acid may be about 0.5N breath. Further, in the case of a mixed acid, each acid may be used in any proportion.
濃度比によって特に効果は変わらない。温度は室温(約
20℃)から100℃の範囲である。処理時間は約5分
以上である。処理はこれらの酸を活性炭が十分浸漬する
程度に加え、放置するか、あるいはわずかに攪拌する。The effect does not particularly change depending on the concentration ratio. Temperatures range from room temperature (approximately 20°C) to 100°C. Processing time is about 5 minutes or more. In the treatment, these acids are added to the extent that the activated carbon is fully immersed, and the mixture is left to stand or is slightly stirred.
ついで沙過、デカンテーシ讐ンによって酸を除去し、十
分、水洗、乾燥する。The acid is then removed by filtration and decantation, followed by thorough washing and drying.
酸を含んだままの活性炭を熱処理しても、その効果は変
わらないが、装置を腐食させることがあるので好ましく
ない。さらに重要なことは酸で処理した後、この酸を除
去する際のPRである。酸の除去操作として、通常■水
洗、■アルカリ水溶液による中和、が行われる。■の水
洗の場合はPHは7またはそれ以下となり、何ら支障は
ないが、■のアルカリ水溶液による場合はPHによって
生成するホイスカーの構造が異なる。すなわち、PI(
が7以下のときは第1図に示したのと同様なりに属する
ホイスカーとなるが、PRが7以上とした場合には第4
図に示したのと同様なAに属するホイスカーとなる。し
たがって、過剰のアルカリの使用は本発明の効果を失う
ことになる。なお、PI(7以上とした活性炭は再び鉱
酸で処理し、PHを7以下とすれば第1図に示したのと
同様のBに属するホイスカーが生成する。Even if activated carbon containing acid is heat-treated, the effect remains the same, but it is not preferable because it may corrode the equipment. What is more important is the PR when removing the acid after treatment with the acid. The acid removal operations usually include (1) washing with water and (2) neutralization with an aqueous alkali solution. In the case of (2) washing with water, the pH is 7 or lower and there is no problem; however, in the case of (2) using an aqueous alkaline solution, the structure of the whisker produced differs depending on the pH. That is, PI(
When PR is 7 or less, the whisker belongs to the same category as shown in Figure 1, but when PR is 7 or more, it belongs to the fourth whisker.
This results in a whisker belonging to A similar to that shown in the figure. Therefore, the use of excess alkali will lose the effectiveness of the present invention. Note that if the activated carbon with a PI of 7 or more is treated again with mineral acid to make the PH 7 or less, whiskers belonging to B, similar to those shown in FIG. 1, are generated.
鉱酸で処理した活性炭は約2000℃以上で、窒素、ア
ルゴン等の不活性ガス中で熱処理する。これらの温度で
の保持時間は約30分以上である。数時間という長時間
保持しても生成するホイスカーの生成量が顕著に増加す
る様子は認められない。2000℃以下ではホイスカー
の生成量は少なくなる。The activated carbon treated with a mineral acid is heat treated at about 2000° C. or higher in an inert gas such as nitrogen or argon. Hold times at these temperatures are about 30 minutes or more. Even after holding for a long period of time, such as several hours, no significant increase in the amount of whiskers produced was observed. At temperatures below 2000°C, the amount of whiskers produced decreases.
この熱処理によって、ホイスカーは活性炭粒子表面に綿
状に生成する。その様子を走査型電子顕微鏡(SEM)
で観察し、第1図に示した。この試料は実施例1にした
がって処理した活性炭を2800℃で処理したものであ
る。この図にみられるように、粒子表面に生成したホイ
スカーは大部分0.2μ−の直径で数10〜数100閣
の長さのものである。By this heat treatment, whiskers are generated in the form of fluff on the surface of the activated carbon particles. The situation was observed using a scanning electron microscope (SEM).
The results are shown in Figure 1. This sample was obtained by treating activated carbon treated according to Example 1 at 2800°C. As seen in this figure, most of the whiskers formed on the particle surface have a diameter of 0.2 .mu.m and a length of several tens to hundreds of degrees.
部分的に節状をなしているものもある。また、少量では
あるが、約5μmの最大直径を持つ長さ約10〜20μ
腸の“葉巻形”のものも存在する。高分解能電子顕微鏡
、マイクロラウェXs回折による構造解析から、前者は
帯状黒鉛結晶がラセン状に巻いた5croll 1ay
erあるいはeoneantrtc s+relesの
Bに属する構造であり、後者はAに属し、A−1のeo
ne−helixのタイプのものである。Some are partially nodular. In addition, although in small quantities, it has a length of about 10 to 20 μm with a maximum diameter of about 5 μm.
There are also "cigar-shaped" intestines. Structural analysis using high-resolution electron microscopy and microlawe Xs diffraction reveals that the former is a 5-croll 1-ay structure consisting of band-shaped graphite crystals wound in a helical shape.
The structure belongs to B of er or eoneantrtc s+reles, the latter belongs to A, and the eo of A-1
It is of the ne-helix type.
作用
活性炭をそのまま約2800℃で熱処理したときに生成
するホイスカーはAに属する構造のものであったが、こ
の活性炭をあらかじめ鉱酸で処理することにより、Bに
属するホイスカーが生成する。この構造の異なる本イス
カーが生成する理由については今の所、明確ではない。The whiskers produced when activated carbon is heat-treated as it is at about 2800°C have a structure belonging to A, but by treating this activated carbon with a mineral acid in advance, whiskers belonging to B are produced. At present, it is not clear why Iskar with this different structure is generated.
熱処理した活性炭をSEMで観察した場合、本発明では
粒子は綿状ホイスカーに覆われるため粒子表面を観察す
ることは出来ないが、活性炭をそのまま熱処理したもの
では観察可能である。この結果から、本イスカーは粒子
表面の特定の場所から数本の葉巻状ボイスカーが生成し
ており、ホイスカーの生成点のあることがわかる。本発
明の場合も同様に粒子表面の生成点からホイスカーが生
成すると仮定すれば、鉱酸で処理することによって、こ
の生成点の状態が変化し、そのため、生成するホイスカ
ーの結晶構造が変化したと推定される。When heat-treated activated carbon is observed with an SEM, in the present invention, the particle surface cannot be observed because the particles are covered with flocculent whiskers, but it is possible to observe the activated carbon that has been heat-treated as it is. From this result, it can be seen that several cigar-shaped voice cars are generated from specific locations on the particle surface of the present whisker, and there is a point where whiskers are generated. In the case of the present invention, assuming that whiskers are similarly generated from the generation point on the particle surface, it is assumed that the treatment with mineral acid changes the state of this generation point, and as a result, the crystal structure of the generated whisker changes. Presumed.
なお、一般に活性炭を製造する際、ガスあるいは薬品で
賦活後、酸処理を行うことは公知の事実である。したが
って、市販の活性炭はすでに酸処理されたものであると
みなされる。しかしながら、前述のように、Bに属する
ホイスカーを生成させるためには酸処理が必要である。It is a well-known fact that when activated carbon is produced, it is generally activated with gas or chemicals and then subjected to acid treatment. Therefore, commercially available activated carbon is considered to have already been acid-treated. However, as mentioned above, acid treatment is necessary to generate whiskers belonging to B.
この理由については7ページに記載したように、酸処理
後、その酸の中和のためにアルカリを使用しているため
と推定される。The reason for this is presumed to be that, as described on page 7, an alkali is used to neutralize the acid after the acid treatment.
実施例 1
77Kにおける窒素ガース吸着からBH3式で求めた比
表面積が986/ / g−クランストン−インクレイ
(CI)法による細孔分布から求めた平均細孔直径が1
. lnmである径2〜3閣の破砕状石炭系活性炭20
gを300−の3角フラスコに入れ、38%塩酸100
−を加えた後、30℃の恒温水槽中で5分間保持した。Example 1 The specific surface area determined by the BH3 formula from nitrogen girth adsorption at 77K is 986//g-The average pore diameter determined from the pore distribution by the Cranston-Inclay (CI) method is 1
.. Crushed coal-based activated carbon with a diameter of 2 to 3 nm, 20
Put 100 g of 38% hydrochloric acid into a 300-mL Erlenmeyer flask
After adding -, the mixture was kept in a constant temperature water bath at 30°C for 5 minutes.
ついで、直ちに11の水中に入れ、静置後、デカンテー
シ曹ンによって大部分の水を除き、残りに新たな水を加
え、加熱煮沸し、静置した浸水を除いた。この操作を3
回くり返した後ガラスフィルターでシ濾過した。このと
きの5p液のP旧よ6.3であった。シ濾過物を約1o
o℃で一夜乾燥して塩酸処理活性炭を得た。Then, it was immediately put into water in Step 11, and after being allowed to stand still, most of the water was removed using a decanting soda, fresh water was added to the remainder, and the water that had been left to stand was removed by heating and boiling. Perform this operation 3
After repeated rotations, the mixture was filtered through a glass filter. At this time, the P of the 5p solution was 6.3. Approximately 1 liter of filtered material
It was dried overnight at 0° C. to obtain hydrochloric acid-treated activated carbon.
塩酸処理活性次的5gを内径25m、深さ25腫のふた
付、黒鉛製ルツボに入れ、タンマン炉でアルゴン気流中
、平均昇温速度450℃/hrで2800℃まで加熱し
、この温度で30分間保持した。5 g of hydrochloric acid-treated active material was placed in a lidded graphite crucible with an inner diameter of 25 m and a depth of 25 m, and heated in a Tammann furnace in an argon stream at an average heating rate of 450°C/hr to 2800°C. Hold for minutes.
このようにして熱処理した活性炭の表面にはホイスカー
が綿状に生成しているのが認められた。It was observed that whiskers were formed in the form of fluff on the surface of the activated carbon heat-treated in this manner.
その様子を走査型電子顕微鏡(SEM)で観察し、第1
図に示す。第1図a)は低倍率で全体の様子を観察した
ものであり、同図b)は高倍率で綿状ホイスカーの様子
を観察したものである。この図にみられるように、直径
約0.2μ−のホイスカーが生成しているのがわかる。The situation was observed using a scanning electron microscope (SEM), and the first
As shown in the figure. Figure 1a) shows the overall appearance observed under low magnification, and Figure 1b) shows the appearance of the flocculent whiskers observed under high magnification. As seen in this figure, it can be seen that whiskers with a diameter of about 0.2 μm are generated.
このホイスカーは無数にからみ合っているため、一本の
長さを知ることは出来ないが、長いものは数(至)にお
よぶものも存在するようである。このホイスカーをxi
aマイクロアナライザーにより分析しh所、炭素で構成
されており、また、透過電子顕微鏡観察および電子線回
折による結晶構造解析を行った所、前述の黒鉛ホイスカ
ーの構造のうち、Bに属する構造のものであることがわ
かった。しかし、B−1、B−2の構造は同一の構造パ
ターンを与えるので、このいずれであるかはわからない
。Because these whiskers are intertwined in countless numbers, it is impossible to know the length of a single whisker, but it appears that there are several whiskers that are long. xi this whisker
As analyzed by a microanalyzer, h is composed of carbon, and crystal structure analysis by transmission electron microscopy and electron beam diffraction reveals that it has a structure belonging to B among the graphite whisker structures mentioned above. It turned out to be. However, since the structures B-1 and B-2 give the same structural pattern, it is not known which one it is.
なお、第1図中には直径が大きく、かつ短い葉巻状の形
状をしたものが認められる。このものの結晶構造はA−
1に属するものであるから、生成するホイスカーの全て
がBに属する結晶構造のものではない。In addition, in FIG. 1, a cigar-like shape with a large diameter and a short length can be seen. The crystal structure of this substance is A-
Therefore, not all of the generated whiskers have a crystal structure belonging to B.
上記と同様の活性炭を用いて種々の鉱酸で処理した後熱
処理した。その結果をまとめて第1表および第2,3図
に示す。The same activated carbon as above was treated with various mineral acids and then heat treated. The results are summarized in Table 1 and Figures 2 and 3.
第1表
これらの図から認められるように、細く、長いBに属す
るホイスカーが最も多量に生成するのは塩酸処理の場合
であることがわかる。他の酸の場合にはこのホイスカー
の他に葉巻状のものもかなり生成する。また、リン酸や
アルカリ処理では葉巻状のもののみ生成し、処理による
効果は認められない。As can be seen from these figures in Table 1, the largest amount of thin and long whiskers belonging to B is produced in the case of hydrochloric acid treatment. In the case of other acids, in addition to this whisker, a considerable amount of cigar-like material is also produced. Furthermore, when treated with phosphoric acid or alkali, only cigar-shaped particles are produced, and no effect of the treatment is observed.
比較例
実施例1と同様の活性炭を36%塩酸中、30℃5分間
処理した。これに1規定カセイソーダ水溶液を徐々に加
え中和し、最終的にPfullとした。これを37’遇
し、十分水洗後乾燥した。この活性炭をタンマン炉で2
800℃まで加熱し、この温度で30分間保持した。こ
の熱処理物をSEMで観察した所、第4図に示したよう
に、粒子表面に葉巻状のホイスカーが生成しており、わ
ずかに、直径0.2μ−の細く、長いホイスカーが認め
られた。この状況は未処理の活性炭を熱処理した場合と
ほとんど同様である。そこで、とのPH1まで処理した
活性炭を再び36%塩酸中、30℃、5分間処理し、十
分水洗した後、3p過、乾燥した。2過したときの3P
液のPHは6であった。これをタンマン炉で2800℃
、30分間熱処理した所、第1図に示したのと同様に已
に属するホイスカーが生成した。Comparative Example Activated carbon similar to Example 1 was treated in 36% hydrochloric acid at 30°C for 5 minutes. A 1N caustic soda aqueous solution was gradually added to the mixture to neutralize it, and finally it was made into Pfull. This was kept for 37 minutes, thoroughly washed with water, and then dried. This activated carbon is heated in a Tammann furnace for 2
It was heated to 800°C and held at this temperature for 30 minutes. When this heat-treated product was observed with a SEM, as shown in FIG. 4, cigar-shaped whiskers were formed on the particle surface, and a few thin and long whiskers with a diameter of 0.2 μm were observed. This situation is almost the same as when untreated activated carbon is heat treated. Therefore, the activated carbon treated to pH 1 was treated again in 36% hydrochloric acid at 30°C for 5 minutes, thoroughly washed with water, filtered through 3p, and dried. 3P after 2
The pH of the liquid was 6. This was heated to 2800℃ in a Tamman furnace.
When the sample was heat-treated for 30 minutes, whiskers similar to those shown in FIG. 1 were generated.
実施例 2
石炭系球状活性炭(水蒸気賦活、比表面積767’ /
g s平均細孔直径1. Onm)および木質系粉末
活性炭(塩化亜鉛賦活、比表面積1313m″/g、平
均細孔直径1.9nm) 20 gをそれぞれ300m
jの3角フラスコに採取し、これに36%塩酸100m
J加えた。Example 2 Coal-based spherical activated carbon (steam activation, specific surface area 767'/
g s Average pore diameter 1. Onm) and wood-based powder activated carbon (zinc chloride activated, specific surface area 1313 m''/g, average pore diameter 1.9 nm) 20 g each to 300 m
Collect the sample in an Erlenmeyer flask and add 100ml of 36% hydrochloric acid to it.
J added.
ついで、100℃に加熱した油浴中に入れ、60分間保
持した後、ガラスフィルター(No、4)で減圧シr過
した。5p過物は熱水等により洗浄し、炉液がPH6に
達するまで水洗し、約80℃で一昼夜減圧乾燥した。Then, the mixture was placed in an oil bath heated to 100° C., maintained for 60 minutes, and then filtered under reduced pressure through a glass filter (No. 4). The 5p filtered product was washed with hot water, etc. until the pH of the furnace solution reached 6, and then dried under reduced pressure at about 80° C. all day and night.
これらの塩酸処理活性炭を実施例1と同様にして、28
00℃、30分熱処理した。この処理物のホイスカーの
生成状態をSEMII察で調べた所、石炭系活性炭の場
合は第1図と類似で直径約0.2μmの長いものが多く
生成していたが、木質系活性炭の場合は第3図に類似′
で、直径約0.2μ■のものが大部分が短かく、かつそ
の量も多くない。更に葉巻状のものも生成していた。These hydrochloric acid-treated activated carbons were treated in the same manner as in Example 1, and 28
Heat treatment was performed at 00°C for 30 minutes. When we examined the state of whisker formation in this treated material using SEMII inspection, we found that in the case of coal-based activated carbon, many long whiskers with a diameter of about 0.2 μm were formed, similar to that shown in Figure 1, but in the case of wood-based activated carbon, Similar to Figure 3'
Most of them are short, with a diameter of about 0.2 μm, and their quantity is not large. Furthermore, cigar-shaped substances were also produced.
効果
本発明の方法によって得られるホイスカーの結晶構造は
Bに属するものである。これはR,Baconが得たホ
イスカーと同様の結晶構造を持つことから、同様の物性
を持つと考えられる。したがって、このホイスカーは例
えば複合材の原料として有用なものといえる。しかも、
原料として活性炭という比較的安価なものであり、かつ
、それを鉱酸で処理する簡単な操作を施すことによって
、安易に得られることば、工業的製造法として有益な方
法であろう。Effect The crystal structure of the whisker obtained by the method of the present invention belongs to B. Since this has the same crystal structure as the whisker obtained by R. Bacon, it is thought that it has similar physical properties. Therefore, this whisker can be said to be useful, for example, as a raw material for composite materials. Moreover,
The raw material is activated carbon, which is relatively inexpensive, and can be easily obtained by treating it with a mineral acid, making it a useful industrial manufacturing method.
第1図は塩酸処理した石炭系活性炭上に生成したホイス
カーの走査型電子顕微鏡写真であゆ、第1図a)は低倍
率で、同図b)は高倍率のものである。第2図は50%
硫酸処理、第3図は62%硝酸処理、第4図は塩酸処理
後アルカリ処理(PH11)した石炭系活性炭上に生成
したホイスカーの走査型電子顕微鏡写真である。Figure 1 is a scanning electron micrograph of whiskers formed on coal-based activated carbon treated with hydrochloric acid. Figure 1 a) is a low magnification, and Figure 1 b) is a high magnification. Figure 2 is 50%
These are scanning electron micrographs of whiskers formed on coal-based activated carbon treated with sulfuric acid, Figure 3 treated with 62% nitric acid, and Figure 4 treated with hydrochloric acid followed by alkali treatment (PH11).
Claims (3)
理した後、2000℃以上で熱処理することを特徴とす
る黒鉛ホイスカーの製造方法。(1) A method for producing graphite whiskers, which comprises treating activated carbon with a specific surface area of 500 m^2/g with a mineral acid and then heat-treating it at 2000°C or higher.
あることを特徴とする特許請求の範囲第1項記載の方法
。(2) The method according to claim 1, wherein the mineral acid is hydrochloric acid, sulfuric acid, nitric acid, or a mixed acid thereof.
、PHが7以下の状態で処理することを特徴とする特許
請求の範囲第1項記載の方法。(3) The method according to claim 1, wherein the activated carbon is treated with a mineral acid and then the mineral acid is removed at a pH of 7 or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60104998A JPS61266398A (en) | 1985-05-17 | 1985-05-17 | Method for manufacturing graphite whiskers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60104998A JPS61266398A (en) | 1985-05-17 | 1985-05-17 | Method for manufacturing graphite whiskers |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61266398A true JPS61266398A (en) | 1986-11-26 |
JPH031278B2 JPH031278B2 (en) | 1991-01-10 |
Family
ID=14395765
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60104998A Granted JPS61266398A (en) | 1985-05-17 | 1985-05-17 | Method for manufacturing graphite whiskers |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61266398A (en) |
-
1985
- 1985-05-17 JP JP60104998A patent/JPS61266398A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH031278B2 (en) | 1991-01-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6358878B1 (en) | Carbon fibril-forming metal catalysts | |
US7575733B2 (en) | Plasma-treated carbon fibrils and method of making same | |
DE60217566T2 (en) | Expanded carbon fibers and composites using same | |
JP2009040673A (en) | Method for manufacturing porous graphite carbon with high crystallinity and catalyst for fuel cell using the graphite carbon as carrier | |
DE102017215665A1 (en) | METHOD FOR CLEANING CARBON NANOTUBES | |
KR20180057323A (en) | Method of manufacturing metal-loaded TiO2/graphene composites through one-pot hydrothermal synthesis and the TiO2/graphene composites manufactured by the same | |
US3497318A (en) | Preparation of carbon textiles from polyacrylonitrile base textiles | |
DE69111953T2 (en) | Manufacture of reduced titanium oxide. | |
KR100497775B1 (en) | Catalyst for Process of Graphite Nanofibers And Process Thereof, Graphite Nanofibers And Process of Graphite Nanofibers | |
KR20210128176A (en) | Method for Preparing Graphene-Carbon Nanotube Composite | |
KR100813178B1 (en) | Hollow Graphite Nanocarbon Using Polymers Containing Metal Catalysts and Manufacturing Method Thereof | |
RU2221744C2 (en) | Method to produce metal-containing carbon nanostructures from organic compound with additives of inorganic salts | |
JPS61266398A (en) | Method for manufacturing graphite whiskers | |
KR100664751B1 (en) | Method for manufacturing titania nanotubes | |
CN111036254B (en) | A kind of preparation method of titanium dioxide, titanium carbide supported carbon fiber composite catalytic functional material | |
JPS62141126A (en) | Production of activated carbon fiber | |
US3488151A (en) | Preparation of carbon fibers from polyvinyl alcohol base fibers | |
JPS62246813A (en) | Production of spherical graphite body | |
JPH031277B2 (en) | ||
JPS61275118A (en) | Manufacturing method of graphite film | |
CN112794309B (en) | Preparation method of carbon nano tube based on silk template | |
JPH0476959B2 (en) | ||
Khan et al. | Catalytic nanocomposites for wastewater treatment | |
KR100550397B1 (en) | Method for producing aluminum hydroxide nanofibers by electrolysis | |
Jia et al. | Low-dimensional materials and applications |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
EXPY | Cancellation because of completion of term |