JPH052012A - Carrier for gas chromatography using aggregate of carbon fine particles and method for producing the same - Google Patents

Carrier for gas chromatography using aggregate of carbon fine particles and method for producing the same

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Publication number
JPH052012A
JPH052012A JP3181780A JP18178091A JPH052012A JP H052012 A JPH052012 A JP H052012A JP 3181780 A JP3181780 A JP 3181780A JP 18178091 A JP18178091 A JP 18178091A JP H052012 A JPH052012 A JP H052012A
Authority
JP
Japan
Prior art keywords
less
carbon
fine particle
carbonized
particle diameter
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
Application number
JP3181780A
Other languages
Japanese (ja)
Other versions
JP3006918B2 (en
Inventor
Hiroshi Ichikawa
宏 市川
Akira Yokoyama
昭 横山
Keiichi Hirata
恵一 平田
Hiroo Wada
啓男 和田
Kenzo Kodera
健三 小寺
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.)
Shinwa Chemical Industries Ltd
Nippon Carbon Co Ltd
Original Assignee
Shinwa Chemical Industries Ltd
Nippon Carbon Co Ltd
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Filing date
Publication date
Application filed by Shinwa Chemical Industries Ltd, Nippon Carbon Co Ltd filed Critical Shinwa Chemical Industries Ltd
Priority to JP3181780A priority Critical patent/JP3006918B2/en
Publication of JPH052012A publication Critical patent/JPH052012A/en
Application granted granted Critical
Publication of JP3006918B2 publication Critical patent/JP3006918B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

(57)【要約】 【構成】 不溶融熱硬化性樹脂の内から選ばれた微粒子
材料に、特定の粒子直径を有するカーボンブラック、フ
リーカーボンの内から選ばれた超微粒子材料を表面に付
着せしめたのち、加熱により炭化し得る液状熱硬化性樹
脂と、有機溶剤を加えスラリー状とし、これを乾燥して
成形、硬化、焼成炭化した後、粉砕、分級してなる嵩比
重が0.2〜0.5、窒素ガス吸着法による比表面積が
1.0m2/g以下でかつ表面に1μm〜20nmの高
さの複数の突起を有する炭素微粒子集合体を用いたガス
クロマトグラフィー用担体。 【効果】 吸着力が珪藻土系と同等以上で、かつ高沸点
成分の水溶液分析を始め広範な分析が可能で、しかも液
相の担持力がよく、全ての液相の濡れ性が向上する。
(57) [Summary] [Structure] An ultrafine particle material selected from carbon black having a specific particle diameter and free carbon is attached to the surface of a fine particle material selected from among non-melting thermosetting resins. After that, a liquid thermosetting resin that can be carbonized by heating and an organic solvent are added to form a slurry, which is dried, molded, cured, calcined and carbonized, and then pulverized and classified to have a bulk specific gravity of 0.2 to 0.5, a carrier for gas chromatography using a carbon fine particle aggregate having a specific surface area of 1.0 m 2 / g or less by a nitrogen gas adsorption method and having a plurality of protrusions having a height of 1 μm to 20 nm on the surface. [Effect] The adsorption power is equal to or higher than that of diatomaceous earth type, and a wide range of analysis including analysis of an aqueous solution of a high boiling point component is possible, and the liquid phase carrying ability is good, and the wettability of all liquid phases is improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、高沸点成分の水溶液分
析を始め広範な分析が可能で特に液相との濡れ性に優れ
液相担持力の大きい炭素微粒子集合体を用いたガスクロ
マトグラフィー用担体及びその製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is capable of performing a wide range of analyzes including analysis of aqueous solutions of high-boiling components, and particularly gas chromatography using a carbon fine particle aggregate having excellent wettability with a liquid phase and having a large liquid phase carrying ability. And a manufacturing method thereof.

【0002】[0002]

【従来の技術】従来より、ガスクロマトグラフィー用担
体(以下、ガスクロ用担体という)としては天然の珪藻
土を焼結し、酸およびシラン化剤で処理した担体が広く
使用されている。これは、珪藻土が液相担持力が大き
く、かつ吸着力が小さい性質を持つからである。
2. Description of the Related Art Conventionally, as a carrier for gas chromatography (hereinafter referred to as a carrier for gas chromatography), a carrier obtained by sintering natural diatomaceous earth and treating it with an acid and a silanizing agent has been widely used. This is because diatomaceous earth has a large liquid phase supporting force and a small adsorbing force.

【0003】しかし、この種のガスクロ用担体は、珪藻
土が天然物であるためロット間のバラツキが大きく、ま
た、水による加水分解を受け易いため新たな吸着点が発
現して著しい性能低下を起こすので、水を含む材料の分
析ができない等の欠点があった。
However, in this type of carrier for gas chromatography, since diatomaceous earth is a natural product, there is a large variation between lots, and since it is easily hydrolyzed by water, new adsorption points are developed and the performance is significantly reduced. Therefore, there is a defect that the material containing water cannot be analyzed.

【0004】そこで本発明者等は、先に吸着力が珪藻土
より更に低く、珪藻土と同等以上の分離性能を備えてお
り、バラツキが小さく、また、加水分解を受けることが
なく、水を含む試料の分析も良好にできる等の特徴を備
えたガスクロ用担体として「カーボンや熱硬化性樹脂の
微粒子を基材とし、嵩比重を0.2〜0.5、比表面積
を1m2/g以下に調節した炭素微粒子集合体からなる
担体」を提案した(特願平2−7684号)。
Therefore, the present inventors previously found that the sample containing water, which has a lower adsorptivity than that of diatomaceous earth and has a separation performance equal to or higher than that of diatomaceous earth, has a small variation, and is not hydrolyzed. As a carrier for gas chromatography, which has features such as being able to perform good analysis of "a fine particle of carbon or a thermosetting resin as a base material, a bulk specific gravity of 0.2 to 0.5 and a specific surface area of 1 m 2 / g or less. A carrier composed of an adjusted carbon fine particle aggregate "was proposed (Japanese Patent Application No. 2-7684).

【0005】[0005]

【発明が解決しようとする課題】しかしながら、この炭
素微粒子集合体からなる担体は、上述の如く珪藻土を上
回る性能を備えているが、それと同時に、分析に使用す
る液相の担持力が十分でなく、また、ポリエステル系液
相等の一部の液相との濡れ性が不十分という欠点があっ
た。そのため、全ての用途に用いられるガスクロ用担体
の開発が望まれていた。本発明は上記欠点を解決し、分
析に使用する液相の担持力がよく、全ての液相の濡れ性
が向上したガスクロ用担体を提供することを目的とす
る。
However, the carrier composed of the aggregate of carbon fine particles has the performance superior to that of diatomaceous earth as described above, but at the same time, the supporting ability of the liquid phase used for the analysis is not sufficient. Further, there is a defect that the wettability with a part of liquid phase such as polyester liquid phase is insufficient. Therefore, development of a carrier for gas chromatography that is used for all purposes has been desired. An object of the present invention is to solve the above-mentioned drawbacks and to provide a carrier for gas chromatography which has a good supporting ability for a liquid phase used for analysis and has improved wettability of all liquid phases.

【0006】[0006]

【課題を解決するための手段】そこで、本発明者らは上
記問題点を解決すべく鋭意研究を重ねた結果、前記炭素
微粒子集合体の欠点が生ずるのは、炭素微粒子集合体の
表面が平滑であることに起因することを見出し、その表
面に特定の超微粒子材料を被覆して表面をでこぼこにす
れば、液相担持力が1.5倍以上向上し、液相との濡れ
性が大幅に改善され、しかも、上記炭素微粒子集合体か
らなる担体の利点も継承していることを見い出し、本発
明を完成した。
The inventors of the present invention have conducted extensive studies to solve the above-mentioned problems, and as a result, the drawback of the carbon fine particle aggregate is that the surface of the carbon fine particle aggregate is smooth. However, if the surface is coated with a specific ultrafine particle material and the surface is roughened, the liquid phase carrying power is improved by 1.5 times or more, and the wettability with the liquid phase is significantly increased. It was found that the advantages of the carrier composed of the above-mentioned aggregate of carbon fine particles are inherited, and the present invention has been completed.

【0007】すなわち、本発明の要旨は、炭素粉、黒鉛
粉、加熱により炭化し得る粉末状又は球状の不溶融熱硬
化性樹脂の内から選ばれた粒子直径が100μm以下
で、かつ5μm以下の粒子の割合が20%以下の微粒子
材料を、該微粒子材料の粒子直径の1/100以下の粒
子直径を有するカーボンブラック、フリーカーボンの内
から選ばれた超微粒子材料と加熱により炭化し得る液状
熱硬化性樹脂とで被覆し、ついで成形、硬化、焼成炭化
した後、粉砕、分級してなる嵩比重が0.2〜0.5、
窒素ガス吸着法による比表面積が1.0m2/g以下
で、かつ表面に1μm〜20nmの高さの複数の突起を
有する炭素微粒子集合体を用いたガスクロ用担体であ
る。
That is, the gist of the present invention is that the particle diameter selected from carbon powder, graphite powder, and powdery or spherical non-melting thermosetting resin which can be carbonized by heating is 100 μm or less and 5 μm or less. Liquid heat capable of carbonizing a fine particle material having a particle ratio of 20% or less with an ultrafine particle material selected from carbon black having a particle diameter of 1/100 or less of the particle diameter of the fine particle material and free carbon by heating. A bulk specific gravity of 0.2 to 0.5 obtained by coating with a curable resin, followed by molding, curing, firing and carbonization, followed by pulverization and classification.
A carrier for gas chromatography using a carbon fine particle aggregate having a specific surface area of 1.0 m 2 / g or less by a nitrogen gas adsorption method and having a plurality of protrusions having a height of 1 μm to 20 nm on the surface.

【0008】さらに詳述すると、まず、炭素粉、黒鉛
粉、加熱により炭化し得る粉末状または球状の不溶融熱
硬化性樹脂の内から選ばれた粒子直径が100μm以下
でかつ5μm以下の割合が20%以下の微粒子材料10
0重量部に、該微粒子材料の粒子直径の1/100以下
の粒子直径を有するカーボンブラック、フリーカーボン
の内から選ばれた超微粒子材料0.1〜5重量部をメカ
ノケミカル法により微粒子材料の表面に付着せしめたの
ち、加熱により炭化し得る液状熱硬化性樹脂5〜50重
量部と、有機溶剤を少なくとも20重量部加えスラリー
状とするか、あるいは、上記微粒子材料100重量部
に、上記超微粒子材料0.1〜5重量部、上記液状熱硬
化性樹脂5〜50重量部、少なくとも20重量部の上記
有機溶剤とを加え混合してスラリー状とする。
More specifically, first, a particle diameter selected from carbon powder, graphite powder, and powdery or spherical non-melting thermosetting resin which can be carbonized by heating is 100 μm or less and 5 μm or less. 20% or less of particulate material 10
To 0 part by weight, 0.1 to 5 parts by weight of an ultrafine particle material selected from carbon black having a particle diameter of 1/100 or less of the particle diameter of the fine particle material and free carbon is added to the fine particle material by a mechanochemical method. After being adhered to the surface, 5 to 50 parts by weight of a liquid thermosetting resin which can be carbonized by heating and at least 20 parts by weight of an organic solvent are added to form a slurry, or 100 parts by weight of the fine particle material is added to 0.1 to 5 parts by weight of the particulate material, 5 to 50 parts by weight of the liquid thermosetting resin, and at least 20 parts by weight of the organic solvent are added and mixed to form a slurry.

【0009】このとき微粒子状材料として使用する炭素
粉、黒鉛粉は、石油系または石炭系のコークスを熱処理
して炭素質、または黒鉛質とし、これを砕粉したものが
好ましく、また加熱により炭化し得る粉末状または球状
の不溶融熱硬化性樹脂としては、例えば、フェノール、
変性フェノール等が挙げられる。
The carbon powder and graphite powder used as the particulate material at this time are preferably those obtained by heat-treating petroleum-based or coal-based coke to obtain carbonaceous or graphite, and crushing this, and carbonizing by heating. The powdery or spherical non-melting thermosetting resin that can be used is, for example, phenol,
Examples include modified phenol and the like.

【0010】この微粒子状材料の粒子径が100μmを
超えると、得られる炭素微粒子集合体の嵩比重が0.5
を超え、表面積が低下する。また5μm以下のものが2
0%を超えると、得られる炭素微粒子集合体の比表面積
が1m2/gを超え、吸着力が大きくなりすぎ、いずれ
の場合も分離能が低下するので好ましくない。
When the particle size of the fine particle material exceeds 100 μm, the bulk specific gravity of the obtained carbon fine particle aggregate is 0.5.
And the surface area decreases. Also, if the thickness is 5 μm or less, 2
If it exceeds 0%, the specific surface area of the obtained carbon fine particle aggregate exceeds 1 m 2 / g, the adsorptive power becomes too large, and in either case, the separability is lowered, which is not preferable.

【0011】微粒子状材料の表面に被覆する超微粒子状
材料は、カーボンブラック、フリーカーボン(ピッチ類
のキノリン不溶分)が好適でその粒子直径は、微粒子状
材料の直径の1/100以下のものを微粒子材料100
重量部に対し、0.1〜5重量部用いる。超微粒子材料
の粒子直径が、微粒子材料の粒子直径の1/100を超
えると得られるガスクロ用担体の液相への担持力や濡れ
性の改善効果はない。
The ultrafine particle material coated on the surface of the fine particle material is preferably carbon black or free carbon (quinoline insoluble matter of pitches), and the particle diameter is 1/100 or less of the diameter of the fine particle material. The particulate material 100
0.1 to 5 parts by weight is used with respect to parts by weight. When the particle diameter of the ultrafine particle material exceeds 1/100 of the particle diameter of the fine particle material, there is no effect of improving the carrying force and wettability of the carrier for gas chromatography obtained in the liquid phase.

【0012】超微粒子状材料を微粒子材料の表面に被覆
するには、ライカイ機等を用いるメカノケミカル法、あ
るいは超微粒子状材料を溶剤で希釈した液状熱硬化性樹
脂中に分散してそれを微粒子材料と混合して行なうこと
もできる。
To coat the surface of the fine particle material with the ultrafine particle material, a mechanochemical method using a Reiki machine, or by dispersing the ultrafine particle material in a liquid thermosetting resin diluted with a solvent, the fine particle material is dispersed. It can also be performed by mixing with the materials.

【0013】加熱により炭化しえる液状熱硬化性樹脂と
しては、例えば、フェノール、変性フェノール、フラ
ン、ユリア等が挙げられる。また、有機溶剤としては、
メタノール、エタノール、アセトン等が挙げられる。
Examples of the liquid thermosetting resin which can be carbonized by heating include phenol, modified phenol, furan and urea. Further, as the organic solvent,
Methanol, ethanol, acetone, etc. may be mentioned.

【0014】これらの配合量は、上記に示す範囲が好ま
しく、液状熱硬化性樹脂が下限未満では集合体の強度が
低下し、上限を超えると、集合体の嵩比重が0.5を超
え分離能が低下するので好ましくなく、また、超微粒子
材料が5重量部を超えると比表面積が1m2/gを超え
また0.1重量部未満では効果を呈さない。さらに有機
溶剤が少量となると、微粒子材料の液状熱硬化性樹脂の
被覆がかえって不均一になり集合体の強度低下の原因と
なる。
The blending amount of these is preferably in the range shown above, and when the liquid thermosetting resin is less than the lower limit, the strength of the aggregate decreases, and when it exceeds the upper limit, the bulk specific gravity of the aggregate exceeds 0.5 and separation occurs. If the ultrafine particle material exceeds 5 parts by weight, the specific surface area exceeds 1 m 2 / g and less than 0.1 parts by weight, no effect is exhibited. Furthermore, when the amount of the organic solvent is small, the coating of the liquid thermosetting resin of the fine particle material is rather non-uniform, which causes a decrease in the strength of the aggregate.

【0015】次いで、スラリー状になったものを乾燥し
て、溶剤を除去することにより、樹脂液が微粒子上に均
一にコーティングされる。このとき、樹脂が硬化しない
温度領域で減圧乾燥処理することが好ましい。
Then, the slurry is dried to remove the solvent, so that the resin liquid is uniformly coated on the fine particles. At this time, it is preferable to carry out the reduced pressure drying treatment in a temperature range where the resin is not cured.

【0016】次に、これを成形するが、成形方法はノズ
ルから押し出して棒状に成形する方法やモールド成形等
があるが、押出し成形が粉砕性の面で特に好ましい。こ
のように熱処理をする前に成形するのは、そのまま熱処
理すると得られる集合体が不均質になるからである。
Next, this is molded. As the molding method, there are a method of extruding from a nozzle and molding into a rod shape, a molding method, and the like, but extrusion molding is particularly preferable in terms of pulverizability. The reason why the molding is performed before the heat treatment is that the aggregate obtained by the heat treatment becomes heterogeneous.

【0017】次いで、成形したものを100〜200℃
で硬化し、さらに、1500〜3000℃で炭化焼成
し、これを粉砕した後、分級して、例えば100〜30
0μmの粒状の炭素質微粒子集合体を得る。得られた炭
素微粒子集合体は、5〜100μmの骨格微粒子が炭化
樹脂で結合された構造を有し、嵩比重が0.2〜0.
5、窒素ガス吸着法による比表面積が1.0m2/g以
下で、かつ、表面に1μm〜20nmの高さの複数の突
起を有するもので、ガスクロ用担体として好適に用いる
ことができる。
Then, the molded product is heated to 100 to 200 ° C.
And then carbonized at 1500 to 3000 ° C., crushed, and then classified to, for example, 100 to 30
A granular carbonaceous particle aggregate of 0 μm is obtained. The obtained carbon fine particle aggregate has a structure in which skeleton fine particles of 5 to 100 μm are bonded by a carbonized resin, and has a bulk specific gravity of 0.2 to 0.
5. It has a specific surface area of 1.0 m 2 / g or less according to the nitrogen gas adsorption method and has a plurality of protrusions with a height of 1 μm to 20 nm on the surface, and can be suitably used as a carrier for gas chromatography.

【0018】[0018]

【発明の効果】本発明の炭素微粉子集合体は嵩比重が
0.2〜0.5、と従来のものと比べて非常に小さいに
もかかわらず、吸着力が珪藻土系と同等以上の分離性能
を備え、ばらつきが小さく、また、加水分解を受けるこ
とがないので、水を含む試料の分析も良好にできる。さ
らに、本発明により得られた炭素微粒子集合体は、表面
に1μm〜20nmの高さの複数の突起を有するもの
で、ガスクロ用担体として、高沸点成分の水溶液分析を
始め広範な分析が可能で、しかも液相の担持力がよく、
全ての液相の濡れ性が向上したガスクロ用担体を提供す
ることができる。
EFFECTS OF THE INVENTION The carbon fine powder aggregate of the present invention has a bulk specific gravity of 0.2 to 0.5, which is very small as compared with the conventional one, but has an adsorption force equal to or higher than that of the diatomaceous earth type. Since it has performance, has little variation, and is not subject to hydrolysis, it is possible to analyze a sample containing water well. Furthermore, the carbon fine particle aggregate obtained by the present invention has a plurality of protrusions with a height of 1 μm to 20 nm on the surface, and can be used as a carrier for gas chromatography for a wide range of analysis including aqueous solution analysis of high boiling point components. In addition, it has a good liquid phase holding power,
It is possible to provide a carrier for gas chromatography having improved wettability of all liquid phases.

【0019】[0019]

【実施例】次に、実施例及び比較例を用いて本発明をさ
らに具体的に説明するが、本発明はこれに限定されるも
のでない。
EXAMPLES Next, the present invention will be described more specifically with reference to Examples and Comparative Examples, but the present invention is not limited thereto.

【0020】実施例1 粒子直径が30μmで、かつ5μm以下の粒子の割合が
5%の市販の不溶融フェノール樹脂500gに粒子直径
23nmの市販のカーボンブラックを5g加え、ライカ
イ機中で1時間処理するメカノケミカル法でフェノール
樹脂表面にカーボンブラックを付着した。
Example 1 5 g of commercially available carbon black having a particle diameter of 23 nm was added to 500 g of a commercially available unmelted phenol resin having a particle diameter of 30 μm and a ratio of particles having a particle diameter of 5 μm or less of 5%, and treated in a liquor machine for 1 hour. Carbon black was attached to the surface of the phenol resin by the mechanochemical method.

【0021】次いで、カーボンブラックが付着したフェ
ノール樹脂500gに市販のフェノール樹脂液100
g、更にメタノール300gを加えスラリー化した後、
減圧下で乾燥し、メタノールを除去した。
Next, a commercially available phenol resin liquid 100 was added to 500 g of the phenol resin to which carbon black was adhered.
g and further 300 g of methanol to make a slurry,
Dried under reduced pressure to remove methanol.

【0022】得られたフェノール樹脂コートフェノール
樹脂を孔径0.2mmφのノズルから押し出して棒状に
成形した後、150℃で2時間加熱して硬化させた後、
2000℃で焼成した。焼成物を破砕、分級し、80〜
100メッシュ(180〜150μm)に粒度を揃えた
炭素微粒子集合体を得た。
The obtained phenol resin-coated phenol resin was extruded from a nozzle having a hole diameter of 0.2 mmφ to form a rod shape, which was then heated at 150 ° C. for 2 hours to be cured,
It was baked at 2000 ° C. 80-
A carbon fine particle aggregate having a uniform particle size of 100 mesh (180 to 150 μm) was obtained.

【0023】この嵩比重は0.35であり、窒素ガス吸
着法による比表面積は0.7m2/gであった。また、
その表面を走査型電子顕微鏡で観察したところ、図1に
示すように表面に多数の突起を有しており、その高さは
1μm〜20μmと推定された。
The bulk specific gravity was 0.35, and the specific surface area measured by the nitrogen gas adsorption method was 0.7 m 2 / g. Also,
When the surface was observed with a scanning electron microscope, it had a large number of protrusions on the surface as shown in FIG. 1, and its height was estimated to be 1 μm to 20 μm.

【0024】次に、ポリエステル系液相であるAdva
nce−DS(信和化工(株)製)を5%担持し、これ
を充填剤として高級脂肪酸のエステルであるステアリン
酸メチルおよびオレイン酸メチルを分析した。そのガス
クロマトグラムを図2に示した。図2より、本発明品を
使用して、これらの高級脂肪酸メチルエステルを良好に
分離できることがわかる。
Next, Adva which is a polyester liquid phase
nce-DS (manufactured by Shinwa Kako Co., Ltd.) was loaded at 5%, and using this as a filler, methyl stearate and methyl oleate, which are esters of higher fatty acids, were analyzed. The gas chromatogram is shown in FIG. From FIG. 2, it can be seen that these higher fatty acid methyl esters can be satisfactorily separated by using the product of the present invention.

【0025】比較例1 カーボンブラックを付着しなかった外は、実施例1に準
じて炭素微粒子集合体を得た。この嵩比重は0.34で
あり、窒素ガス吸着法による比表面積は0.5m2/g
であった。また、その表面積を走査型顕微鏡で観察した
ところ、図3に示すように表面に突起は存在せず、表面
はガラス状を呈していた。
Comparative Example 1 An aggregate of carbon fine particles was obtained in the same manner as in Example 1 except that carbon black was not attached. The bulk specific gravity is 0.34, and the specific surface area by the nitrogen gas adsorption method is 0.5 m 2 / g.
Met. Further, when the surface area was observed with a scanning microscope, as shown in FIG. 3, there were no protrusions on the surface and the surface was glassy.

【0026】これに実施例1に準じてAdvance−
DSを5%担持し、ステアリン酸メチル、オレイン酸メ
チルを分析した。そのガスクロマトグラムを図4に示し
た。図4より、本充填剤ではステアリン酸メチルおよび
オレイン酸メチルを完全に分離することができなかっ
た。これは本比較例の炭素微粒子集合体のAdvanc
e−DSに対する濡れ性が悪いためであり、実施例1お
よび比較例1の比較から、本発明の方法で液相に対する
濡れ性を改善できることが明らかになった。
According to the first embodiment, Advance-
DS was carried by 5%, and methyl stearate and methyl oleate were analyzed. The gas chromatogram is shown in FIG. From FIG. 4, it was not possible to completely separate methyl stearate and methyl oleate with this filler. This is the Advance of the carbon fine particle aggregate of this comparative example.
This is because the wettability with respect to e-DS is poor, and comparison between Example 1 and Comparative Example 1 revealed that the method of the present invention can improve the wettability with respect to the liquid phase.

【0027】比較例2 カーボンブラックの量を50gにする以外は、実施例1
に準じて80〜100メッシュに粒度を揃えた炭素微粒
子集合体を得た。この嵩比重は0.32であり、窒素ガ
ス吸着法による比表面積は4.3m2/gであった。ま
た、走査型顕微鏡観察によると、実施例1と同様にその
表面は多数の突起を有していた。
Comparative Example 2 Example 1 except that the amount of carbon black was 50 g.
According to the above, a carbon fine particle aggregate having a uniform particle size of 80 to 100 mesh was obtained. The bulk specific gravity was 0.32, and the specific surface area measured by the nitrogen gas adsorption method was 4.3 m 2 / g. Further, according to the observation with a scanning microscope, the surface had a large number of protrusions as in Example 1.

【0028】これに実施例1に準じてAdvance−
DSを5%担持し、ステアリン酸メチルおよびオレイン
酸メチルを分析した。そのガスクロマトグラムを図5に
示した。図5より、本充填剤ではステアリン酸メチルと
オレイン酸メチルはほとんど分離できないことが明らか
になった。
According to the first embodiment, Advance-
5% of DS was carried and methyl stearate and methyl oleate were analyzed. The gas chromatogram is shown in FIG. From FIG. 5, it became clear that methyl stearate and methyl oleate could hardly be separated with this filler.

【0029】実施例2 実施例1で用いた市販のフェノール樹脂液100gにメ
タノール300g、更に粒子直径100nmのカーボン
ブラック10gを加え、ボールミルで2時間混合してカ
ーボンブラックの均一に分散したスラリーを得た。この
スラリーに10〜30μに粒度調整した黒鉛粉500g
を加え、充分混合してスラリー状とした後、減圧下で乾
燥した。
Example 2 300 g of methanol and 10 g of carbon black having a particle diameter of 100 nm were added to 100 g of the commercially available phenol resin solution used in Example 1 and mixed for 2 hours with a ball mill to obtain a slurry in which carbon black was uniformly dispersed. It was 500g of graphite powder with particle size adjusted to 10-30μ in this slurry
Was added and mixed thoroughly to form a slurry, and then dried under reduced pressure.

【0030】得られたフェノール樹脂コート黒鉛粉を実
施例1に準じて処理し、100〜120メッシュに粒度
を揃えた炭素微粒子集合体を得た。この嵩比重は0.3
5であり、窒素ガス吸着法による比表面積は0.5m2
/gであった。また、走査型電子顕微鏡の観察によると
その表面には多数の突起を有していた。
The obtained phenol resin-coated graphite powder was treated according to Example 1 to obtain an aggregate of carbon fine particles having a uniform particle size of 100 to 120 mesh. This bulk specific gravity is 0.3
5 and the specific surface area by the nitrogen gas adsorption method is 0.5 m 2
/ G. Further, according to the observation with a scanning electron microscope, the surface had many protrusions.

【0031】次にポリエチレングリコール系液相である
PEG−1000を40%担持し、これを充填剤として
水溶液中のメタノールおよびエタノールを分析した。そ
のガスクロマトグラムを図6に示した。図6より、本発
明品を使用してこれらの試料を良好に分析できることが
明らかになった。
Next, 40% of PEG-1000, which is a polyethylene glycol type liquid phase, was loaded, and using this as a filler, methanol and ethanol in the aqueous solution were analyzed. The gas chromatogram is shown in FIG. From FIG. 6, it became clear that these samples can be satisfactorily analyzed using the product of the present invention.

【0032】比較例3 カーボンブラックを加えない以外は、実施例2に準じて
100〜120メッシュに粒度を揃えた炭素微粒子集合
体を得た。この嵩比重は0.34であったが、窒素ガス
吸着法による比表面積は測定できないレベルであった。
また、走査型顕微鏡による観察では、その表面は比較例
1と同様にガラス状を呈していた。
Comparative Example 3 An aggregate of carbon fine particles having a uniform particle size of 100 to 120 mesh was obtained in the same manner as in Example 2 except that carbon black was not added. This bulk specific gravity was 0.34, but the specific surface area by the nitrogen gas adsorption method was at a level that could not be measured.
In addition, the surface thereof was glass-like as in Comparative Example 1 when observed with a scanning microscope.

【0033】次にPFG−1000を40%担持した
が、この充填剤は流動性がほとんどなく、カラムに充填
することができなかった。これは、本比較例の炭素微粒
子集合体の液相担持力が低いためであり、実施例2およ
び本比較例から、本発明の方法で液相担持力を大幅に改
善できることが明らかになった。
Next, 40% of PFG-1000 was carried, but this packing material had almost no fluidity and could not be packed in the column. This is because the liquid phase carrying ability of the carbon fine particle aggregate of this comparative example was low, and it was revealed from Example 2 and this comparative example that the liquid phase carrying ability can be greatly improved by the method of the present invention. .

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の炭素微粒子集合体の粒子構造を示す電
子顕微鏡写真。
FIG. 1 is an electron micrograph showing a particle structure of a carbon fine particle aggregate of the present invention.

【図2】本発明の炭素微粒子集合体を用いたガスクロマ
トグラム。
FIG. 2 is a gas chromatogram using the aggregate of carbon fine particles of the present invention.

【図3】比較例1により得た炭素微粒子集合体の粒子構
造を示す電子顕微鏡写真。
FIG. 3 is an electron micrograph showing the particle structure of a carbon fine particle aggregate obtained in Comparative Example 1.

【図4】比較例1の炭素微粒子集合体を用いたガスクロ
マトグラム。
FIG. 4 is a gas chromatogram using the carbon fine particle aggregate of Comparative Example 1.

【図5】比較例2の炭素微粒子集合体を用いたガスクロ
マトグラム。
FIG. 5 is a gas chromatogram using the carbon fine particle aggregate of Comparative Example 2.

【図6】実施例2の本発明の炭素微粒子集合体を用いた
ガスクロマトグラム。
FIG. 6 is a gas chromatogram using the carbon fine particle aggregate of the present invention in Example 2.

【符号の説明】[Explanation of symbols]

1 アセトン 2 ステアリン酸メチル 3 オレイン酸メチル 4 メタノール 5 エタノール 6 水 1 Acetone 2 Methyl stearate 3 Methyl oleate 4 methanol 5 ethanol 6 water

───────────────────────────────────────────────────── フロントページの続き (72)発明者 和田 啓男 京都府京都市伏見区景勝町50番地の2 信 和化工株式会社内 (72)発明者 小寺 健三 京都府京都市伏見区景勝町50番地の2 信 和化工株式会社内   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Hiroo Wada             2 Shin, 50, Kagekatsu-cho, Fushimi-ku, Kyoto-shi, Kyoto             Wakako Co., Ltd. (72) Inventor Kenzo Kodera             2 Shin, 50, Kagekatsu-cho, Fushimi-ku, Kyoto-shi, Kyoto             Wakako Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 炭素粉、黒鉛粉、加熱により炭化し得る
粉末状又は球状の不溶融熱硬化性樹脂の内から選ばれた
粒子直径が100μm以下で、かつ5μm以下の粒子の
割合が20%以下の微粒子材料を、該微粒子材料の粒子
直径の1/100以下の粒子直径を有するカーボンブラ
ック、フリーカーボンの内から選ばれた超微粒子材料と
加熱により炭化し得る液状熱硬化性樹脂とで被覆し、つ
いで成形、硬化、焼成炭化した後、粉砕、分級してなる
嵩比重が0.2〜0.5、窒素ガス吸着法による比表面
積が1.0m2/g以下でかつ表面に1μm〜20nm
の高さの複数の突起を有する炭素微粒子集合体を用いた
ガスクロマトグラフィー用担体。
1. A particle diameter selected from carbon powder, graphite powder, and powdery or spherical non-melting thermosetting resin that can be carbonized by heating is 100 μm or less, and the proportion of particles having a diameter of 5 μm or less is 20%. The following fine particle materials are coated with an ultrafine particle material selected from carbon black and free carbon having a particle diameter of 1/100 or less of the particle diameter of the fine particle material and a liquid thermosetting resin that can be carbonized by heating. Then, it is molded, cured, calcined and carbonized, and then pulverized and classified to have a bulk specific gravity of 0.2 to 0.5, a specific surface area by a nitrogen gas adsorption method of 1.0 m 2 / g or less and a surface of 1 μm to 20 nm
For use in gas chromatography using a carbon fine particle aggregate having a plurality of protrusions of the same height.
【請求項2】 炭素粉、黒鉛粉、加熱により炭化し得る
粉末状又は球状の不溶融熱硬化性樹脂の内から選ばれた
粒子直径が100μm以下で、かつ5μm以下の粒子の
割合が20%以下の微粒子材料100重量部に、該微粒
子材料の粒子直径の1/100以下の粒子直径を有する
カーボンブラック、フリーカーボンの内から選ばれた超
微粒子材料0.1〜5重量部をメカノケミカル法により
該微粒子材料の表面に付着せしめ、次いで加熱により炭
化し得る液状熱硬化性樹脂5〜50重量部と、少なくと
も20重量部の有機溶剤を加えてスラリー状とし、これ
を乾燥して成形、硬化、1500〜3000℃で焼成炭
化した後、粉砕、分級することを特徴とする嵩比重が
0.2〜0.5、窒素ガス吸着法による比表面積が1.
0m2/g以下でかつ表面に1μm〜20nmの高さの
多数の突起を有する炭素微粒子集合体を用いたガスクロ
マトグラフィー用担体の製造方法。
2. A particle diameter selected from carbon powder, graphite powder, and powdery or spherical non-melting thermosetting resin which can be carbonized by heating is 100 μm or less, and the proportion of particles of 5 μm or less is 20%. To 100 parts by weight of the following fine particle material, 0.1 to 5 parts by weight of an ultrafine particle material selected from carbon black having a particle diameter of 1/100 or less of the particle diameter of the fine particle material and free carbon is added by a mechanochemical method. And 5 to 50 parts by weight of a liquid thermosetting resin that can be carbonized by heating and at least 20 parts by weight of an organic solvent to form a slurry, which is dried and molded and cured. , Calcination and carbonization at 1500 to 3000 ° C., followed by pulverization and classification, the bulk specific gravity is 0.2 to 0.5, and the specific surface area by the nitrogen gas adsorption method is 1.
A method for producing a carrier for gas chromatography, which uses a carbon fine particle aggregate having 0 m 2 / g or less and a large number of protrusions having a height of 1 μm to 20 nm on the surface.
【請求項3】 炭素粉、黒鉛粉、加熱により炭化し得る
粉末状又は球状の不溶融熱硬化性樹脂の内から選ばれた
粒子直径が100μm以下で、かつ5μm以下の粒子の
割合が20%以下の微粒子材料100重量部に、該微粒
子材料の粒子直径の1/100以下の粒子直径を有する
カーボンブラック、フリーカーボンの内から選ばれた超
微粒子材料0.1〜5重量部と加熱により炭化し得る液
状熱硬化性樹脂5〜50重量部と、少なくとも20重量
部の有機溶剤とを加えてスラリー状とし、これを乾燥し
て成形、硬化、1500〜3000℃で焼成炭化した
後、粉砕、分級することを特徴とする嵩比重が0.2〜
0.5、窒素ガス吸着法による比表面積が1.0m2/
g以下で、かつ表面に1μm〜20nmの高さの多数の
突起を有する炭素微粒子集合体を用いたガスクロマトグ
ラフィー用担体の製造方法。
3. A particle diameter selected from carbon powder, graphite powder and powdery or spherical non-melting thermosetting resin capable of being carbonized by heating is 100 μm or less, and the proportion of particles having a diameter of 5 μm or less is 20%. 100 parts by weight of the following fine particle material is carbonized by heating with 0.1 to 5 parts by weight of an ultrafine particle material selected from carbon black having a particle diameter of 1/100 or less of the particle diameter of the fine particle material and free carbon. 5 to 50 parts by weight of a liquid thermosetting resin capable of being treated and at least 20 parts by weight of an organic solvent are added to form a slurry, which is dried, molded, cured, calcined and carbonized at 1500 to 3000 ° C., and then crushed, Bulk specific gravity characterized by classification is 0.2 to
0.5, specific surface area by nitrogen gas adsorption method of 1.0 m 2 /
A method for producing a carrier for gas chromatography using a carbon fine particle aggregate having a number of g or less and a large number of protrusions having a height of 1 μm to 20 nm on the surface.
JP3181780A 1991-06-26 1991-06-26 Carrier for gas chromatography using aggregated carbon particles and method for producing the same Expired - Lifetime JP3006918B2 (en)

Priority Applications (1)

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JP3181780A JP3006918B2 (en) 1991-06-26 1991-06-26 Carrier for gas chromatography using aggregated carbon particles and method for producing the same

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Application Number Priority Date Filing Date Title
JP3181780A JP3006918B2 (en) 1991-06-26 1991-06-26 Carrier for gas chromatography using aggregated carbon particles and method for producing the same

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Publication Number Publication Date
JPH052012A true JPH052012A (en) 1993-01-08
JP3006918B2 JP3006918B2 (en) 2000-02-07

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8256783B2 (en) 2007-06-22 2012-09-04 Radar Industries, Inc. Suspension system for a vehicle
US8620059B2 (en) 2007-12-13 2013-12-31 Fpinnovations Characterizing wood furnish by edge pixelated imaging

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8256783B2 (en) 2007-06-22 2012-09-04 Radar Industries, Inc. Suspension system for a vehicle
US8620059B2 (en) 2007-12-13 2013-12-31 Fpinnovations Characterizing wood furnish by edge pixelated imaging

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