JPH10236876A - Method for producing carbonaceous powder slurry - Google Patents

Method for producing carbonaceous powder slurry

Info

Publication number
JPH10236876A
JPH10236876A JP9060001A JP6000197A JPH10236876A JP H10236876 A JPH10236876 A JP H10236876A JP 9060001 A JP9060001 A JP 9060001A JP 6000197 A JP6000197 A JP 6000197A JP H10236876 A JPH10236876 A JP H10236876A
Authority
JP
Japan
Prior art keywords
carbonaceous powder
slurry
carbonaceous
dispersant
viscosity
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.)
Pending
Application number
JP9060001A
Other languages
Japanese (ja)
Inventor
Yoshinari Kato
吉成 加藤
Yoshio Hironaka
与志雄 廣中
Hidehiro Todaka
栄弘 戸高
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.)
Akechi Ceramics Co Ltd
Original Assignee
Akechi Ceramics Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Akechi Ceramics Co Ltd filed Critical Akechi Ceramics Co Ltd
Priority to JP9060001A priority Critical patent/JPH10236876A/en
Publication of JPH10236876A publication Critical patent/JPH10236876A/en
Pending legal-status Critical Current

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  • Colloid Chemistry (AREA)
  • Ceramic Products (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Compositions Of Oxide Ceramics (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Producing Shaped Articles From Materials (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Abstract

(57)【要約】 【目的】 少量の分散剤でより高濃度で低粘度の条件で
の炭素質粉末の水中での分散性を改良し、鋳込み成形体
の製造に適当な炭素質粉末のスラリーを製造するための
炭素質粉末の水系処理方法の提供を目的とする。 【構成】 炭素質粉末、又は及び有機物質に対し高分子
樹脂分散剤として、縮合ナフタレンスルホン酸アンモニ
ウム塩、スチレンアクリル酸共重合体、スチレンマレイ
ン酸共重合体のうち1種または2種以上を使用すること
を特徴としている。 【効果】 本発明の炭素質粉末の水系処理方法によれ
ば、低粘度で高濃度の炭素質スラリーを実現できる。ま
たこの炭素質スラリーを用いることにより、従来困難で
あった炭素材料の鋳込み成形が可能となった。
(57) [Abstract] [Objective] A slurry of a carbonaceous powder suitable for producing cast moldings by improving the dispersibility of carbonaceous powder in water under conditions of higher concentration and lower viscosity with a small amount of a dispersant. It is an object of the present invention to provide an aqueous treatment method of a carbonaceous powder for producing a carbonaceous powder. [Constitution] Use one or more of condensed naphthalenesulfonic acid ammonium salt, styrene acrylic acid copolymer, and styrene maleic acid copolymer as a polymer resin dispersant for carbonaceous powder or an organic substance. It is characterized by doing. According to the aqueous treatment method for carbonaceous powder of the present invention, a low-viscosity, high-concentration carbonaceous slurry can be realized. By using this carbonaceous slurry, it has become possible to cast a carbon material, which has been difficult in the past.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は炭素質粉末の水系処
理方法に関する。詳しくは炭素材料を製造するに当た
り、鋳込み成形用炭素質スラリーを得るに必要な炭素質
粉末の水系処理方法に関するものである。
[0001] The present invention relates to an aqueous treatment method for carbonaceous powder. More specifically, the present invention relates to an aqueous treatment method of carbonaceous powder necessary for obtaining a carbonaceous slurry for casting in producing a carbon material.

【0002】[0002]

【従来の技術】複雑形状を持つ炭素材料成形体を得るた
めには鋳込み成形は非常に有効な手段と考えられる。特
に加圧成形法や押出し成形法では製造できない形状の製
品でも成形できるので工業的に極めて有用な方法であ
る。
2. Description of the Related Art Casting is considered to be a very effective means to obtain a carbon material molded body having a complicated shape. In particular, it is an industrially extremely useful method because it can mold a product having a shape that cannot be produced by the pressure molding method or the extrusion molding method.

【0003】鋳込み成形に適したスラリーは最大の固体
含有量で最大の流動性を持ったものである。言い換えれ
ば必要最小限の水分量で低粘度のスラリーが要求され
る。またスラリーを得るために用いる分散剤は必要以上
に多すぎるとスラリーが凝集したり、焼成物に支障を及
ぼすため最小限に抑えなければならない。現在鋳込み成
形はセラミックスの分野で幅広く行われている。一般的
なセラミックスの鋳込み成形用のスラリーは水分10〜
30重量%、粘度500cp以下に調整される。
[0003] Slurries suitable for casting are those having the highest solids content and the highest fluidity. In other words, a low-viscosity slurry with a necessary minimum water content is required. If the amount of the dispersing agent used to obtain the slurry is too large, the slurry aggregates or hinders the fired product, so that it must be minimized. Currently, casting is widely performed in the field of ceramics. Slurries for casting ceramics generally have a water content of 10
It is adjusted to 30% by weight and the viscosity to 500 cp or less.

【0004】しかし炭素質粉末を水に分散させる場合に
おいては今まで上記水分、粘度を達成した例が無く、鋳
込み成形に適した炭素質粉末スラリーは得られなかっ
た。例えば炭素質粉末を水に分散させる用途としてカー
ボンブラックを水に分散させた顔料や原料の粒度分析が
あり、すでにポリカルボン酸アンモニウム塩やリノール
酸ソーダと言った分散剤によって水系処理がなされてい
るが、この場合は分散剤量が多く、または水分量が多い
ため鋳込み成形に適したスラリーは得られなかった。炭
素質粉末が水系において分散しない原因としては炭素質
粉末が疎水性で多孔質であるためと考えられるが、この
ように従来の水系処理方法では鋳込み成形に適したスラ
リーの処理が不可能であった。
However, in the case of dispersing carbonaceous powder in water, there has been no example of achieving the above-mentioned water content and viscosity, and a carbonaceous powder slurry suitable for casting was not obtained. For example, as a use for dispersing carbonaceous powder in water, there is a particle size analysis of pigments and raw materials in which carbon black is dispersed in water, and an aqueous treatment has already been performed with a dispersant such as ammonium polycarboxylate or sodium linoleate. However, in this case, a slurry suitable for casting was not obtained because of a large amount of the dispersant or a large amount of water. The reason why the carbonaceous powder does not disperse in the aqueous system is considered to be the fact that the carbonaceous powder is hydrophobic and porous. However, it is impossible to treat the slurry suitable for casting by the conventional aqueous treatment method. Was.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記推察に基
づき、少量の分散剤でより高濃度で低粘度の条件での炭
素質粉末の水中での分散性を改良し、鋳込み成形体の製
造に適当な炭素質粉末のスラリーを製造するための炭素
質粉末の水系処理方法の提供を目的とする。
SUMMARY OF THE INVENTION Based on the above presumption, the present invention is to improve the dispersibility of carbonaceous powder in water under a condition of higher concentration and lower viscosity with a small amount of dispersant, and to produce a cast molding. It is an object of the present invention to provide an aqueous treatment method for a carbonaceous powder for producing a slurry of a carbonaceous powder suitable for the method.

【0006】[0006]

【課題を解決するための手段】本発明者等は上記目的を
達成するために鋭意研究を重ねた結果、1種類もしくは
2種類以上の高分子分散剤を特定な量添加することによ
り良好な結果が得られることを見出し本発明を完成させ
るに至った。すなわち炭素質粉末の水系のスラリーを製
造するにあたり分散剤として、炭素質粉末100重量部
に対して縮合ナフタレンスルホン酸アンモニウム塩を1
〜5重量部、及び、又はスチレンアクリル酸共重合体を
0〜3重量部、及び、又はスチレンマレイン酸共重合体
を0〜3重量部添加することを特徴とする炭素質粉末ス
ラリーの製造方法である。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to achieve the above object, and as a result, it has been found that adding a specific amount of one or more polymer dispersants gives a good result. Were found, and the present invention was completed. That is, in producing an aqueous slurry of carbonaceous powder, 1 part by weight of condensed ammonium naphthalenesulfonate is used as a dispersant per 100 parts by weight of carbonaceous powder.
A method for producing a carbonaceous powder slurry, comprising adding 0 to 3 parts by weight of a styrene acrylic acid copolymer and / or 0 to 3 parts by weight of a styrene maleic acid copolymer. It is.

【0007】以下さらに詳しく本発明を説明する。本発
明においては分散剤として縮合ナフタレンスルホン酸ア
ンモニウム塩、スチレンアクリル酸共重合体、スチレン
マレイン酸共重合体を併用もしくは単独で用いる。この
うち縮合ナフタレンスルホン酸アンモニウム塩について
は、縮合ナフタレンスルホン酸塩であればアンモニウム
塩やナトリウム塩、またそれ以外の塩全てについて良好
な分散性を示すが成形後の焼成を考えた場合、ナトリウ
ム塩は不純物が残るために好ましくない。アンモニウム
塩の場合、炭化する温度域(800℃以上)でほとんど
揮発するため不純物が少なく好ましい。これらのナフタ
レンスルホン酸塩分散剤の添加量は炭素質粉末100重
量部に対して1〜5重量部が好適である。この範囲をは
ずれるとスラリー粘度が高くなり、鋳込み成形を行うこ
とができない。
Hereinafter, the present invention will be described in more detail. In the present invention, condensed ammonium naphthalenesulfonate, a styrene acrylic acid copolymer, and a styrene maleic acid copolymer are used in combination or alone as a dispersant. Among these, the ammonium salt of condensed naphthalene sulfonic acid, if it is a condensed naphthalene sulfonic acid salt, shows an excellent dispersibility for ammonium salts and sodium salts, and all other salts. Is not preferable because impurities remain. In the case of an ammonium salt, it is preferable that it contains few impurities because it is almost volatilized in a temperature range where carbonization occurs (800 ° C. or higher). The addition amount of these naphthalene sulfonate dispersants is preferably 1 to 5 parts by weight based on 100 parts by weight of the carbonaceous powder. If it is out of this range, the viscosity of the slurry becomes high, so that casting cannot be performed.

【0008】一方、スチレンマレイン酸共重合体として
は、スチレン/アクリル酸の共重合比が1以上であり、
重量平均分子量が5000〜15000のものが好適に
用いられる。これらの共重合体の添加量は炭素質粉末1
00重量部に対して0〜3重量部が好適である。この範
囲よりも多いと泡立ちが激しくなるため緻密な鋳込み成
形体が得られない。
On the other hand, the styrene / maleic acid copolymer has a styrene / acrylic acid copolymerization ratio of 1 or more,
Those having a weight average molecular weight of 5,000 to 15,000 are preferably used. The amount of addition of these copolymers was 1
0 to 3 parts by weight per 100 parts by weight is preferred. If the amount is more than this range, foaming becomes severe, so that a dense cast molded product cannot be obtained.

【0009】また、スチレンマレイン酸共重合体として
は、スチレン無水マレイン酸の共重合比が1〜3で、重
量平均分子量が1500〜3000のものが好ましい。
共重合体中の無水マレイン酸の一部又は全部がエステル
化したもの、またさらにこのエステル化されたマレイン
酸のナトリウム塩やアンモニウム塩も好ましい。しかし
先と同様に鋳込み成形体の焼成を考えた場合アンモニウ
ム塩の方が好ましい。これらの共重合体の添加量は炭素
質粉末100重量部に対して0〜3重量部が好適であ
る。この範囲よりも多いとスラリー粘度が高くなり鋳込
み成形に適したスラリーを得ることが出来ない。
The styrene-maleic acid copolymer preferably has a copolymerization ratio of styrene-maleic anhydride of 1 to 3 and a weight average molecular weight of 1500 to 3000.
Those obtained by esterifying a part or all of maleic anhydride in the copolymer, and furthermore, sodium or ammonium salts of the esterified maleic acid are also preferable. However, when sintering of the cast molded body is considered as described above, the ammonium salt is more preferable. The addition amount of these copolymers is preferably 0 to 3 parts by weight based on 100 parts by weight of the carbonaceous powder. If the amount is more than this range, the viscosity of the slurry increases, and a slurry suitable for casting cannot be obtained.

【0010】[0010]

【作用】本発明の炭素質粉末の水系処理方法によれば、
従来よりも高濃度で低粘度の炭素質スラリーを少ない分
散剤量で製造することが可能となった。またこの炭素質
スラリーを用いることにより炭素材料の鋳込み成形が可
能となった。
According to the method of the present invention for treating an aqueous carbonaceous powder,
It has become possible to produce a carbonaceous slurry having a higher concentration and a lower viscosity with a smaller amount of dispersant than before. Also, by using this carbonaceous slurry, casting of a carbon material has become possible.

【0011】[0011]

【実施例】以下、本発明の実施例を説明する。Embodiments of the present invention will be described below.

【0012】[0012]

【実施例1】5000ccポリエチレン製広口瓶をボー
ルミルポットとして用い、これに蒸留水2000g、玉
石としてジルコニア製ボール(φ=5mm)を2500
g、縮合ナフタレンスルホン酸アンモニウム塩分散剤の
40%水溶液(SAN NOPCO LIMITED社
製商品名ローマ PWA−40)を100g、スチレン
アクリル酸共重合体分散剤の34%水溶液(ジョンソン
(株)社製商品名ジョンクリル62)を12g入れボー
ルミルにてよく混合した。この後、石油系コークス
((株)中越黒鉛製商品名GL500、粒度500メッ
シュ)をボールミルにて混合しながら3260gになる
まで加えた。ボールミル混合時間は144時間とした。
得られた炭素粉末スラリーは水分37.3重量%、粘度
480cp、pH=4.0(10.8℃)であった。
Example 1 A 5000 cc polyethylene wide-mouthed bottle was used as a ball mill pot, and 2,000 g of distilled water was added thereto, and zirconia balls (φ = 5 mm) were used as cobblestones for 2500.
g, 100 g of a 40% aqueous solution of a condensed ammonium naphthalenesulfonate dispersant (manufactured by SAN NOPCO LIMITED), and 100 g of a 34% aqueous solution of a styrene-acrylic acid copolymer dispersant (manufactured by Johnson Corporation) 12 g of Joncryl 62) was well mixed in a ball mill. Thereafter, petroleum-based coke (trade name: GL500, manufactured by Chuetsu Graphite Co., Ltd., particle size: 500 mesh) was added to 3260 g while mixing with a ball mill. The ball mill mixing time was 144 hours.
The obtained carbon powder slurry had a water content of 37.3% by weight, a viscosity of 480 cp, and a pH of 4.0 (10.8 ° C.).

【0013】[0013]

【実施例2】縮合ナフタレンスルホン酸アンモニウム塩
分散剤(ローマ PWA−40)を66g、スチレンア
クリル酸共重合体分散剤(ジョンクリル62)を14
g、自己焼結性メソフェーズカーボン(大阪ガスケミカ
ル(株)製商品名メソカーボンマイクロビーズ)を50
00gとした以外は実施例1と同様にしてスラリーを作
成した。得られたメソフェーズカーボン粉末のスラリー
は水分28.3重量%、粘度320cp、pH=8.2
(10.8℃)であった。
Example 2 66 g of condensed naphthalenesulfonic acid ammonium salt dispersant (Rome PWA-40) and 14 parts of styrene acrylic acid copolymer dispersant (Johncryl 62) were used.
g, 50 parts of self-sintering mesophase carbon (trade name: mesocarbon microbeads manufactured by Osaka Gas Chemical Co., Ltd.)
A slurry was prepared in the same manner as in Example 1 except that the amount was set to 00 g. The slurry of the obtained mesophase carbon powder had a water content of 28.3% by weight, a viscosity of 320 cp, and a pH of 8.2.
(10.8 ° C.).

【0014】[0014]

【実施例3】縮合ナフタレンスルホン酸アンモニウム塩
分散剤(ローマ PWA−40)を44g、ピッチ粉末
(大阪ガスケミカル(株)製商品名CIKU)を460
0gとした以外は実施例1と同様にしてスラリーを作成
した。得られたピッチ粉末のスラリーは水分30.3重
量%、粘度380cp、pH=8.3(10.8℃)で
あった。
Example 3 44 g of condensed ammonium naphthalenesulfonate dispersant (Roma PWA-40) and 460 of pitch powder (trade name CIKU, manufactured by Osaka Gas Chemical Co., Ltd.)
A slurry was prepared in the same manner as in Example 1 except that the amount was 0 g. The resulting pitch powder slurry had a water content of 30.3% by weight, a viscosity of 380 cp, and a pH of 8.3 (10.8 ° C.).

【0015】[0015]

【実施例4】スチレンアクリル酸共重合体分散剤の代わ
りにスチレン無水マレイン酸共重合体分散剤(アーコケ
ミカル・アジア・パシフィック・リミテッド社製商品名
SMAレジン)を12gとした以外は実施例1と同様に
してスラリーを作製した。得られた炭素粉末のスラリー
は水分28.0重量%、粘度300cp、pH=5.2
(10.8℃)であった。
Example 4 Example 1 was repeated except that the styrene-acrylic acid copolymer dispersant was replaced by 12 g of a styrene-maleic anhydride copolymer dispersant (trade name: SMA resin, manufactured by Arco Chemical Asia Pacific Limited). A slurry was prepared in the same manner as described above. The slurry of the obtained carbon powder had a water content of 28.0% by weight, a viscosity of 300 cp, and a pH of 5.2.
(10.8 ° C.).

【0016】比較例1 分散剤としてポリカルボン酸アンモニウム塩分散剤を炭
素質粉末100重量部に対して0〜10重量%添加した
以外は実施例1と全く同様にしてスラリーを作った。得
られたスラリーの粘度は1000cpを越え、鋳込み成
形に適したスラリーを得ることが出来なかった。
Comparative Example 1 A slurry was prepared in exactly the same manner as in Example 1 except that a polycarboxylic acid ammonium salt dispersant was added as a dispersant in an amount of 0 to 10% by weight based on 100 parts by weight of the carbonaceous powder. The viscosity of the obtained slurry exceeded 1000 cp, and a slurry suitable for cast molding could not be obtained.

【0017】比較例2 分散剤としてリノール酸ソーダを炭素質粉末100重量
部に対して0〜10重量%添加した以外は実施例1と全
く同様にしてスラリーを作った。得られたスラリーの粘
度は1000cpをはるかに越え、鋳込み成形に適した
スラリーを得ることは出来なかった。
Comparative Example 2 A slurry was prepared in the same manner as in Example 1 except that sodium linoleate was added as a dispersant in an amount of 0 to 10% by weight based on 100 parts by weight of the carbonaceous powder. The viscosity of the obtained slurry far exceeded 1000 cp, and a slurry suitable for cast molding could not be obtained.

【0018】[0018]

【発明の効果】以上記述したように、本発明の炭素質粉
末の水系処理方法によれば、低粘度で高濃度の炭素質ス
ラリーを実現できる。またこの炭素質スラリーを用いる
ことにより、従来困難であった炭素材料の鋳込み成形が
可能となった。
As described above, according to the aqueous treatment method of carbonaceous powder of the present invention, a low-viscosity, high-concentration carbonaceous slurry can be realized. By using this carbonaceous slurry, it has become possible to cast a carbon material, which has been difficult in the past.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C01B 31/02 101 C01B 31/02 101Z C04B 35/622 C04B 35/00 D ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI C01B 31/02 101 C01B 31/02 101Z C04B 35/622 C04B 35/00 D

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 炭素質粉末、又は、及び有機物質に対し
高分子樹脂分散剤として、縮合ナフタレンスルホン酸ア
ンモニウム塩、スチレンアクリル酸共重合体、スチレン
マレイン酸共重合体のうち1種または2種類以上を使用
することを特徴とする炭素質粉末スラリーの製造方法。
1. One or two of condensed ammonium naphthalenesulfonate, styrene acrylic acid copolymer and styrene maleic acid copolymer as a polymer resin dispersant for a carbonaceous powder or an organic substance. A method for producing a carbonaceous powder slurry, comprising using the above.
【請求項2】 請求項1のスラリーを水分20〜40重
量%、粘度500cp以下に調製したことを特徴とする
鋳込み成形用の炭素質粉末スラリーの製造方法。
2. A method for producing a carbonaceous powder slurry for casting, wherein the slurry of claim 1 is adjusted to a water content of 20 to 40% by weight and a viscosity of 500 cp or less.
JP9060001A 1997-02-26 1997-02-26 Method for producing carbonaceous powder slurry Pending JPH10236876A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9060001A JPH10236876A (en) 1997-02-26 1997-02-26 Method for producing carbonaceous powder slurry

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9060001A JPH10236876A (en) 1997-02-26 1997-02-26 Method for producing carbonaceous powder slurry

Publications (1)

Publication Number Publication Date
JPH10236876A true JPH10236876A (en) 1998-09-08

Family

ID=13129443

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9060001A Pending JPH10236876A (en) 1997-02-26 1997-02-26 Method for producing carbonaceous powder slurry

Country Status (1)

Country Link
JP (1) JPH10236876A (en)

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