JPH0380087B2 - - Google Patents

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Publication number
JPH0380087B2
JPH0380087B2 JP58190092A JP19009283A JPH0380087B2 JP H0380087 B2 JPH0380087 B2 JP H0380087B2 JP 58190092 A JP58190092 A JP 58190092A JP 19009283 A JP19009283 A JP 19009283A JP H0380087 B2 JPH0380087 B2 JP H0380087B2
Authority
JP
Japan
Prior art keywords
slurry
dicarboxylic acid
unsaturated dicarboxylic
polymer
present
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 - Lifetime
Application number
JP58190092A
Other languages
Japanese (ja)
Other versions
JPS6082307A (en
Inventor
Tsunehisa Ueda
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.)
Zeon Corp
Original Assignee
Nippon Zeon 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 Nippon Zeon Co Ltd filed Critical Nippon Zeon Co Ltd
Priority to JP58190092A priority Critical patent/JPS6082307A/en
Publication of JPS6082307A publication Critical patent/JPS6082307A/en
Publication of JPH0380087B2 publication Critical patent/JPH0380087B2/ja
Granted legal-status Critical Current

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  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Description

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

本発明は陶磁器用泥漿の解膠剤に関し、さらに
詳しくは、流動性及び貯蔵安定性に優れた陶磁器
用泥漿の解膠剤に関する。 陶器、磁器、せつ器などの陶磁器は、天然の岩
石、土壌、鉱物や人工の結晶などの無機原料を適
宜配合し成形したのち高温に加熱して焼き固める
ことによつて製造される。かかる陶磁器の製造工
程は一般に坏土調製、成形、焼成の各工程から成
り、さらに坏土の調製については原料の調製及び
素地の調製に分けられる。 このうち、原料の調製工程では原料粘土を粗砕
機で粗砕きしたのち、水と混合し分散させること
によつて泥漿とし、これを静置するか一定の遅い
速度で流す間に粗粒子や比重の大きい不純物を除
去した後、脱水することにより粘土分の濃縮が行
われる。一方、素地の調製工程では配合する原料
を混合し、湿式微分砕法にて粉砕、混合を行い微
細で均一な素地を得た後、脱水して所望の濃度の
泥漿が調製される。 このような泥漿の調製工程では泥漿の減粘によ
る不純物除去の効果率、高濃度泥漿による脱水量
の減少による生産性、経済向上などのために従来
から種々の解膠剤が使用されており、また鋳込み
成形の場合には高濃度で成形性、排出性に優れた
泥漿が要求されるためにやはり解膠剤が使用され
ている。 かかる解膠剤の具体例として、従来からケイ酸
ソーダ、炭酸ソーダ、ポリリン酸塩、フミン酸、
タンニン酸などが知られている。しかしながらこ
れら公知の解膠剤は解膠性、貯蔵安定性の面で未
だ充分だとは云えず、特に流動性の優れた高濃度
泥漿を得るには必ずしも適切な解膠剤とほ云えな
かつた。 そこで本発明者らは従来技術のかかる欠点を改
良すべく鋭意検討を進めた結果、特定な重合体の
水溶性塩とポリリン酸塩との組合わせが陶磁器用
泥漿の解膠剤としてきわめて優れていることを見
い出し、本発明を完成するに到つた。 かくして本発明によれば、(a)α,β−不飽和ジ
カルボン酸系モノマーの重合体またはα,β−不
飽和ジカルボン酸系モノマーと非極性ビニル系モ
ノマーとの共重合体の水溶性塩と(b)ポリリン酸塩
とを有効成分として含有し、(a)/(b)の重量比が
(95/5)〜(50/50)であることを特徴とする
陶磁器用泥漿の解膠剤が提供される。 本発明で用いられるα,β−不飽和ジカルボン
酸系モノマーの重合体またはα,β−不飽和ジカ
ルボン酸系モノマーと非極性ビニル系モノマーと
の共重合体は通常、数平均分子量500〜100000、
好ましくは、1000〜50000を有するα,β−不飽
和ジカルボン酸系モノマーの重合体または該α,
β−不飽和ジカルボン酸系モノマーと共重合可能
な非極性ビニル系モノマーとの共重合体である。
共重合体中のα,β−不飽和ジカルボン酸系モノ
マーの比率は適宜選択しうるが、通常、10〜100
モル%、好ましくは20〜100モルもである。 ここで、α,β−不飽和ジカルボン酸系モノマ
ーとは、カルボキシル基または酸無水物基を有す
る不飽和ジカルボン酸化合物をさし、その具体例
のしては、マレイン酸、フマル酸、イタコン酸な
どのごときα,β−不飽和ジカルボン酸、無水マ
レイン酸、無水イタコン酸、無水シトラコン酸な
どのごときのα,β−不飽和ジカルボン酸無水物
などが例示される。 また、非極性ビニル系モノマーは前記α,β−
不飽和ジカルボン酸系モノマーとラジカル重合可
能なものであればいずれでもよく、その具体例と
して、例えばエチレン、プロピレン、ブテン、2
−メチル−ブテン−1、ペンテン、ヘキセン、オ
クテン、ジイソブチレン、デセン、シクロペンテ
ン、シクロヘキセン、スチレン、ビニルトルエ
ン、α−メチルスチレン、クマロン、インデン、
メチルビニルエーテルなどが挙げられる。 本発明で用いられる重合体はその製法によつて
制限されるものではないが、通常は常法に従つて
ラジカル重合により製造される。 本発明においては、前記重合体の水溶性塩とポ
リリン酸塩とが陶磁器用泥漿の解膠剤として用い
られる。該重合体の塩は重合体が水溶化しうる範
囲内で存在するカルボキシル基、または酸無水物
基の少なくとも一部を塩にしたものであればよ
く、なかでも50モル%以上が塩を形成しているも
のであることが好ましい。 かかる塩の具体的な例として、例えばナトリウ
ム、カリウム、マグネシウム、カルシウム、バリ
ウムなどのごときアルカリ金属、またはアルカリ
土類金属の塩、アンモニウム塩、アミノ塩などが
例示され、なかでも経済性の面からナトリウム塩
が、好ましく、また金属の存在が陶磁器の仕上り
に悪影響をおよぼす場合にはアンモニウム塩やア
ミン塩が賞用される。 これらの重合体塩の製法は格別制限されるもの
ではなく、モノマーを中和したのちに重合する方
法、α,β−不飽和ジカルボン酸の重合体を合成
した後に常法ち従つて塩基の存在下で中和する方
法のいずれを採用してもよい。 本発明で用いられるポリリン酸塩は、トリポリ
リン酸ソーダやピロリン酸ソーダのごとき線状結
合リン酸の塩である。(a)α,β−不飽和ジカルボ
ン酸系重合体の水溶性塩と(b)ポリリン酸塩との使
用比率は、(a)/(b)の重量比が(95/5)〜(50/
50)であり、好ましくは、(80/20)〜(60/40)
である。(a)/(b)の値が上記の範囲外では泥漿の粘
度が増大して好ましくない。 本発明の解膠剤は固形のものもあつて水溶液で
あつてもよいが、通像は取り扱いの容易さを考え
て固形分濃度10〜50重量%の水溶液の形で使用さ
れる。この際、本発明の効果を本質的に損わない
範囲内であれば、ケイ酸ソーダ、炭酸ソーダなど
のごとき他の解膠剤やその他の配合剤を適宜混合
して使用することもできる。 本発明における解膠剤の添加方法は何ら制限さ
れるものではなく、陶磁器原料に直接添加する方
法、混練水に添加する方法、泥漿に添加する方法
のいずれを採用してもよい、泥漿を調製するに当
つて用いられる解膠剤の割合は、陶磁器原料の種
類、粒径、粒度分布、泥漿濃度、他の解膠剤の有
無などの条件により必ずしも一様ではないが、泥
漿濃度40〜90重量%、とくに50〜80重量%の泥漿
を調製する場合には、固型分基準で陶磁器原料
100重量部当り解膠剤中のα,β−不飽和ジカル
ボン酸系重合体の水溶性塩の有効成分が通常0.01
〜5重量部、好ましくは0.03〜1重量部となるよ
うな割合である。 かくして本発明によれば、泥漿の粘度を大巾に
低下させ、流動性、貯蔵安定性に優れた泥漿を調
製することができ、他の解膠剤を用いる場合に比
較して高濃度化または低粘度化を可能にすること
ができる。 次に本発明を実施例によりさらに具体的に説明
する。なお、実施例で用いた重合体水溶液の性状
は第1表に示すとうりであり、試験方法は下記の
とうりである。また部及び%は断りのない限り重
量基準である。
The present invention relates to a deflocculant for ceramic slurry, and more particularly to a deflocculant for ceramic slurry having excellent fluidity and storage stability. Ceramics such as pottery, porcelain, and mortarware are manufactured by appropriately blending inorganic raw materials such as natural rocks, soil, minerals, and artificial crystals, shaping them, and then heating them to high temperatures and baking them. The manufacturing process of such ceramics generally consists of the steps of clay preparation, molding, and firing, and the clay preparation is further divided into raw material preparation and base preparation. In the raw material preparation process, the raw material clay is coarsely crushed using a crusher, then mixed with water and dispersed to form a slurry, which is left to stand or flowed at a constant slow speed to produce coarse particles and specific gravity. After removing large impurities, the clay content is concentrated by dehydration. On the other hand, in the matrix preparation step, the raw materials to be blended are mixed, pulverized and mixed using a wet micropulverization method to obtain a fine and uniform matrix, and then dehydrated to prepare a slurry with a desired concentration. In the slurry preparation process, various deflocculants have traditionally been used to improve the effectiveness of impurity removal by reducing the viscosity of the slurry, and to improve productivity and economy by reducing the amount of dewatering caused by high-concentration slurry. Furthermore, in the case of cast molding, a deflocculant is also used because a highly concentrated slurry with excellent moldability and dischargeability is required. Specific examples of such deflocculants include sodium silicate, soda carbonate, polyphosphates, humic acid,
Tannic acid is also known. However, these known deflocculants are not yet sufficient in terms of peptizing properties and storage stability, and are not necessarily suitable for obtaining highly concentrated slurries with particularly good fluidity. . Therefore, the present inventors conducted intensive studies to improve this drawback of the prior art and found that a combination of a water-soluble salt of a specific polymer and a polyphosphate is extremely effective as a deflocculant for ceramic slurry. The present invention was completed based on the discovery that the present invention exists. Thus, according to the present invention, (a) a water-soluble salt of a polymer of an α,β-unsaturated dicarboxylic acid monomer or a copolymer of an α,β-unsaturated dicarboxylic acid monomer and a nonpolar vinyl monomer; (b) A deflocculant for ceramic slurry, which contains polyphosphate as an active ingredient and has a weight ratio of (a)/(b) of (95/5) to (50/50). is provided. The polymer of α,β-unsaturated dicarboxylic acid monomer or the copolymer of α,β-unsaturated dicarboxylic acid monomer and nonpolar vinyl monomer used in the present invention usually has a number average molecular weight of 500 to 100,000,
Preferably, a polymer of α,β-unsaturated dicarboxylic acid monomer having a molecular weight of 1,000 to 50,000 or the α,
It is a copolymer of a β-unsaturated dicarboxylic acid monomer and a copolymerizable nonpolar vinyl monomer.
The ratio of α,β-unsaturated dicarboxylic acid monomer in the copolymer can be selected as appropriate, but is usually 10 to 100.
mol %, preferably even 20 to 100 mol. Here, the α,β-unsaturated dicarboxylic acid monomer refers to an unsaturated dicarboxylic acid compound having a carboxyl group or an acid anhydride group, and specific examples thereof include maleic acid, fumaric acid, and itaconic acid. Examples thereof include α,β-unsaturated dicarboxylic acid anhydrides such as maleic anhydride, itaconic anhydride, citraconic anhydride, and the like. In addition, the nonpolar vinyl monomer is the α,β-
Any material that can be radically polymerized with an unsaturated dicarboxylic acid monomer may be used, and specific examples thereof include ethylene, propylene, butene, 2
-Methyl-butene-1, pentene, hexene, octene, diisobutylene, decene, cyclopentene, cyclohexene, styrene, vinyltoluene, α-methylstyrene, coumaron, indene,
Examples include methyl vinyl ether. The polymer used in the present invention is not limited in its production method, but is usually produced by radical polymerization according to a conventional method. In the present invention, the water-soluble salt of the polymer and the polyphosphate are used as a deflocculant for ceramic slurry. The salt of the polymer may be one in which at least a portion of the carboxyl groups or acid anhydride groups present within the range that allows the polymer to be water-solubilized, and in particular, 50 mol% or more forms a salt. It is preferable that the Specific examples of such salts include salts of alkali metals such as sodium, potassium, magnesium, calcium, barium, etc., or alkaline earth metal salts, ammonium salts, and amino salts. Sodium salts are preferred, and ammonium and amine salts are preferred when the presence of metal adversely affects the finish of the ceramic. The methods for producing these polymer salts are not particularly limited, and include a method in which monomers are neutralized and then polymerized, and a method in which a polymer of α,β-unsaturated dicarboxylic acid is synthesized and then a conventional method is used. Any of the neutralization methods described below may be employed. The polyphosphates used in the present invention are salts of linearly bound phosphoric acids such as sodium tripolyphosphate and sodium pyrophosphate. The usage ratio of (a) water-soluble salt of α,β-unsaturated dicarboxylic acid polymer and (b) polyphosphate is such that the weight ratio of (a)/(b) is between (95/5) and (50 /
50), preferably (80/20) to (60/40)
It is. If the value of (a)/(b) is outside the above range, the viscosity of the slurry will increase, which is undesirable. The deflocculant of the present invention may be solid or may be in the form of an aqueous solution; however, for imaging purposes, it is used in the form of an aqueous solution with a solid content concentration of 10 to 50% by weight in view of ease of handling. At this time, other deflocculants such as sodium silicate, soda carbonate, and other compounding agents may be appropriately mixed and used as long as they do not essentially impair the effects of the present invention. The method of adding the deflocculant in the present invention is not limited in any way, and any of the following methods may be used: directly adding it to ceramic raw materials, adding it to kneading water, or adding it to slurry. The proportion of peptizer used in this process is not necessarily uniform depending on the type of ceramic raw material, particle size, particle size distribution, slurry concentration, presence or absence of other deflocculants, etc. When preparing a slurry of 50 to 80% by weight, ceramic raw materials on a solid content basis
The active ingredient of the water-soluble salt of the α,β-unsaturated dicarboxylic acid polymer in the peptizer is usually 0.01 per 100 parts by weight.
-5 parts by weight, preferably 0.03-1 parts by weight. Thus, according to the present invention, it is possible to significantly reduce the viscosity of the slurry, to prepare a slurry with excellent fluidity and storage stability, and to make the slurry more concentrated or more stable than when other deflocculants are used. It is possible to reduce the viscosity. Next, the present invention will be explained in more detail with reference to Examples. The properties of the aqueous polymer solutions used in the Examples are shown in Table 1, and the test methods are as follows. In addition, parts and percentages are based on weight unless otherwise specified.

【表】 試験方法 (1) 泥漿粘度:ブルツクフイールド粘度計によ
り、12rpm、25℃にて測定。 (2) 流動性:60mm径のガラスロートに泥漿を入
れ、50c.c.の泥漿が摘下するのに要する時間。5
分以内を〇、5〜8分を△、8分以上を×で表
示。 (3) 貯蔵安定性:泥漿を密封容器に入れ50℃の恒
温槽中に24時間放置後、その泥漿の粘度及び流
動性を測定。 参考例 1 軟質磁器用坏土を固型分濃度68%に調製したの
ち試料〜と各種解膠剤とそれぞれ単独に添加
し、泥漿解膠剤試験を行つた。結果を第2表に示
す。
[Table] Test method (1) Slime viscosity: Measured at 12 rpm and 25°C using a Bruckfield viscometer. (2) Fluidity: The time required for 50 c.c. of slurry to be extracted by pouring slurry into a 60 mm diameter glass funnel. 5
○ indicates within minutes, △ indicates 5 to 8 minutes, and × indicates 8 minutes or more. (3) Storage stability: After placing the slurry in a sealed container and leaving it in a constant temperature bath at 50℃ for 24 hours, the viscosity and fluidity of the slurry were measured. Reference Example 1 After preparing soft clay for porcelain to a solid content concentration of 68%, samples ~ and various deflocculants were added individually to conduct a slurry deflocculant test. The results are shown in Table 2.

【表】 参考例 2 硬質磁器用坏土を固型分濃度68%に調製したの
ち第1表の試料と各種解膠剤とをそれぞれ単独
に添加し、泥漿解膠剤試験を行つた。結果を第3
表に示す。
[Table] Reference Example 2 After preparing clay for hard porcelain to a solid content concentration of 68%, the samples shown in Table 1 and various deflocculants were individually added, and a slurry peptizer test was conducted. 3rd result
Shown in the table.

【表】 実施例1,2、比較例1〜3 トリポリリン酸ソーダと試料とを適宜併用し
て、参考例2と同様にして硬質磁器用坏土を固型
分濃度68%に調製したのち泥漿解膠剤試験を行つ
た。結果を第4表に示す。
[Table] Examples 1 and 2, Comparative Examples 1 to 3 Hard porcelain clay was prepared in the same manner as Reference Example 2 to a solid content concentration of 68% using appropriate combinations of sodium tripolyphosphate and samples, and then slurry was prepared. A peptizer test was conducted. The results are shown in Table 4.

【表】 第4表からα,β−不飽和ジカルボン酸系重合
体の水溶性塩とトリポリリン酸ソーダとを併用す
ることにより単独使用時より優れた解膠性を示す
ことがわかる。 参考例 3 せつ器用鉄分含有坏土を泥漿濃度58%に調製し
たのち試料と各種解膠剤とをそれぞれ単独に添
加し泥漿試験を行つた。結果は第5表に示す。
[Table] From Table 4, it can be seen that the combined use of a water-soluble salt of an α,β-unsaturated dicarboxylic acid polymer and sodium tripolyphosphate exhibits better peptizing properties than when used alone. Reference Example 3 After preparing iron-containing clay for mortarware to a slurry concentration of 58%, a slurry test was conducted by adding the sample and various deflocculants separately. The results are shown in Table 5.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 (a)α,β−不飽和ジカルボン酸系モノマーの
重合体またはα,β−不飽和ジカルボン酸系モノ
マーと非極性ビニル系モノマーとの共重合体の水
溶性塩と(b)ポリリン酸塩とを有効成分として含有
し、(a)/(b)の重量比が(95/5)〜(50/50)で
あることを特徴とする陶磁器用泥漿の解膠剤。
1 (a) Water-soluble salt of a polymer of α,β-unsaturated dicarboxylic acid monomer or copolymer of α,β-unsaturated dicarboxylic acid monomer and nonpolar vinyl monomer, and (b) polyphosphate A deflocculant for ceramic slurry, comprising as an active ingredient, the weight ratio of (a)/(b) being (95/5) to (50/50).
JP58190092A 1983-10-12 1983-10-12 Deflocculant of mud for pottery Granted JPS6082307A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58190092A JPS6082307A (en) 1983-10-12 1983-10-12 Deflocculant of mud for pottery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58190092A JPS6082307A (en) 1983-10-12 1983-10-12 Deflocculant of mud for pottery

Publications (2)

Publication Number Publication Date
JPS6082307A JPS6082307A (en) 1985-05-10
JPH0380087B2 true JPH0380087B2 (en) 1991-12-20

Family

ID=16252231

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58190092A Granted JPS6082307A (en) 1983-10-12 1983-10-12 Deflocculant of mud for pottery

Country Status (1)

Country Link
JP (1) JPS6082307A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5179170A (en) * 1989-04-17 1993-01-12 Kawasaki Steel Corporation Dispersant and cement admixture

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4879230A (en) * 1972-01-25 1973-10-24
JPS533407A (en) * 1976-06-30 1978-01-13 Nagoya Yukagaku Kogyo Kk Bodies for ceramics
JPS553850A (en) * 1978-06-23 1980-01-11 Dai Ichi Kogyo Seiyaku Co Ltd Dispersant for bentonite stabilizer liquor
JPS5689289A (en) * 1979-12-18 1981-07-20 Katsumi Mokeiten Kk Uniform illuminating room inner light unit

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4879230A (en) * 1972-01-25 1973-10-24
JPS533407A (en) * 1976-06-30 1978-01-13 Nagoya Yukagaku Kogyo Kk Bodies for ceramics
JPS553850A (en) * 1978-06-23 1980-01-11 Dai Ichi Kogyo Seiyaku Co Ltd Dispersant for bentonite stabilizer liquor
JPS5689289A (en) * 1979-12-18 1981-07-20 Katsumi Mokeiten Kk Uniform illuminating room inner light unit

Also Published As

Publication number Publication date
JPS6082307A (en) 1985-05-10

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