JPH0780975B2 - Method for producing α-methylstyrene copolymer for ceramic binder - Google Patents
Method for producing α-methylstyrene copolymer for ceramic binderInfo
- Publication number
- JPH0780975B2 JPH0780975B2 JP61078453A JP7845386A JPH0780975B2 JP H0780975 B2 JPH0780975 B2 JP H0780975B2 JP 61078453 A JP61078453 A JP 61078453A JP 7845386 A JP7845386 A JP 7845386A JP H0780975 B2 JPH0780975 B2 JP H0780975B2
- Authority
- JP
- Japan
- Prior art keywords
- methylstyrene
- producing
- weight
- ceramic binder
- copolymer
- 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
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- Graft Or Block Polymers (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compositions Of Oxide Ceramics (AREA)
- Polymerisation Methods In General (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、セラミックバインダー用として好適なα−メ
チルスチレン共重合体の製造方法に関する。詳しくは特
にドクターブレード法、カレンダー法によってフィルム
或はシート状のセラミック成形品を作る際に好適に用い
られるα−メチルスチレン共重合体の製造方法に関す
る。TECHNICAL FIELD The present invention relates to a method for producing an α-methylstyrene copolymer suitable as a ceramic binder. More specifically, it relates to a method for producing an α-methylstyrene copolymer which is preferably used when a film- or sheet-shaped ceramic molded article is produced by a doctor blade method or a calendar method.
[従来の技術] セラミック製品を製造する際に種々の成形法が知られて
いるが、比較的精密な構造体を製造する際には種々の有
機高分子化合物のバインダーを用いることが行われてい
る。バインダーとしては焼結前のセラミックの構造体の
成形が容易で、しかも構造体がある程度の強度を有し、
かつ焼結する際にバインダーがスムーズに分解飛散し、
焼結されたセラミック構造体中にバインダー及びその分
解物等が残存しないことが要請されており、この要請の
ため、従来、比較的熱分解性の良好なポリメタクリル酸
エステル系,ポリスチレン系の樹脂が広く用いられてい
る。[Prior Art] Various molding methods are known for manufacturing ceramic products, but binders of various organic polymer compounds are used for manufacturing relatively precise structures. There is. As a binder, it is easy to form a ceramic structure before sintering, and the structure has some strength,
In addition, the binder smoothly decomposes and scatters during sintering,
It is required that binders and decomposed products thereof do not remain in the sintered ceramic structure. For this reason, conventionally, polymethacrylic acid ester-based and polystyrene-based resins having relatively good thermal decomposability are required. Is widely used.
[発明が解決すべき問題点] ポリα−メチルスチレン系の樹脂は極めて熱分解性に優
れているが、比較的セラミック粉末とのなじみが不良で
あり、しかもポリα−メチルスチレン系の樹脂をバイン
ダーとして用いてセラミック構造体を作るとその構造体
はもろく、特にシート状、フィルム状のセラミック成形
品を作る際、成形物を巻取ることが不可能であるなどの
問題があった。[Problems to be Solved by the Invention] Poly-α-methylstyrene-based resins are extremely excellent in thermal decomposability, but they are relatively poor in compatibility with ceramic powder, and poly-α-methylstyrene-based resins are When a ceramic structure is made by using it as a binder, the structure is brittle, and there is a problem that it is impossible to wind the formed product, especially when making a sheet-shaped or film-shaped ceramic molded product.
上記問題を解決するためには、α−メチルスチレンとジ
アルキルアクリルアミド、アクリル酸、メタクリル酸な
どの極性基含有モノマー、さらにはブチルメタクリレー
ト或はブチルアクリレートなどのモノマーと共重合する
ことが考えられる。しかし、α−メチルスチレンは高重
合体を得るためにはアニオン重合を行う必要があるが、
通常の方法では上記極性基含有モノマー、ブチルメタク
リレート、ブチルアクリレートとは共重合体が得られな
いという問題があった。In order to solve the above problems, it is considered that α-methylstyrene is copolymerized with a polar group-containing monomer such as dialkyl acrylamide, acrylic acid or methacrylic acid, and further a monomer such as butyl methacrylate or butyl acrylate. However, α-methylstyrene needs to undergo anionic polymerization in order to obtain a high polymer,
The conventional method has a problem that a copolymer cannot be obtained with the above polar group-containing monomer, butyl methacrylate and butyl acrylate.
[問題を解決するための手段] 本発明者は、上記問題を解決する方法について鋭意検討
し、セラミックバインダー用に好適なα−メチルスチレ
ン共重合体を製造する方法を見い出し本発明を完成し
た。[Means for Solving the Problem] The present inventor diligently studied a method for solving the above problem, found a method for producing an α-methylstyrene copolymer suitable for a ceramic binder, and completed the present invention.
即ち、本発明に係るセラミックバインダー用α−メチル
スチレン共重合体の製造方法は、炭化水素溶剤の存在下
アニオン系重合開始剤を用いてα−メチルスチレンとα
−メチルスチレンに対して以下に示すモノマーの総和が
0.05重量比以下のN,N−ジアルキルアクリルアミドとア
クリル酸及び/又はメタクリル酸を共重合し、次いでα
−メチルスチレンの0.1重量比以上1.0重量比以下のブチ
ルメタクリレート及び/又はブチルアクリレートを添加
して重合反応を行うことを特徴とする。That is, the method for producing an α-methylstyrene copolymer for a ceramic binder according to the present invention uses α-methylstyrene and α using an anionic polymerization initiator in the presence of a hydrocarbon solvent.
-The sum of the monomers shown below for methylstyrene is
Copolymerizing N, N-dialkylacrylamide with acrylic acid and / or methacrylic acid in an amount of 0.05 weight ratio or less, and then α
It is characterized in that butyl methacrylate and / or butyl acrylate in an amount of 0.1% by weight or more and 1.0% by weight or less of methylstyrene is added to carry out the polymerization reaction.
本発明においてはα−メチルスチレンの一部をスチレン
或はその核置換誘導体に代替することが可能であり、そ
の比率は、α−メチルスチレンの30重量%未満とするの
が好ましく、それ以上では熱分解性が不良である。In the present invention, it is possible to replace a part of α-methylstyrene with styrene or a nuclear-substituted derivative thereof, and the ratio thereof is preferably less than 30% by weight of α-methylstyrene, and above that. Poor thermal decomposition.
本発明に用いられるN,N−ジアルキル(該アルキルは炭
素数1〜5の低級アルキル、好ましくはメチル、エチル
である。)アクリルアミドとアクリル酸及び/又はメタ
クリル酸はα−メチルスチレンの0.05重量比以下であ
り、好ましくは0.001〜0.03重量比である。0.05重量比
より多いとポリα−メチルスチレンのもつ易分解性の特
性が失われ好ましくなく、一方0.001重量比より少な過
ぎるとセラミックとのなじみの改良が不充分であり好ま
しくない。N, N-dialkyl used in the present invention (wherein the alkyl is lower alkyl having 1 to 5 carbon atoms, preferably methyl or ethyl). Acrylamide and acrylic acid and / or methacrylic acid are in a weight ratio of α-methylstyrene of 0.05. It is below, preferably 0.001 to 0.03 weight ratio. When it is more than 0.05 weight ratio, the easily decomposable property of poly α-methylstyrene is lost, which is not preferable. On the other hand, when it is less than 0.001 weight ratio, the compatibility with ceramics is insufficiently improved, which is not preferable.
本発明において、ブチルメタクリレート及び/又はブチ
ルアクリレートの量はα−メチルスチレンの0.1重量比
以上1.0重量比以下である。0.1重量比より少ないと構造
体のもろさに対する改善性が少なく、一方1.0重量比よ
りも多いとポリα−メチルスチレンの熱分解性が失われ
好ましくない。In the present invention, the amount of butyl methacrylate and / or butyl acrylate is not less than 0.1 weight ratio and not more than 1.0 weight ratio of α-methylstyrene. If the amount is less than 0.1% by weight, the improvement in the fragility of the structure is small, while if it is more than 1.0% by weight, the thermal decomposition property of poly α-methylstyrene is lost, which is not preferable.
本発明に用いられるアニオン系重合開始剤としては、好
ましくは有機リチウムが用いられ、中でもアルキルリチ
ウム、具体的にはn−ブチルリチウム、sec−ブチルリ
チウムなどが市場でも入手可能なものとして挙げられ
る。使用量は、特に制限はなく、共重合の組成及び分子
量によって適当な量が選ばれる。As the anionic polymerization initiator used in the present invention, organolithium is preferably used, and among them, alkyllithium, specifically, n-butyllithium, sec-butyllithium and the like are mentioned as commercially available. The amount used is not particularly limited, and an appropriate amount is selected depending on the composition of copolymerization and the molecular weight.
本発明においては活性化剤としてはエチレングリコール
のジアルキルエーテル、ジエチレングリコールのジアル
キルエーテル、或はテトラヒドロフランなどのエーテル
類を使用することも可能である。In the present invention, as the activator, ethylene glycol dialkyl ether, diethylene glycol dialkyl ether, or ethers such as tetrahydrofuran can be used.
本発明において、重合媒体としては炭化水素溶媒、好ま
しくはα−メチルスチレン自身或いはベンゼン、トルエ
ン、エチルベンゼン、ヘキサン、ヘプタン、メチルシク
ロヘキサン、デカリン、テトラリン等の不活性溶媒が使
用できる。In the present invention, as the polymerization medium, a hydrocarbon solvent, preferably α-methylstyrene itself or an inert solvent such as benzene, toluene, ethylbenzene, hexane, heptane, methylcyclohexane, decalin or tetralin can be used.
本発明においては、α−メチルスチレンとN,N−ジアル
キルアクリルアミドとアクリル酸及び/又はメタクリル
酸を共重合する際の温度は、特に制限はないが、実質的
に未反応単量体が存在しなくなる低温で行うことが好ま
しく、これによって、得られる共重合体の組成を定量的
に決定できる。そのための重合温度は通常5℃以下で、
−5℃〜−50℃が好ましく用いられる。In the present invention, the temperature for copolymerizing α-methylstyrene and N, N-dialkylacrylamide and acrylic acid and / or methacrylic acid is not particularly limited, but substantially unreacted monomers are present. It is preferable to carry out at a low temperature, at which the composition of the obtained copolymer can be quantitatively determined. The polymerization temperature for that is usually 5 ° C or lower,
-5 ° C to -50 ° C is preferably used.
さらに本発明では、α−メチルスチレンとN,N−ジアル
キルアクリルアミドとアクリル酸及び/又はメタクリル
酸を共重合した後にブチルメタクリレート及び/又はブ
チルアクリレートを添加して共重合反応を行うことを特
徴とする。添加速度は特に制限はないが、添加による発
熱が生じない程度が好ましく、この重合においても重合
温度は比較的低温で通常5℃以下が好ましい。Further, the present invention is characterized in that α-methylstyrene, N, N-dialkylacrylamide, acrylic acid and / or methacrylic acid are copolymerized, and then butyl methacrylate and / or butyl acrylate are added to carry out the copolymerization reaction. . The addition rate is not particularly limited, but it is preferably such that the addition does not generate heat, and the polymerization temperature in this polymerization is also relatively low, usually 5 ° C. or lower.
各共重合において重合時間の制限はないが、希望とする
単量体の変化率と重合温度によって数分〜数十時間が適
当である。There is no limitation on the polymerization time in each copolymerization, but several minutes to several tens hours are suitable depending on the desired monomer conversion rate and the polymerization temperature.
重合反応終了後は、アニオン重合の失活剤(アルコール
類、水、エポキシ化合物等)で処理され、次いで必要に
応じ不活性溶媒を蒸留、水蒸気蒸留で留去したり、多量
のメタノール中に投じることで共重合体を沈降分離する
ことも可能である。After the completion of the polymerization reaction, it is treated with an anionic polymerization deactivator (alcohols, water, epoxy compound, etc.), and then an inert solvent is distilled off if necessary, steam distillation or thrown into a large amount of methanol. It is also possible to separate the copolymer by sedimentation.
[発明の効果] 本発明の方法を実施することにより、セラミックバイン
ダー用として好適なセラミック粉末とのなじみがよくか
つ成型性のよいセラミック構造体を作る熱分解性共重合
体を得ることができ、工業的に極めて価値がある。[Effects of the Invention] By carrying out the method of the present invention, it is possible to obtain a thermally decomposable copolymer for forming a ceramic structure that is well compatible with a ceramic powder suitable for a ceramic binder and has good moldability, It is extremely valuable industrially.
[実施例] 以下に実施例を挙げて本発明をさらに説明する。[Examples] The present invention is further described below with reference to Examples.
実施例1 α−メチルスチレン35ml、トルエン100ml、ジエチレン
グリコールジメチルエーテル0.5ml、N,N−ジメチルアク
リルアミド0.5ml、メタクリル酸0.1mlを加え、室温でリ
ビングポリマーによる着色がみられるまでn−ブチルリ
チウムを添加し、着色がみられた後さらに1mmolを添加
した後に−5℃として2時間重合を行った。α−メチル
スチレンリビングポリマー溶液にn−ブチルメタクリレ
ート15mlを約3分で添加し、−5℃のまま2時間重合を
行った後メタノール1mlを添加して失活させた。大量の
メタノールに投じて得られた共重合体を乾燥させた重量
は42gであった。N,N−ジメチルアクリルアミド、メタク
リル酸及びn−ブチルメタクリレートの含量は各々1.1
重量%、0.2重量%、31.6重量%であり、30℃トルエン
溶液での極限粘度は0.48であった。また得られたポリマ
ーの軟化点は125℃であった。Example 1 35 ml of α-methylstyrene, 100 ml of toluene, 0.5 ml of diethylene glycol dimethyl ether, 0.5 ml of N, N-dimethylacrylamide and 0.1 ml of methacrylic acid were added, and n-butyllithium was added at room temperature until coloring by living polymer was observed. After coloring was observed, 1 mmol was further added, and the temperature was adjusted to -5 ° C to carry out polymerization for 2 hours. To the α-methylstyrene living polymer solution, 15 ml of n-butyl methacrylate was added in about 3 minutes, polymerization was carried out at −5 ° C. for 2 hours, and then 1 ml of methanol was added to deactivate. The weight of the dried copolymer obtained by throwing it into a large amount of methanol was 42 g. The contents of N, N-dimethylacrylamide, methacrylic acid and n-butylmethacrylate are 1.1 each.
%, 0.2% and 31.6% by weight, and the intrinsic viscosity in a toluene solution at 30 ° C. was 0.48. The softening point of the obtained polymer was 125 ° C.
比較例1 実施例1においてn−ブチルメタクリレートをα−メチ
ルスチレンと同時に仕込んだ他は同じ条件で重合を行っ
たところポリマーは得られなかった。Comparative Example 1 No polymer was obtained when polymerization was carried out under the same conditions as in Example 1 except that n-butyl methacrylate was charged at the same time as α-methylstyrene.
実施例2 n−ブチルメタクリレート15mlのかわりにiso−ブチル
メタクリレート15mlを用いたことのみ異ならせて実施例
1と同様に実験した。ポリマーの収率は全モノマーに対
して94重量%であり、極限粘度は0.45、N,N−ジメチル
アクリルアミド、メタクリル酸及びiso−ブチルメタク
リレートの含量は各々1.0重量%、0.2重量%、31.8重量
%であった。また得られたポリマーの軟化点は130℃で
あった。Example 2 An experiment was conducted in the same manner as in Example 1 except that 15 ml of iso-butyl methacrylate was used instead of 15 ml of n-butyl methacrylate. The polymer yield was 94% by weight based on the total monomers, the intrinsic viscosity was 0.45, and the contents of N, N-dimethylacrylamide, methacrylic acid and iso-butylmethacrylate were 1.0% by weight, 0.2% by weight and 31.8% by weight, respectively. Met. The softening point of the obtained polymer was 130 ° C.
比較例2 n−ブチルメタクリレート15mlを添加しない他は実施例
1と同様に実験した。得られたポリマーの軟化点は230
℃であった。Comparative Example 2 The same experiment as in Example 1 was carried out except that 15 ml of n-butyl methacrylate was not added. The softening point of the obtained polymer is 230.
It was ℃.
試験例 実施例1および2の共重合体について各々10gを、トル
エン30mlに溶解し、アルミナ(粒径2μm)30gと混練
したところ、いずれもよく分散し均一のスラリーとなっ
た。また溶媒を除去後、この構造体は80℃以上で成型が
可能であった。Test Example 10 g of each of the copolymers of Examples 1 and 2 was dissolved in 30 ml of toluene and kneaded with 30 g of alumina (particle size: 2 μm), and both were well dispersed to form a uniform slurry. Further, after removing the solvent, this structure could be molded at 80 ° C. or higher.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08F 297/02 MRD ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area C08F 297/02 MRD
Claims (3)
剤を用いてα−メチルスチレンとα−メチルスチレンに
対して以下に示すモノマーの総和が0.05重量比以下のN,
N−ジアルキルアクリルアミドとアクリル酸及び/又は
メタクリル酸を共重合し、次いでα−メチルスチレンの
0.1重量比以上1.0重量比以下のブチルメタクリレート及
び/又はブチルアクリレートを添加して重合反応を行う
ことを特徴とするセラミックバインダー用α−メチルス
チレン共重合体の製造方法。1. An α-methylstyrene in the presence of a hydrocarbon solvent and α-methylstyrene, and the total amount of the following monomers based on α-methylstyrene is 0.05% by weight or less N,
Copolymerization of N-dialkyl acrylamide with acrylic acid and / or methacrylic acid followed by α-methylstyrene
A method for producing an α-methylstyrene copolymer for a ceramic binder, comprising adding butyl methacrylate and / or butyl acrylate in an amount of 0.1 to 1.0 by weight to carry out a polymerization reaction.
なくなる低温で行われることを特徴とする特許請求の範
囲第1項記載のセラミックバインダー用α−メチルスチ
レン共重合体の製造方法。2. The production of α-methylstyrene copolymer for a ceramic binder according to claim 1, wherein the polymerization reaction is carried out at a low temperature at which substantially no unreacted monomer is present. Method.
とする特許請求の範囲第1項又は第2項記載のセラミッ
クバインダー用α−メチルスチレン共重合体の製造方
法。3. The method for producing an α-methylstyrene copolymer for a ceramic binder according to claim 1, wherein the polymerization reaction is carried out at 5 ° C. or lower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61078453A JPH0780975B2 (en) | 1986-04-04 | 1986-04-04 | Method for producing α-methylstyrene copolymer for ceramic binder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61078453A JPH0780975B2 (en) | 1986-04-04 | 1986-04-04 | Method for producing α-methylstyrene copolymer for ceramic binder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62235307A JPS62235307A (en) | 1987-10-15 |
| JPH0780975B2 true JPH0780975B2 (en) | 1995-08-30 |
Family
ID=13662454
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61078453A Expired - Lifetime JPH0780975B2 (en) | 1986-04-04 | 1986-04-04 | Method for producing α-methylstyrene copolymer for ceramic binder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0780975B2 (en) |
-
1986
- 1986-04-04 JP JP61078453A patent/JPH0780975B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62235307A (en) | 1987-10-15 |
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