JPS63319248A - Production of sintered ceramic - Google Patents
Production of sintered ceramicInfo
- Publication number
- JPS63319248A JPS63319248A JP62154297A JP15429787A JPS63319248A JP S63319248 A JPS63319248 A JP S63319248A JP 62154297 A JP62154297 A JP 62154297A JP 15429787 A JP15429787 A JP 15429787A JP S63319248 A JPS63319248 A JP S63319248A
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- mixing
- methylstyrene
- alcohol
- ceramic
- 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
Links
- 239000000919 ceramic Substances 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000002904 solvent Substances 0.000 claims abstract description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000843 powder Substances 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 9
- 239000011230 binding agent Substances 0.000 claims abstract description 7
- 239000002002 slurry Substances 0.000 claims abstract description 7
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 150000008065 acid anhydrides Chemical class 0.000 claims description 9
- 229920005992 thermoplastic resin Polymers 0.000 claims description 4
- 239000007870 radical polymerization initiator Substances 0.000 claims 1
- -1 poly(alpha-methyl styrene) Polymers 0.000 abstract description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 6
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 abstract description 5
- 239000003999 initiator Substances 0.000 abstract description 4
- 238000000465 moulding Methods 0.000 abstract description 4
- 239000002253 acid Substances 0.000 abstract 1
- 150000008064 anhydrides Chemical class 0.000 abstract 1
- 229920003251 poly(α-methylstyrene) Polymers 0.000 abstract 1
- 238000000034 method Methods 0.000 description 20
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 8
- 238000005245 sintering Methods 0.000 description 8
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 6
- 238000005238 degreasing Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- YIWUKEYIRIRTPP-UHFFFAOYSA-N 2-ethylhexan-1-ol Chemical compound CCCCC(CC)CO YIWUKEYIRIRTPP-UHFFFAOYSA-N 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OFNISBHGPNMTMS-UHFFFAOYSA-N 3-methylideneoxolane-2,5-dione Chemical compound C=C1CC(=O)OC1=O OFNISBHGPNMTMS-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- WUOACPNHFRMFPN-UHFFFAOYSA-N alpha-terpineol Chemical compound CC1=CCC(C(C)(C)O)CC1 WUOACPNHFRMFPN-UHFFFAOYSA-N 0.000 description 2
- NNBZCPXTIHJBJL-UHFFFAOYSA-N decalin Chemical compound C1CCCC2CCCCC21 NNBZCPXTIHJBJL-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- SQIFACVGCPWBQZ-UHFFFAOYSA-N delta-terpineol Natural products CC(C)(O)C1CCC(=C)CC1 SQIFACVGCPWBQZ-UHFFFAOYSA-N 0.000 description 2
- 238000007606 doctor blade method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 150000003254 radicals Chemical class 0.000 description 2
- 229940116411 terpineol Drugs 0.000 description 2
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 229940057995 liquid paraffin Drugs 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-N o-dicarboxybenzene Natural products OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- WVDDGKGOMKODPV-ZQBYOMGUSA-N phenyl(114C)methanol Chemical compound O[14CH2]C1=CC=CC=C1 WVDDGKGOMKODPV-ZQBYOMGUSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000001272 pressureless sintering Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- PXXNTAGJWPJAGM-UHFFFAOYSA-N vertaline Natural products C1C2C=3C=C(OC)C(OC)=CC=3OC(C=C3)=CC=C3CCC(=O)OC1CC1N2CCCC1 PXXNTAGJWPJAGM-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Landscapes
- Compositions Of Oxide Ceramics (AREA)
Abstract
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焼結体の製造方法に関し、詳しくは
、焼結処理前の成形体の強度を向上させ、しかも比較的
低温で完全に脱脂が行われるようにしたセラミック焼結
体の製造方法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing a ceramic sintered body, and more specifically, it improves the strength of a molded body before sintering treatment and completely degreases the body at a relatively low temperature. The present invention relates to a method of manufacturing a ceramic sintered body in which the following steps are performed.
複雑な形状、或いは高寸法精度が要求されるセラミック
製品の製造法としては、予め成形した成形体を焼成する
いわゆる常圧焼結法、或いは反応焼結法などの技術を利
用することが工業的に行なわれでいる。ここで成形体を
成形する手段としては、例えばアルミナやフェライトな
どのセラミック粉末に、必要に応じてバインダーの他に
焼結促進剤を加えた組成物を乾式あるいは湿式法で所望
の形状に成形、即ち湿式プレス法、ドクターブレード法
、押出成形法、射出成形法などにより成形 ゛
することが行われている。To manufacture ceramic products with complex shapes or requiring high dimensional accuracy, it is industrially possible to use techniques such as the so-called pressureless sintering method, in which a pre-formed compact is fired, or the reaction sintering method. It is being done. Here, the means for forming the compact includes, for example, forming a composition of ceramic powder such as alumina or ferrite into a desired shape using a dry or wet method, in which a sintering accelerator is added in addition to a binder as necessary. That is, molding is performed by a wet press method, a doctor blade method, an extrusion molding method, an injection molding method, or the like.
比較的低温で脱脂が可能な方法として本発明者らは、既
にポリアルファメチルスチレンを使用する方法(特開昭
56−51657号公報)、更に焼結前の成形物の強度
を改良する方法(特開昭60−65762号公報)を擢
案じている。The present inventors have already developed a method that uses polyalphamethylstyrene (Japanese Patent Application Laid-Open No. 56-51657) as a method that allows degreasing at a relatively low temperature, and a method that further improves the strength of the molded product before sintering ( JP-A No. 60-65762).
しかしながら、上述の方法では特別のポリα−メチルス
チレンを必要とし、しかも焼結前の成形物が特に湿式法
で成形した場合に不均一であるという問題があった。However, the above-mentioned method requires a special poly-α-methylstyrene and has the problem that the molded product before sintering is non-uniform, especially when molded by a wet method.
本発明者らは上記問題を解決する方法について鋭意検討
し、本発明を完成した。The present inventors have intensively studied methods for solving the above problems and have completed the present invention.
即ち、本発明はセラミック粉末に熱可塑性樹脂をバイン
ダーとして混合し、所望の形に成形したのち脱脂し、焼
結するセラミック焼結体の製造方法において、熱可塑性
樹脂として不飽和酸無水物で加熱処理したポリα−メチ
ルスチレンを用い、しかも少なくともアルコール類を含
有する溶媒中で混合してスラリー状として成形すること
を特徴とするセラミック成形体の製造方法である。That is, the present invention is a method for producing a ceramic sintered body in which ceramic powder is mixed with a thermoplastic resin as a binder, molded into a desired shape, degreased, and sintered. This is a method for producing a ceramic molded body, which uses treated polyα-methylstyrene and is characterized in that it is mixed in a solvent containing at least an alcohol and molded into a slurry.
本発明において、パイインダーとして用いるポリα−メ
チルスチレンとしては、不飽和酸無水物と加熱処理する
前においてα−メチルスチレンの単独重合体の他に、ポ
リα−メチルスチレンの分解特性を失わない程度他の共
重合性の単量体との共重合体も使用できる。例えば、他
の共重合性の単量体、スチレン及び誘導体、メタクリル
酸エステル、アクリル酸エステル等を数%〜数数十金含
有る共重合体などが使用できる。In the present invention, the polyα-methylstyrene used as the pie inder is not limited to a homopolymer of α-methylstyrene before being heat-treated with an unsaturated acid anhydride to the extent that it does not lose the decomposition properties of polyα-methylstyrene. Copolymers with other copolymerizable monomers can also be used. For example, a copolymer containing other copolymerizable monomers, styrene and derivatives, methacrylic esters, acrylic esters, etc. in several percent to several tens of gold can be used.
使用される重合体の分子量としては特に制限はないが通
常数千〜数百万のものが使用され、上述の特開昭60−
51657号公報に示されているような2〜8量体との
混合物であっても良い。There is no particular restriction on the molecular weight of the polymer used, but it is usually in the range of several thousand to several million.
It may also be a mixture with a dimer to octamer as shown in Japanese Patent No. 51657.
本発明において、重要なのは、上述のバインダーとして
用いるポリα−メチルスチレンを予め不飽和酸無水物と
加熱処理することにある。In the present invention, what is important is that the polyα-methylstyrene used as the binder is previously heat-treated with an unsaturated acid anhydride.
ここで不飽和酸無水物としては、不飽和基を含有する酸
無水物であればよく、好ましくは、無水マレイン酸、無
水イタコン酸等が用いられる。Here, the unsaturated acid anhydride may be any acid anhydride containing an unsaturated group, and maleic anhydride, itaconic anhydride, etc. are preferably used.
加熱処理は、不飽和酸無水物とポリα−メチルスチレン
をよく分散するため通常両者を溶解し得る溶剤に溶解せ
しめて行われる。加熱温度としては、ラジカル開始剤を
併用しない場合は通常100°C以上で、又併用する場
合は開始剤の分解温度以上で行われ好ましくは200°
C以下で行われる。加熱時間は温度によって異なるがポ
リα−メチルスチレンの分子量が大幅に低下しない程度
に止めるのが好ましく、通常30分〜数時間である。不
飽和酸無水物の使用割合としてはポリα−メチルスチレ
ン100重量部に対して0.01〜10重量部程度であ
るのが好ましい。0.01重量部より少ないと効果がな
く、10重量部より多いとポリα−メチルスチレンの分
解性に影響を与え好ましくない。The heat treatment is usually carried out by dissolving the unsaturated acid anhydride and polyα-methylstyrene in a solvent capable of dissolving them in order to disperse them well. The heating temperature is usually 100°C or higher when a radical initiator is not used in combination, or at a temperature higher than the decomposition temperature of the initiator when a radical initiator is used in combination, preferably 200°C.
Performed below C. The heating time varies depending on the temperature, but it is preferably kept to an extent that does not significantly reduce the molecular weight of polyα-methylstyrene, and is usually from 30 minutes to several hours. The proportion of the unsaturated acid anhydride used is preferably about 0.01 to 10 parts by weight per 100 parts by weight of polyα-methylstyrene. If it is less than 0.01 parts by weight, there is no effect, and if it is more than 10 parts by weight, it affects the decomposability of polyα-methylstyrene, which is not preferable.
本発明においては、こうして処理したポリα−メチルス
チレンは次いでセラミックとアルコール類と混合される
。混合は加熱処理の際の溶液にアルコール類を追加し、
さらにセラミック粉を加えて行うのが操作が簡単で経済
的である。従って加熱処理の際には最終のセラミック粉
のスラリーの溶剤の内ポリα−メチルスチレンの良溶媒
である炭化水素化合物を用い、その比率をセラミックと
混合する際の比率と同一とすればよい。In the present invention, the poly-alpha-methylstyrene treated in this way is then mixed with a ceramic and an alcohol. Mixing involves adding alcohol to the solution during heat treatment,
Furthermore, adding ceramic powder is easy and economical. Therefore, during the heat treatment, a hydrocarbon compound that is a good solvent for polyα-methylstyrene among the solvents in the final ceramic powder slurry may be used, and the ratio thereof may be the same as the ratio when mixed with the ceramic.
アルコール類としてはOH基を分子中に1個以上含有す
る化合物であり、多価アルコールであってもかまわない
。アルコール類としては通常炭素数1〜20程度のもの
が使用でき、メタノール、エタノール、プロパツール、
ブタノール、ヘキサノール等の脂肪族アルコールが一般
的であるが、もちろんシクロヘキサノール、テルピネオ
ール等の脂環族アルコール、フェノール、ベンジルアル
コール等の芳香族アルコール等も使用できる。The alcohols are compounds containing one or more OH groups in the molecule, and may be polyhydric alcohols. As alcohols, those having about 1 to 20 carbon atoms can be used, such as methanol, ethanol, propatool,
Aliphatic alcohols such as butanol and hexanol are commonly used, but of course alicyclic alcohols such as cyclohexanol and terpineol, aromatic alcohols such as phenol and benzyl alcohol, etc. can also be used.
本発明においては、上記アルコールと併用するポリα−
メチルスチレンの良溶媒である上述の炭化水素化合物と
してはベンゼン、トルエン、キシレン、エチルベンゼン
等の芳香族炭化水素化合物、シクロヘキサン、デカリン
等の脂環族炭化水素化合物が用いられ、テトラヒドロフ
ラン等のエーテルを併用することもできる。・
なお、アルコール類の使用量としては、種類およびセラ
ミックの種類により異なるが、好ましくはアルコール類
の体積を使用するセラミック粉末の0.1〜10倍程度
とするのが適当であり、良溶媒を使用する場合はその量
比は使用する溶剤の種類によって異なるが、良溶剤であ
る上述の溶剤をポリα−メチルスチレンが均一に熔解す
る程度に用いるとよい。また、必要ならば、先ず、セラ
ミッり粉末をアルコール類に分散し、次いで上述の処理
したポリα−メチルスチレンの溶液と混合することもで
きる。In the present invention, polyα-
The above-mentioned hydrocarbon compounds that are good solvents for methylstyrene include aromatic hydrocarbon compounds such as benzene, toluene, xylene, and ethylbenzene, and alicyclic hydrocarbon compounds such as cyclohexane and decalin, in combination with ethers such as tetrahydrofuran. You can also.・Although the amount of alcohol to be used varies depending on the type and type of ceramic, it is appropriate that the volume of alcohol be approximately 0.1 to 10 times the volume of the ceramic powder used, and a good solvent should be used. When used, the amount ratio varies depending on the type of solvent used, but it is preferable to use the above-mentioned solvent, which is a good solvent, to the extent that the polyα-methylstyrene is uniformly melted. Moreover, if necessary, the ceramic powder can be first dispersed in alcohol and then mixed with the above-mentioned solution of treated polyα-methylstyrene.
混合は、ボールミル、ホモジナイザー等の比較的強く混
合できる装置を用いるのが好ましい。又混合の際の温度
としては特に制限はなく、常温で行えば充分である。For mixing, it is preferable to use a device capable of relatively strong mixing, such as a ball mill or a homogenizer. There are no particular restrictions on the temperature during mixing, and room temperature is sufficient.
本発明においては、上記ポリα−メチルスチレンの他に
、必要に応じ可塑剤、例えば、フタル酸ジエステル、流
動パラフィン、スチレン或いはα−メチルスチレンのオ
リゴマーを併用できる。これらの使用割合としては、セ
ラミック粉100重量部に対してポリα−メチルスチレ
ンを5〜50重量部、不飽和酸無水物を0.001〜5
重量部、可塑剤を0〜50重量部使用するのが一般的で
ある。In the present invention, in addition to the above-mentioned polyα-methylstyrene, a plasticizer such as phthalic acid diester, liquid paraffin, styrene, or an oligomer of α-methylstyrene can be used in combination, if necessary. The ratio of these used is 5 to 50 parts by weight of polyα-methylstyrene and 0.001 to 5 parts by weight of unsaturated acid anhydride to 100 parts by weight of ceramic powder.
It is common to use 0 to 50 parts by weight of the plasticizer.
本発明の方法はどのような成形法にも適用可能であるが
、特にセラミック粉とバインダーと適当な溶媒を混合し
て流動化しドクターブレード法などでシート化する方法
などの湿式法に適用すると効果的である。Although the method of the present invention can be applied to any molding method, it is particularly effective when applied to wet methods such as mixing ceramic powder, a binder, and an appropriate solvent, fluidizing it, and forming it into a sheet using a doctor blade method. It is true.
以下、実施例を示し本発明をさらに説明する。 The present invention will be further explained below with reference to Examples.
実施例1
ポリα−メチルスチレン(数平均分子量15万)35w
t%、α−メチルスチレンオリゴマー(三井東圧化学
■製 MS−730) 15iyt%、無水マレイン酸
3.5wt%を含むトルエン溶液60gにベンゾイルパ
ーオキサイド20mgを加え、100°Cで1時間良く
撹拌したのち室温まで冷却し、次いで2−エチルヘキサ
ノール30dを加え、さらにセラミック成型用超微粒ア
ルミナ100gを加え良く混合したスラリーをテフロン
シート上に流し、厚さ1+mnのシートとした。Example 1 Poly α-methylstyrene (number average molecular weight 150,000) 35w
Add 20 mg of benzoyl peroxide to 60 g of toluene solution containing 15 iyt%, 3.5 wt% of maleic anhydride, and stir well for 1 hour at 100°C. Thereafter, the slurry was cooled to room temperature, 30 d of 2-ethylhexanol was added, 100 g of ultrafine alumina for ceramic molding was added, and the well-mixed slurry was poured onto a Teflon sheet to form a sheet with a thickness of 1+ mm.
乾燥後シートを切断して切断面を観察したところアルミ
ナは均一に分散していた。After drying, the sheet was cut and the cut surface was observed to find that the alumina was uniformly dispersed.
また、シートを1010X10に切断し、直径5mmの
穴をパツキンカッターであけたものを400″Cで脱脂
したところシート及び穴の形状に欠陥はなかった。更に
1400℃で焼結して欠陥のないアルミナの焼結体を得
た。In addition, when the sheet was cut to 1010 x 10 and a hole with a diameter of 5 mm was made with a packing cutter and degreased at 400''C, there were no defects in the shape of the sheet or the hole.Furthermore, the sheet was sintered at 1400℃ and there was no defect. A sintered body of alumina was obtained.
比較例1
無水マレイン酸と加熱処理せず、しかも2−エチルヘキ
サノールに代えてトルエンを用いた他は実施例1と同様
にしたところ、切断面は不均一であり、穴をあける際に
シートの一部が破壊し、脱脂後は全部で3ケ所が破壊し
ていた。Comparative Example 1 The same procedure as Example 1 was performed except that no heat treatment was performed with maleic anhydride and toluene was used instead of 2-ethylhexanol. Some parts were destroyed, and after degreasing, a total of three places were destroyed.
実施例2
無水マレイン酸に代えて無水イタコン酸を用いた他は実
施例1と同様にしたところ、シートの断面は均一であり
、脱脂後の成型体の形状に問題は・なく、焼結後の欠陥
もなかった。Example 2 The same procedure as Example 1 was carried out except that itaconic anhydride was used instead of maleic anhydride. The cross section of the sheet was uniform, there was no problem with the shape of the molded product after degreasing, and after sintering. There were no defects.
実施例3
ポリα−メチルスチレンに代えてα−メチルスチレンと
スチレンの共重合体(分子量25万、スチレン含量52
重量%)を用い、しかもアルコールとしてテルピネオー
ルを用いた他は実施例1と同様にしたところ、脱脂後の
成型体の形状に異常はなく、更に1400°Cで焼結し
て均一な焼結体を得た。Example 3 A copolymer of α-methylstyrene and styrene (molecular weight 250,000, styrene content 52
When the procedure was the same as in Example 1 except that terpineol was used as the alcohol, there was no abnormality in the shape of the molded body after degreasing, and a uniform sintered body was obtained by sintering at 1400°C. I got it.
本発明の方法を実施することにより脱脂前の成型物が均
一であり、比較的低温で脱脂でき、しかも加工、脱脂、
焼結の際に破壊することなくセラミック焼結体が製造で
きるので工業的に極めて価値がある。By implementing the method of the present invention, the molded product before degreasing is uniform, can be degreased at a relatively low temperature, and furthermore, processing, degreasing,
It is extremely valuable industrially because ceramic sintered bodies can be produced without breaking during sintering.
Claims (1)
混合し、所望の形に成形したのち脱脂し、焼結するセラ
ミック焼結体の製造方法において、熱可塑性樹脂として
不飽和酸無水物と加熱処理したポリα−メチルスチレン
を用い、しかも少なくともアルコール類を含有する溶媒
中で混合してスラリー状として成形することを特徴とす
るセラミック成形体の製造方法。 2、熱可塑性樹脂をラジカル重合開始剤の存在下に不飽
和酸無水物と処理する特許請求の範囲第1項記載のセラ
ミック成形体の製造方法。[Claims] 1. A method for producing a ceramic sintered body in which ceramic powder is mixed with a thermoplastic resin as a binder, molded into a desired shape, degreased, and sintered, wherein an unsaturated acid anhydride is used as the thermoplastic resin. 1. A method for producing a ceramic molded body, which comprises using heat-treated polyα-methylstyrene and mixing the mixture in a solvent containing at least alcohol to form a slurry. 2. The method for producing a ceramic molded body according to claim 1, which comprises treating a thermoplastic resin with an unsaturated acid anhydride in the presence of a radical polymerization initiator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62154297A JPS63319248A (en) | 1987-06-23 | 1987-06-23 | Production of sintered ceramic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62154297A JPS63319248A (en) | 1987-06-23 | 1987-06-23 | Production of sintered ceramic |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63319248A true JPS63319248A (en) | 1988-12-27 |
Family
ID=15581053
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62154297A Pending JPS63319248A (en) | 1987-06-23 | 1987-06-23 | Production of sintered ceramic |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63319248A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2024122491A1 (en) * | 2022-12-07 | 2024-06-13 | 積水化学工業株式会社 | Inorganic particle dispersed slurry composition and method for producing inorganic sintered body |
-
1987
- 1987-06-23 JP JP62154297A patent/JPS63319248A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2024122491A1 (en) * | 2022-12-07 | 2024-06-13 | 積水化学工業株式会社 | Inorganic particle dispersed slurry composition and method for producing inorganic sintered body |
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