JPH0450157A - Ceramic material for extrusion molding and process for extrusion molding of the material - Google Patents
Ceramic material for extrusion molding and process for extrusion molding of the materialInfo
- Publication number
- JPH0450157A JPH0450157A JP2158816A JP15881690A JPH0450157A JP H0450157 A JPH0450157 A JP H0450157A JP 2158816 A JP2158816 A JP 2158816A JP 15881690 A JP15881690 A JP 15881690A JP H0450157 A JPH0450157 A JP H0450157A
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- ceramic material
- extrusion molding
- less
- 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
Links
- 238000001125 extrusion Methods 0.000 title claims abstract description 65
- 229910010293 ceramic material Inorganic materials 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title claims description 10
- 239000000463 material Substances 0.000 title abstract description 13
- 150000004676 glycans Chemical class 0.000 claims abstract description 26
- 229920001282 polysaccharide Polymers 0.000 claims abstract description 26
- 239000005017 polysaccharide Substances 0.000 claims abstract description 26
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 15
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229920000609 methyl cellulose Polymers 0.000 claims abstract description 15
- 239000001923 methylcellulose Substances 0.000 claims abstract description 15
- 235000010981 methylcellulose Nutrition 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000012188 paraffin wax Substances 0.000 claims abstract description 10
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims abstract description 9
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims abstract description 9
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 claims abstract description 9
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 claims abstract description 9
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 claims abstract description 9
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 claims abstract description 9
- 235000021355 Stearic acid Nutrition 0.000 claims abstract description 8
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims abstract description 8
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 8
- 235000019422 polyvinyl alcohol Nutrition 0.000 claims abstract description 8
- 239000008117 stearic acid Substances 0.000 claims abstract description 8
- 239000001993 wax Substances 0.000 claims abstract description 8
- 230000000813 microbial effect Effects 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 18
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 8
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims description 8
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical group OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 4
- 239000000919 ceramic Substances 0.000 abstract description 27
- 239000002245 particle Substances 0.000 abstract description 7
- 239000011230 binding agent Substances 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 5
- 239000004014 plasticizer Substances 0.000 abstract description 5
- 244000005700 microbiome Species 0.000 abstract description 3
- 229920002984 Paramylon Polymers 0.000 abstract description 2
- 229920006184 cellulose methylcellulose Polymers 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 15
- 238000005452 bending Methods 0.000 description 14
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 7
- 238000010304 firing Methods 0.000 description 5
- 238000009472 formulation Methods 0.000 description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 235000012438 extruded product Nutrition 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 229920002558 Curdlan Polymers 0.000 description 3
- 239000001879 Curdlan Substances 0.000 description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 3
- 229940078035 curdlan Drugs 0.000 description 3
- 235000019316 curdlan Nutrition 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 239000011796 hollow space material Substances 0.000 description 2
- 150000002440 hydroxy compounds Chemical class 0.000 description 2
- 229910052582 BN Inorganic materials 0.000 description 1
- 229920002498 Beta-glucan Polymers 0.000 description 1
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 1
- 229920001503 Glucan Polymers 0.000 description 1
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical compound [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052863 mullite Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- MTPVUVINMAGMJL-UHFFFAOYSA-N trimethyl(1,1,2,2,2-pentafluoroethyl)silane Chemical compound C[Si](C)(C)C(F)(F)C(F)(F)F MTPVUVINMAGMJL-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は押出成形により高密度で、かつ高強度を有する
セラミックス焼成体を得るための押出成形用セラミック
ス材料及びその押出成形方法に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a ceramic material for extrusion molding and an extrusion molding method for obtaining a ceramic fired body having high density and high strength by extrusion molding. .
[従来の技術]
従来、押出成形用セラミックス材料としては、一般にバ
インダーとしてメチルセルロースなどのセルロース系化
合物を使用し、可塑剤としてグリセリン等の多価ヒドロ
キシ化合物を使用し、これらをセラミックス材料に含有
したものが知られている。例えば特開昭5B−1148
63号公報に記載のものが知られている。[Prior Art] Conventionally, as a ceramic material for extrusion molding, a cellulose compound such as methyl cellulose is generally used as a binder, a polyhydric hydroxy compound such as glycerin is used as a plasticizer, and these are contained in the ceramic material. It has been known. For example, JP-A-5B-1148
The one described in Publication No. 63 is known.
[発明が解決しようとする課題]
しかしながら、従来の押出成形用セラミックス材料にお
いては、押出成形し、これを焼成してなるセラミックス
焼成体は密度及び曲げ強度の面で十分とはいえず複雑形
状のものの製造には不適当であるので、高密度で、かつ
高い曲げ強度を有するセラミックス焼成体で、しかも複
雑形状のものを得るための押出成形用セラミックス材料
の出現が切望されていた。[Problems to be Solved by the Invention] However, with conventional extrusion-molding ceramic materials, the ceramic fired body obtained by extrusion-molding and firing does not have sufficient density and bending strength, and has a complex shape. Since it is unsuitable for manufacturing objects, there has been a strong desire for a ceramic material for extrusion molding to obtain ceramic fired bodies with high density and high bending strength, as well as complex shapes.
そこで本発明は前記に鑑み、焼成して得られたセラミッ
クス焼成体が高密度で、かつ高強度に優れた特性を有し
、複雑形状のものであっても強度のばらつきの少ない押
出成形用セラミックス材料及びその押出成形方法を提供
することを目的としたものである。In view of the above, the present invention has been developed to produce a ceramic body for extrusion molding in which the fired ceramic body obtained by firing has high density and excellent properties of high strength, and has little variation in strength even when having a complex shape. The purpose of this invention is to provide a material and a method for extrusion molding the same.
[課題を解決するための手段]
本発明の第1発明はセラミックス材料100重量部に対
し、微生物起源の多糖類を2〜5重量部、アクリル酸オ
リゴマー2重量部以下、ワックス、パラフィン、ステア
リン酸のうち少なくとも1種を3重量部以下と所定量の
水とからなる混合物を含有する押出成形用セラミックス
材料であり、本発明の第2発明はセラミックス材料10
0重量部に対し、微生物起源の多糖類並びにポリビニル
アルコール、メチルセルロース、カルボキシメチルセル
ロース及びヒドロキシプロピルメチルセルロースのうち
少くとも1種の合計量2〜7重量部、アクリル酸オリゴ
マー2重量部以下、ワックス、パラフィン、ステアリン
酸のうち少な(とも1種を3重量部以下と所定量の水と
からなる混合物を含有する押出成形用のセラミックス材
料である。この第2発明における微生物起源の多糖類と
ポリビニルアルコール、メチルセルロース、カルボキシ
メチルセルロース及びヒドロキシプロピルメチルセルロ
ースのうち少くとも1種との混合比率は同じ、もしくは
微生物起源の多糖類の方を多く配合することが望ましい
。[Means for Solving the Problems] The first aspect of the present invention is to add 2 to 5 parts by weight of polysaccharides of microbial origin, 2 parts by weight or less of acrylic acid oligomers, wax, paraffin, and stearic acid to 100 parts by weight of the ceramic material. A second aspect of the present invention is a ceramic material for extrusion molding containing a mixture of 3 parts by weight or less of at least one of these and a predetermined amount of water.
0 parts by weight, a total amount of 2 to 7 parts by weight of polysaccharides of microbial origin and at least one of polyvinyl alcohol, methylcellulose, carboxymethylcellulose, and hydroxypropylmethylcellulose, 2 parts by weight or less of acrylic acid oligomers, wax, paraffin, It is a ceramic material for extrusion molding containing a mixture consisting of 3 parts by weight or less of one type of stearic acid and a predetermined amount of water. , carboxymethyl cellulose, and hydroxypropyl methyl cellulose at the same mixing ratio, or it is desirable to mix more polysaccharides of microbial origin.
上記原料粉末となるセラミックス材料はアルミナ、ジル
コニア、ムライト、コージェライト等の酸化物系セラミ
ックス粉末材料のどれでもよい。又、前述したものを主
成分とした、マグネシア、ジルコニア等の酸化物系セラ
ミックス粉末材料、炭化ケイ素、炭化チタン等の炭化物
系セラミックス粉末材料、窒化ケイ素、窒化ボロン等の
窒化物系セラミックス粉末材料との混合物でもよい。セ
ラミックス粉末はできる限り小さい粒度を有することが
望ましく、特に1μ■以下の粒度を有することが好まし
く、更には0.5μ■以下の粒度が好ましい。又、セラ
ミックス材料の純度はできる限り高いものが望ましく9
9%以上が好ましく、更には99.9%以上のものが好
ましい。The ceramic material serving as the raw material powder may be any oxide-based ceramic powder material such as alumina, zirconia, mullite, and cordierite. In addition, oxide-based ceramic powder materials such as magnesia and zirconia, carbide-based ceramic powder materials such as silicon carbide and titanium carbide, and nitride-based ceramic powder materials such as silicon nitride and boron nitride, which have the above-mentioned materials as main components, and It may also be a mixture of It is desirable that the ceramic powder has a particle size as small as possible, particularly preferably a particle size of 1 μm or less, and more preferably a particle size of 0.5 μm or less. In addition, it is desirable that the purity of the ceramic material be as high as possible9.
It is preferably 9% or more, more preferably 99.9% or more.
又、微生物起源の多糖類とはグルカン系の多糖類が好ま
しく、パラミロン、カードラン、スフレノグルカンなど
のβ−1,3−グリコシドを有スるβ−1,3−グルカ
ンが保水性、可塑性などの面から更に好ましい。In addition, the polysaccharides originating from microorganisms are preferably glucan-based polysaccharides, and β-1,3-glucan containing β-1,3-glycoside such as paramylon, curdlan, and soufflenoglucan has good water retention and plasticity. It is more preferable from the viewpoint of
この微生物起源の多糖類は上記セラミックス粉末となじ
みがよく、可塑剤及びバインダーとして使用され、セラ
ミックス材料100重量部に対して2〜5重量部用いら
れる。又、ポリビニルアルコール、メチルセルロース、
カルボキシメチルセルロース及びヒドロキシプロピルメ
チルセルロースもバインダーとして使用され、これと上
記微生物起源の多糖類との混合物でセラミックス材料1
00重量部に対し2〜7重量部添加する。上記添加量を
2〜5重量部又は2〜7重量部の範囲に限定したのは、
この範囲より添加量が少ないと押出成形の際に形状が崩
れ、押出成形品を得ることができなくなるとともに、添
加量が多いと本発明の目的とする高強度、かつ高密度を
有するセラミックス焼成体を得ることができなくなるた
めである。更に第2発明の実施態様において微生物起源
の多糖類並びにポリビニルアルコール、メチルセルロー
ス、カルボキシメチルセルロース及びヒドロキシプロピ
ルメチルセルロースのうち少くとも1種の混合比率を同
じ、もしくは微生物起源の多糖類の方を多く配合するこ
とにより、より優れた強度と密度を有し、かつ強度のば
らつきの少ないセラミックス焼成体を得ることができる
。This polysaccharide of microbial origin is compatible with the ceramic powder and is used as a plasticizer and binder, and is used in an amount of 2 to 5 parts by weight per 100 parts by weight of the ceramic material. Also, polyvinyl alcohol, methyl cellulose,
Carboxymethyl cellulose and hydroxypropyl methyl cellulose are also used as binders, and a mixture of these and the above-mentioned polysaccharides of microbial origin is used to form ceramic material 1.
Add 2 to 7 parts by weight per 00 parts by weight. The above addition amount was limited to 2 to 5 parts by weight or 2 to 7 parts by weight because
If the amount added is less than this range, the shape will collapse during extrusion molding, making it impossible to obtain an extruded product, and if the amount added is too large, the ceramic fired product will have the high strength and high density that is the objective of the present invention. This is because it will not be possible to obtain Furthermore, in the embodiment of the second invention, the mixing ratio of the polysaccharide of microbial origin and at least one of polyvinyl alcohol, methyl cellulose, carboxymethyl cellulose, and hydroxypropyl methyl cellulose is the same, or the polysaccharide of microbial origin is blended in a larger amount. As a result, a fired ceramic body having superior strength and density and less variation in strength can be obtained.
又、上記配合によって混合物をセラミック材料に対して
含有させることにより、混合物がセラミックス材料粉末
及び他の添加剤になじみやすく、このため押出成形用セ
ラミックス材料は均一なものとなり、更に押出成形用セ
ラミックス材料は押出成形により、適切な圧力を加える
ことによりセラミックス材料粉末間の隙間が減少しくセ
ラミックス材料粉末同士が接近し)、高密度を有する押
出成形品を得ることができ、更にはこれを焼成すること
により高密度を有するセラミックス焼成体を得ることが
できるとともに強度のばらつきの少ないものが得られる
。In addition, by incorporating the mixture into the ceramic material according to the above formulation, the mixture is easily compatible with the ceramic material powder and other additives, so that the ceramic material for extrusion molding becomes uniform, and furthermore, the ceramic material for extrusion molding becomes uniform. By extrusion molding, by applying appropriate pressure, the gaps between the ceramic material powders are reduced and the ceramic material powders come closer to each other), and an extruded product with high density can be obtained, and furthermore, this can be fired. As a result, it is possible to obtain a fired ceramic body having a high density, and a product with little variation in strength.
そして、上記混合物に更に解膠剤としてアクリル酸オリ
ゴマー2重量部以下(0は含まず)、滑剤としてワック
ス、ステアリン酸、パラフィン(好ましくはエマルジョ
ン)のうち少なくとも1種を3重量部以下(0は含まず
)添加することによりセラミックス材料を均一に成形及
び押出し成形することができるとともに、複雑な断面形
状を有する例えばLアングル、ハニカム材、矩形ホロー
材などの押出成形に有効である。Then, to the above mixture, 2 parts by weight or less of acrylic acid oligomer (not including 0) as a deflocculant, and 3 parts by weight or less of at least one of wax, stearic acid, and paraffin (preferably emulsion) as a lubricant (0 is not included). By adding (excluding) ceramic materials, it is possible to uniformly mold and extrude the ceramic material, and it is effective for extrusion molding of materials having complicated cross-sectional shapes, such as L angles, honeycomb materials, rectangular hollow materials, etc.
本発明の第3発明は前記第1発明における押出成形用の
セラミックス材料を供給口より供給経路内へ供給し、こ
れを供給経路の一端に設けられた口金に向って、60k
gf/c12以上の押出圧力にて加圧し、前記口金より
押出成形品を成形する押出成形用セラミックス材料の押
出成形方法である。A third aspect of the present invention is to supply the ceramic material for extrusion molding according to the first aspect into the supply route from the supply port, and to direct the ceramic material to the nozzle provided at one end of the supply route for 60 kg.
This is an extrusion molding method of a ceramic material for extrusion molding, which pressurizes at an extrusion pressure of gf/c12 or more and molds an extrusion molded product from the die.
又、第4発明は前記第2発明における押出成形用のセラ
ミックス材料を上記第3発明と同様の方法により押出成
形する方法である。A fourth invention is a method of extrusion molding the ceramic material for extrusion molding according to the second invention by a method similar to the third invention.
具体的には、本発明に係る押出成形用セラミックス材料
を得て、これを例えば第1図図示の真空押出装置5の供
給口1より供給経路2内に供給し、これを前記供給経路
2の一端に設けられた口金3に向って脱気をしながら6
0kgf/cm 2以上の押出圧力にてスクリュー4で
加圧する。Specifically, a ceramic material for extrusion molding according to the present invention is obtained, and this is supplied into the supply route 2 from the supply port 1 of the vacuum extrusion device 5 shown in FIG. 6 while degassing towards the cap 3 provided at one end.
Pressurize with the screw 4 at an extrusion pressure of 0 kgf/cm 2 or more.
ここで押出圧力を60kgf/c12以上にしたのは6
0kgr/Cm2より低圧で押出した場合、押出成形が
困難になるからであるとともに、本発明の目的である密
度及び曲げ強度を有するセラミックス焼成体を得ること
ができなくなるからである。Here, the extrusion pressure was set to 60 kgf/c12 or more.
This is because if extrusion is performed at a pressure lower than 0 kgr/Cm2, extrusion molding becomes difficult, and it becomes impossible to obtain a ceramic fired body having the density and bending strength that are the objectives of the present invention.
より好ましくは60kgf/c+a’以上とすることに
より成形密度を向上させ、より高強度、高密度にするこ
とができる。更に口金3より押出された押出成形品を乾
燥させ、これを焼成することにより、高密度でかつ高強
度を有し、強度のばらつきの少ないしかも複雑形状のセ
ラミックス焼成体を得ることができる。なお、バインダ
ーとしてセルロース系化合物を使用し、可塑剤として多
価ヒドロキシ化合物を使用し、これらをセラミックス材
料に含有した従来のものは、通常50〜60kgf/c
m2の押出圧力にて成形している。More preferably, by setting it to 60 kgf/c+a' or more, the molding density can be improved and higher strength and density can be achieved. Furthermore, by drying the extrusion molded product extruded from the die 3 and firing it, a ceramic fired body having a high density and high strength, with little variation in strength, and having a complex shape can be obtained. In addition, conventional products that use a cellulose compound as a binder and a polyhydric hydroxy compound as a plasticizer, and contain these in a ceramic material, usually have a yield of 50 to 60 kgf/c.
It is molded at an extrusion pressure of m2.
これは該範囲より低圧では保形性の良好なものが得られ
に<<、場合によっては押出成形ができなく、高圧では
押出された押出成形品の乾燥割れが顕著になるためであ
る。This is because if the pressure is lower than this range, a product with good shape retention may not be obtained, and in some cases, extrusion molding may not be possible, and if the pressure is higher than this range, dry cracking of the extruded product becomes noticeable.
[実施例]
以下実施例によって本発明を具体的に説明する。粒度1
μ−以下のアルミナ粉末100重量部にカードランを主
成分とする微生物起源の多糖類2重量部、メチルセルロ
ース2重量部、パラフィン 0.5重量部、アクリル酸
オリゴマー 1重量部、イオン交換水17.5重量部の
配合にて混練機にて十分に混練し、得られた押出成形用
セラミックス材料を真空押出装置にて押出圧力60kg
f/cm2、押出速度300〜400+ni/winの
条件で脱気雰囲気750+a+aHg以上で押出成形を
行い押出成形品を得た。これを300〜400℃の温度
で脱脂(添加剤熱分解)を充分に行った後、1600℃
で2時間常圧焼成しセラミックス焼成体を得た。[Example] The present invention will be specifically described below with reference to Examples. Particle size 1
100 parts by weight of alumina powder below μ-, 2 parts by weight of polysaccharide of microbial origin whose main component is curdlan, 2 parts by weight of methyl cellulose, 0.5 parts by weight of paraffin, 1 part by weight of acrylic acid oligomer, 17. A mixture of 5 parts by weight was thoroughly kneaded using a kneader, and the obtained ceramic material for extrusion molding was extruded using a vacuum extruder at a pressure of 60 kg.
Extrusion molding was carried out in a degassing atmosphere of 750+a+aHg or more under the conditions of f/cm2 and extrusion speed of 300 to 400+ni/win to obtain an extruded product. After sufficient degreasing (additive thermal decomposition) at a temperature of 300 to 400°C, 1600°C
A ceramic fired body was obtained by firing at normal pressure for 2 hours.
なお、上記において使用したアルミナ粉末は99%α−
アルミナで、真空押出装置の押出型(口金)として非対
称形ソリッド材、40X 20mmのし一アングル材型
(肉厚5mm)を使用した。The alumina powder used above was 99% α-
Alumina was used as an extrusion mold (die) of a vacuum extrusion device using an asymmetrical solid material, 40 x 20 mm, single angle material mold (wall thickness: 5 mm).
又、比較のため粒度1μ丑以下のアルミナ粉末100重
量部にグリセリン2.5重量部、メチルセルロース 7
.5重量部、アクリル酸オリゴマー1重量部、イオン交
換水25重量部の配合にて混線機にて混練し、これに適
した条件において押出成形し、焼成を行いセラミックス
焼成体を得た。なお使用するアルミナ粉末、真空押出装
置、押出型は同じものである。For comparison, 100 parts by weight of alumina powder with a particle size of 1 μm or less, 2.5 parts by weight of glycerin, and 7 parts by weight of methyl cellulose were added.
.. 5 parts by weight of acrylic acid oligomer, 1 part by weight of acrylic acid oligomer, and 25 parts by weight of ion-exchanged water were kneaded in a mixer, extrusion molded under suitable conditions, and fired to obtain a ceramic fired body. Note that the alumina powder, vacuum extrusion device, and extrusion die used are the same.
上記のようにして得られたセラミックス焼成体の密度及
び曲げ強度を測定した。The density and bending strength of the ceramic fired body obtained as described above were measured.
測定結果より密度は比較例のものが3.72gram
’であるのに対し、本発明のものでは3,92g/cm
3と高く、又、曲げ強度は比較例のものが257MPa
であるのに対し本発明のものでは421MPaと高く、
更に本発明によるセラミックス焼成体の曲げ強度のワイ
ブル確率分布(第2図図示)を作成してみたところ、ワ
イブル係数が21と高く、強度のばらつきが少なく、均
一性に優れていることが判る。According to the measurement results, the density of the comparative example is 3.72 grams.
', whereas in the case of the present invention, it is 3,92g/cm
3, and the bending strength of the comparative example is 257 MPa.
In contrast, the pressure of the present invention is as high as 421 MPa,
Furthermore, when we created a Weibull probability distribution (shown in Figure 2) of the bending strength of the fired ceramic body according to the present invention, it was found that the Weibull coefficient was as high as 21, indicating that the strength had little variation and was excellent in uniformity.
又、上記の配合の中で微生物起源の多糖類と、メチルセ
ルロースとの配合量の変化によるセラミックス焼成体の
密度及び曲げ強度を測定した結果を第3.4図に示す。Figure 3.4 shows the results of measuring the density and bending strength of the fired ceramic body as a result of varying the amounts of polysaccharide of microbial origin and methyl cellulose in the above formulation.
なお、イオン交換水を除く他の配合量については上記と
同様である。Note that the other blending amounts except for ion-exchanged water are the same as above.
第3.4図に示すように微生物起源の多糖類のみを2〜
5重量部又は微生物起源の多糖類とメチルセルロースと
を2〜6重量部で、かつ微生物起源の多糖類とメチルセ
ルロースとの混合比率が同じ、もしくは微生物起源の多
糖類の方を多く配合してなるものが密度及び曲げ強度に
優れていることが判る。As shown in Figure 3.4, only polysaccharides of microbial origin are
5 parts by weight or 2 to 6 parts by weight of polysaccharides of microbial origin and methylcellulose, and the mixing ratio of polysaccharides of microbial origin and methylcellulose is the same, or the polysaccharide of microbial origin is blended in a larger amount. It can be seen that the material has excellent density and bending strength.
又、上記と同じ配合で他の複雑断面形状のものについて
も同様に実験を行った結果、ハニカム材、矩形ホロー材
などについても同様の密度、曲げ強度及びワイブル係数
が得られており、本発明の押出成形用セラミックス材料
により、高密度及び高強度を有し、かつ強度のばらつき
が少ないセラミックス焼成体を単純な断面形状を有する
ものはもちろん、複雑な断面形状を有するものでも得る
ことができる。Furthermore, as a result of conducting similar experiments on other complex cross-sectional shapes with the same composition as above, similar density, bending strength, and Weibull coefficient were obtained for honeycomb materials, rectangular hollow materials, etc., and the present invention By using the ceramic material for extrusion molding, it is possible to obtain ceramic fired bodies having high density and high strength, and with little variation in strength, not only with simple cross-sectional shapes but also with complicated cross-sectional shapes.
又、上記粒度1μ■以下のアルミナ粉末100重量部に
カードランを主成分とする微生物起源の多糖類2重量部
、メチルセルロース2重量部、パラフィン 0.5重量
部、アクリル酸オリゴマー1重量部、イオン交換水17
.5重量部の配合のもので、押出圧力に対するセラミッ
クス焼成体の曲げ強度の測定を行い、この結果を第5図
に示す。第5図に示すように押出圧力60kgf 7c
m 2以上で曲げ強度が安定化する傾向があり、押出圧
力60kgf/c+++ 2以下では曲げ強度が低下す
る傾向がある。又、本発明の目的とする曲げ強度は押出
圧内約60kgf/cm2で得られることが判る。In addition, 100 parts by weight of the above alumina powder with a particle size of 1μ or less, 2 parts by weight of polysaccharide of microbial origin whose main component is curdlan, 2 parts by weight of methylcellulose, 0.5 parts by weight of paraffin, 1 part by weight of acrylic acid oligomer, and ions. Exchange water 17
.. The bending strength of the fired ceramic body against extrusion pressure was measured using a mixture of 5 parts by weight, and the results are shown in FIG. Extrusion pressure 60kgf 7c as shown in Figure 5
When the extrusion pressure is 60 kgf/c+++2 or less, the bending strength tends to be stabilized. It is also seen that the bending strength aimed at by the present invention can be obtained at an extrusion pressure of about 60 kgf/cm2.
又、本発明の上記と異なる配合についても同様の測定を
行ったが、上記はぼ同様の結果が得られた。Further, similar measurements were performed on formulations of the present invention different from those described above, and almost the same results were obtained.
[発明の効果]
以上のように本発明によれば、上記配合からなる混合物
をセラミックス材料に含有する押出成形用セラミックス
材料を得ることにより、焼成して得られたセラミックス
焼成体が高密度で、かつ高強度に優れた特性を有すると
ともに、複雑形状のものでも強度のばらつきが少ないも
のを得ることができる。[Effects of the Invention] As described above, according to the present invention, by obtaining a ceramic material for extrusion molding containing a mixture consisting of the above-mentioned formulation in the ceramic material, the ceramic fired body obtained by firing has a high density, In addition, it has excellent properties of high strength, and even products with complicated shapes can be obtained with little variation in strength.
又、上記押出成形用セラミックス材料の押出成形方法に
より、かかる優れた特性を有するセラミックス焼成体を
複雑な形状のものであっても容易に得ることができるも
のである。Moreover, by the extrusion molding method of the ceramic material for extrusion molding described above, a fired ceramic body having such excellent properties can be easily obtained even if it has a complicated shape.
第1図は本発明の詳細な説明図、第2図は本発明による
セラミックス焼成体のワイブル確率分布を示す図、第3
.4図は各配合における密度及び曲げ強度の測定結果を
示す図、第5図は押出圧力に対する曲げ強度測定結果を
示す図である。
■・・・供給口、2・・・供給経路、3・・・口金、4
・・・スクリュー 5・・・押出装置。FIG. 1 is a detailed explanatory diagram of the present invention, FIG. 2 is a diagram showing the Weibull probability distribution of the ceramic fired body according to the present invention, and FIG.
.. FIG. 4 is a diagram showing the measurement results of density and bending strength for each formulation, and FIG. 5 is a diagram showing the measurement results of bending strength with respect to extrusion pressure. ■... Supply port, 2... Supply route, 3... Cap, 4
...Screw 5...Extrusion device.
Claims (6)
源の多糖類を2〜5重量部、アクリル酸オリゴマー2重
量部以下、ワックス、パラフィン、ステアリン酸のうち
少なくとも1種を3重量部以下と所定量の水とからなる
混合物を含有する押出成形用セラミックス材料。(1) For 100 parts by weight of the ceramic material, 2 to 5 parts by weight of polysaccharides of microbial origin, 2 parts by weight or less of acrylic acid oligomers, and 3 parts by weight or less of at least one of wax, paraffin, and stearic acid are specified amounts. A ceramic material for extrusion molding containing a mixture of water and water.
源の多糖類並びにポリビニルアルコール、メチルセルロ
ース、カルボキシメチルセルロース及びヒドロキシプロ
ピルメチルセルロースのうち少くとも1種の合計量2〜
7重量部、アクリル酸オリゴマー2重量部以下、ワック
ス、パラフィン、ステアリン酸のうち少なくとも1種を
3重量部以下と所定量の水とからなる混合物を含有する
押出成形用セラミックス材料。(2) Total amount of microbial-originated polysaccharides and at least one of polyvinyl alcohol, methylcellulose, carboxymethylcellulose, and hydroxypropylmethylcellulose, based on 100 parts by weight of the ceramic material
7 parts by weight of an acrylic acid oligomer, 2 parts by weight or less of an acrylic acid oligomer, 3 parts by weight or less of at least one of wax, paraffin, and stearic acid, and a predetermined amount of water.
チルセルロース、カルボキシメチルセルロース、及びヒ
ドロキシプロピルメチルセルロースのうち少くとも1種
との混合比率を同じもしくは微生物起源の多糖類の方を
多く配合してなる請求項(2)記載の押出成形用セラミ
ックス材料。(3) A claim in which the polysaccharide of microbial origin and at least one of polyvinyl alcohol, methylcellulose, carboxymethylcellulose, and hydroxypropylmethylcellulose are mixed in the same ratio, or the polysaccharide of microbial origin is blended in a larger amount ( 2) The ceramic material for extrusion molding described above.
源の多糖類2〜5重量部、アクリル酸オリゴマー2重量
部以下、ワックス、パラフィン、ステアリン酸のうち少
なくとも1種を3重量部以下と所定量の水とからなる混
合物を含有する押出成形用のセラミックス材料を供給口
より供給経路内に供給し、これを供給経路の一端に設け
られた口金に向って、60kgf/cm^2以上の押出
圧力にて加圧し、前記口金より押出し、成形品を成形す
ることを特徴とする押出成形用セラミックス材料の押出
成形方法。(4) A predetermined amount of 2 to 5 parts by weight of polysaccharide of microbial origin, 2 parts by weight or less of acrylic acid oligomer, and 3 parts by weight or less of at least one of wax, paraffin, and stearic acid per 100 parts by weight of the ceramic material. A ceramic material for extrusion molding containing a mixture of water and water is supplied into the supply route from the supply port, and is heated to an extrusion pressure of 60 kgf/cm^2 or more toward the nozzle provided at one end of the supply route. 1. A method for extrusion molding a ceramic material for extrusion molding, characterized in that a molded product is formed by pressurizing the ceramic material using the die and extruding it from the die.
源の多糖類並びにポリビニルアルコール、メチルセルロ
ース、カルボキシメチルセルロース及びヒドロキシプロ
ピルメチルセルロースのうち少くとも1種の合計量2〜
7重量部、アクリル酸オリゴマー2重量部以下、ワック
ス、パラフィン、ステアリン酸のうち少なくとも1種を
3重量部以下と所定量の水とからなる混合物を含有する
押出成形用のセラミックス材料を供給口より供給経路内
に供給し、これを供給経路の一端に設けられた口金に向
って、60kgf/cm^2以上の押出圧力にて加圧し
、前記口金より押出し、成形品を成形することを特徴と
する押出成形用セラミックス材料の押出成形方法。(5) Total amount of at least one of polysaccharides of microbial origin and polyvinyl alcohol, methyl cellulose, carboxymethyl cellulose, and hydroxypropyl methyl cellulose, based on 100 parts by weight of the ceramic material, 2 to 2 parts by weight
7 parts by weight of acrylic acid oligomer, 2 parts by weight or less of acrylic acid oligomer, 3 parts by weight or less of at least one of wax, paraffin, and stearic acid, and a predetermined amount of water. The product is supplied into a supply route, pressurized with an extrusion pressure of 60 kgf/cm^2 or more toward a nozzle provided at one end of the supply route, and extruded from the nozzle to form a molded product. Extrusion molding method of ceramic material for extrusion molding.
チルセルロース、カルボキシメチルセルロース及びヒド
ロキシプロピルメチルセルロースのうち少くとも1種と
の混合比率を同じもしくは微生物起源の多糖類の方を多
く配合してなる請求項(5)記載の押出成形用セラミッ
クス材料の押出成形方法。(6) Claim (5) wherein the polysaccharide of microbial origin and at least one of polyvinyl alcohol, methyl cellulose, carboxymethyl cellulose, and hydroxypropyl methyl cellulose are mixed in the same ratio or the polysaccharide of microbial origin is blended in a larger amount. ) Extrusion molding method of the ceramic material for extrusion molding described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2158816A JPH0798688B2 (en) | 1990-06-19 | 1990-06-19 | Ceramic material for extrusion molding and extrusion molding method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2158816A JPH0798688B2 (en) | 1990-06-19 | 1990-06-19 | Ceramic material for extrusion molding and extrusion molding method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0450157A true JPH0450157A (en) | 1992-02-19 |
JPH0798688B2 JPH0798688B2 (en) | 1995-10-25 |
Family
ID=15679993
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2158816A Expired - Lifetime JPH0798688B2 (en) | 1990-06-19 | 1990-06-19 | Ceramic material for extrusion molding and extrusion molding method thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0798688B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0760039A (en) * | 1993-08-27 | 1995-03-07 | Kenko Igakushiya:Kk | Composition for ceramic filter medium and production of ceramic filter medium |
JP2001220245A (en) * | 2000-02-07 | 2001-08-14 | Kousha:Kk | Method for extrusion molding ceramic material |
KR100547256B1 (en) * | 2003-09-30 | 2006-01-26 | 한국화학연구원 | Inhibition method for dry crack of alumina green body prepared by wet forming technique |
JP2008132490A (en) * | 2007-12-17 | 2008-06-12 | Masaru Ichikawa | Method for manufacturing aromatization catalyst of lower hydrocarbon |
JP2009226583A (en) * | 2008-02-27 | 2009-10-08 | Jgc Catalysts & Chemicals Ltd | Ceramic molding clay and its manufacturing method, method of manufacturing ceramic molding using ceramic molding clay, and ceramic molding manufactured thereby |
-
1990
- 1990-06-19 JP JP2158816A patent/JPH0798688B2/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0760039A (en) * | 1993-08-27 | 1995-03-07 | Kenko Igakushiya:Kk | Composition for ceramic filter medium and production of ceramic filter medium |
JP2001220245A (en) * | 2000-02-07 | 2001-08-14 | Kousha:Kk | Method for extrusion molding ceramic material |
KR100547256B1 (en) * | 2003-09-30 | 2006-01-26 | 한국화학연구원 | Inhibition method for dry crack of alumina green body prepared by wet forming technique |
JP2008132490A (en) * | 2007-12-17 | 2008-06-12 | Masaru Ichikawa | Method for manufacturing aromatization catalyst of lower hydrocarbon |
JP2009226583A (en) * | 2008-02-27 | 2009-10-08 | Jgc Catalysts & Chemicals Ltd | Ceramic molding clay and its manufacturing method, method of manufacturing ceramic molding using ceramic molding clay, and ceramic molding manufactured thereby |
Also Published As
Publication number | Publication date |
---|---|
JPH0798688B2 (en) | 1995-10-25 |
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