JPH0628243Y2 - Ceramic extrusion equipment - Google Patents

Ceramic extrusion equipment

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Publication number
JPH0628243Y2
JPH0628243Y2 JP1989037692U JP3769289U JPH0628243Y2 JP H0628243 Y2 JPH0628243 Y2 JP H0628243Y2 JP 1989037692 U JP1989037692 U JP 1989037692U JP 3769289 U JP3769289 U JP 3769289U JP H0628243 Y2 JPH0628243 Y2 JP H0628243Y2
Authority
JP
Japan
Prior art keywords
ceramic
kneaded
flow
clay
material cylinder
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
JP1989037692U
Other languages
Japanese (ja)
Other versions
JPH02127402U (en
Inventor
勲 水谷
健治 荒井
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP1989037692U priority Critical patent/JPH0628243Y2/en
Publication of JPH02127402U publication Critical patent/JPH02127402U/ja
Application granted granted Critical
Publication of JPH0628243Y2 publication Critical patent/JPH0628243Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【考案の詳細な説明】 (産業上の利用分野) 本考案はセラミック材料の押出成形、特にセラミックハ
ニカム構造体の押出成形に好適なセラミック押出成形装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a ceramic extrusion molding apparatus suitable for extrusion molding of ceramic materials, particularly extrusion molding of ceramic honeycomb structures.

(従来の技術) 従来、セラミック材料の押出成形は、第4図に示すよう
に、真空土練機より円柱状のセラミック成形用坏土を押
出成形機1のマテリアルシリンダ3内に搬入し、次いで
油圧プランジャー8を作動させてピストン4を可動させ
てラムヘッド5によりセラミック成形用坏土を口金2方
向に押出すことが行われていた。
(Prior Art) Conventionally, in extrusion molding of a ceramic material, as shown in FIG. 4, a columnar ceramic molding material is carried into a material cylinder 3 of an extrusion molding machine 1 from a vacuum clay kneader, and then, It has been performed that the hydraulic plunger 8 is operated to move the piston 4 and the ram head 5 pushes the ceramic forming clay in the two directions of the die.

そして、あるセラミック成形用坏土バッチの押出が終了
する直前に次のセラミック成形用坏土バッチをマテリア
ルシリンダ3内に搬入して、同様に押出操作を連続して
いた。
Immediately before the extrusion of a certain ceramic forming clay batch was completed, the next ceramic forming clay batch was carried into the material cylinder 3 and the extrusion operation was continued in the same manner.

このような押出成形装置で得られるセラミック成形体あ
るいは該成形体の焼成体は、セラミック成形用坏土バッ
チにより、特にセラミックハニカム構造体を成形する場
合には、ハニカム構造体の隔壁に相当する口金の成形溝
が非常に小さいため、坏土バッチ間の影響が大きかっ
た。
A ceramic molded body or a fired body of the molded body obtained by such an extrusion molding apparatus is a die corresponding to the partition walls of the honeycomb structure, particularly when a ceramic honeycomb structure is molded by a ceramic molding clay batch. Since the forming groove of was very small, the influence between the kneaded clay batches was great.

すなわち、第5図に示すように、最初の成形した坏土バ
ッチ11と次に成形された坏土バッチ12とは押出方向には
混合されず、かつ該バッチ境界面13で不良が発生しやす
い問題があった。
That is, as shown in FIG. 5, the first formed kneaded clay batch 11 and the next formed kneaded clay batch 12 are not mixed in the extrusion direction, and a defect is likely to occur at the batch boundary surface 13. There was a problem.

このような坏土バッチ間の影響を小さくするため、アメ
リカ特許明細書第3,888,963号に開示されているよう
に、口金の直前に坏土流れ均一化装置(ホモナイザー)
としてのスクリーンを設けた押出成形機が知られてい
る。すなわち、第4図における口金2の上流側の直前
に、第6図(A),(B)にその平面図およびそのA−A′断
面図を示すような、坏土流れ方向に複数の貫通孔15を有
する坏土流れ均質化装置(ホモナイザー)16を設置し、
坏土バッチを解砕して良好なハニカム構造体を得ようと
している。
In order to reduce such an influence between the kneaded clay batches, as disclosed in U.S. Pat. No. 3,888,963, a kneaded clay flow homogenizer (homogenizer) is provided immediately before the die.
An extrusion molding machine provided with a screen is known. That is, immediately before the upstream side of the mouthpiece 2 in FIG. 4, a plurality of penetrations are made in the kneaded material flow direction as shown in the plan view and the AA ′ sectional view of FIGS. 6 (A) and 6 (B). A kneaded clay flow homogenizer (homogenizer) 16 having holes 15 is installed,
The kneaded clay batch is crushed to obtain a good honeycomb structure.

(考案が解決しようとする課題) しかしながら、上述したアメリカ特許明細書第3,888,96
3号に開示された押出成形機では、セラミック成形用坏
土バッチ間の継ぎ目は解砕されるのでバッチ間のバラツ
キを小さくする効果はあるが、バッチ間の境界における
不均一は依然として残っていた。また、通常坏土の流路
はマテリアルシリンダと口金部分では断面積が異なるの
で、坏土の流速分布が生じて、バッチ間の境界面におけ
る不均一の影響は押出成形品10〜20個に達する問題もあ
った。
(Problems to be Solved by the Invention) However, the above-mentioned US Patent Specification No. 3,888,96
In the extruder disclosed in No. 3, since the seam between the ceramic forming clay batches is crushed, it has the effect of reducing the variation between batches, but the non-uniformity at the boundary between batches still remains. . In addition, since the cross-sectional area of the material cylinder and the mouthpiece part of the kneaded clay is usually different, flow velocity distribution of the kneaded material occurs, and the influence of unevenness on the boundary surface between batches reaches 10 to 20 extruded products. There was also a problem.

本考案の目的は上述した課題を解消して、坏土バッチ間
の影響もなく良好な性状の成形品を得ることのできるセ
ラミック押出成形装置を提供しようとするものである。
An object of the present invention is to solve the above-mentioned problems and to provide a ceramic extrusion molding apparatus capable of obtaining a molded product having good properties without any influence between kneaded clay batches.

(課題を解決するための手段) 本考案のセラミック押出成形装置は、マテリアルシリン
ダと、マテリアルシリンダの端部に設けたセラミック構
造体を所定形状に押出すための口金と、マテリアルシリ
ンダ内であって口金の上流側に設けた、坏土を解砕する
ための多数の貫通孔からなる坏土流れ均質化手段とを少
なくとも具え、セラミック坏土バッチをマテリアルシリ
ンダに投入するセラミック押出成形装置において、前記
坏土流れ均質化手段の流動抵抗を外周部ほど小さくした
ことを特徴とするものである。
(Means for Solving the Problems) A ceramic extrusion molding apparatus of the present invention includes a material cylinder, a die for extruding a ceramic structure provided at an end of the material cylinder into a predetermined shape, and a material cylinder. Provided on the upstream side of the die, at least with a kneaded material flow homogenizing means consisting of a large number of through-holes for crushing the kneaded material, in the ceramic extrusion molding apparatus for charging the ceramic kneaded material batch into the material cylinder, It is characterized in that the flow resistance of the kneaded clay flow homogenizing means is made smaller toward the outer peripheral portion.

(作用) 上述した構成において、坏土流れ均質化手段の多数の貫
通孔の開口率を外周部ほど大きくしているため、中心部
に抵抗がかかることにより中央部の坏土が遅れ、次の口
金直前のしぼりによって発生する流速分布と相殺され
る。その結果、押出成形されるセラミック成形坏土バッ
チ間の境界面が押出方向に対して垂直な面に近くなるの
で、セラミック成形坏土バッチ間の不良発生率を小さく
することができる。
(Operation) In the above-mentioned configuration, since the opening ratio of the large number of through holes of the kneaded material flow homogenizing means is increased toward the outer peripheral portion, resistance is applied to the central portion, which delays the kneaded material in the central portion. It is offset by the flow velocity distribution generated by the squeezing just before the base. As a result, the boundary surface between the ceramic molded kneaded clay batches to be extruded becomes close to the surface perpendicular to the extrusion direction, so that the defect occurrence rate between the ceramic molded kneaded clay batches can be reduced.

(実施例) 第1図(A),(B)は本考案における坏土流れ均質化手段の
一例を示す平面図およびそのA−A′断面図である。本
実施例の坏土流れ均質化手段17では、坏土流れ方向の貫
通孔15をほぼ同心円状に配置するとともに、貫通孔15の
開口率を中心部より外周部に向かって徐々に大きくした
例、すなわち貫通孔15の孔径を外周部ほど大きくした例
を示している。
(Embodiment) FIGS. 1 (A) and 1 (B) are a plan view and an AA 'sectional view showing an example of a kneaded clay flow homogenizing means in the present invention. In the kneaded clay flow homogenizing means 17 of the present embodiment, the through holes 15 in the kneaded clay flow direction are arranged substantially concentrically, and the opening ratio of the through holes 15 is gradually increased from the central portion toward the outer peripheral portion. That is, an example in which the hole diameter of the through hole 15 is increased toward the outer peripheral portion is shown.

本例では、従来の坏土流れ均質化手段(ホモナイザー)
と同様に坏土の解砕が達成できるとともに、中心部と外
周部との開口率の変化により中心部に抵抗がかかり中央
部の坏土流れが遅れることにより、次の口金へ到達する
までのしぼりによって発生する流速分布を相殺できる。
In this example, the conventional clay flow homogenizing means (homogenizer)
In the same way as the kneading of the kneaded clay can be achieved, the resistance to the central part due to the change in the opening ratio between the central part and the outer peripheral part delays the flow of the kneaded material in the central part, and The flow velocity distribution generated by the squeezing can be canceled out.

すなわち、第2図に本考案の成形機のマテリアルシリン
ダの先端部を拡大して示すように、メッシュ状のスクリ
ーン18および坏土流れ均質化手段17を通過した坏土は、
図中矢印の長さを流速に対応させて表示するように、中
央部に比較して外周部ほど坏土流れが速い状態となる。
さらに、しぼり部19を通過して口金2へ到達する直前の
坏土流れは外周部に比較して中央部ほど速い状態になる
ため、坏土を坏土流れ均質化手段17を通過する前とほぼ
同じ状態で口金2へ供給することができる。なお、坏土
流れ均質化手段17の貫通孔15の孔径の開口率の変化は、
しぼり部19のしぼり状態を考慮して決定する必要があ
る。
That is, as shown in FIG. 2 in which the tip of the material cylinder of the molding machine of the present invention is enlarged, the kneaded material that has passed through the mesh-shaped screen 18 and the kneaded material flow homogenizing means 17 is
As the length of the arrow in the figure is displayed corresponding to the flow velocity, the kneaded clay flow becomes faster in the outer peripheral portion than in the central portion.
Further, since the kneading flow just before passing through the squeezing part 19 and reaching the mouthpiece 2 becomes faster in the central part as compared with the outer peripheral part, the kneading is made before the kneading of the kneading flow homogenizing means 17. It can be supplied to the base 2 in substantially the same state. The change in the opening ratio of the hole diameter of the through hole 15 of the kneaded clay flow homogenizing means 17,
It is necessary to determine in consideration of the squeezing state of the squeezing portion 19.

第3図に、上述した本考案の押出成形機により押出した
成形体のバッチ継ぎ目部分の押出方向と平行な断面を示
す。すなち、セラミック坏土バッチの後端部あるいは先
端部に顔料を塗布して境界面を調査した。その結果、第
3図に示すように、セラミック坏土バッチ21と第2のセ
ラミックバッチ22の境界面23は、従来例を示す第5図に
比べてみて、押出方向に垂直に近く、セラミック坏土の
流れが均一になっていることがわかった。
FIG. 3 shows a cross section parallel to the extrusion direction of the batch seam portion of the molded product extruded by the extrusion molding machine of the present invention described above. That is, a pigment was applied to the rear end or the front end of the ceramic kneaded clay batch to examine the boundary surface. As a result, as shown in FIG. 3, the boundary surface 23 between the ceramic kneaded clay batch 21 and the second ceramic batch 22 was closer to the vertical direction in the extrusion direction as compared with FIG. It was found that the soil flow was uniform.

本考案の装置は幾多の変形が可能である。例えば、本実
施例においては貫通孔の孔径を外周に向かって徐々に大
きくした例を示したが、均質化手段の厚みを外周部に向
かって徐々に薄くしてもよい。また、貫通孔の径は同一
で孔の数を外周に向かって徐々に多くしてもよい。
The device of the present invention can be modified in many ways. For example, in this embodiment, an example in which the hole diameter of the through hole is gradually increased toward the outer circumference has been shown, but the homogenizing means may be gradually thinned toward the outer circumference. The diameter of the through holes may be the same, and the number of holes may be gradually increased toward the outer circumference.

(考案の効果) 以上の説明から明らかなように、本考案のセラミック押
出成形装置によれば、流動抵抗を外周部ほど小さくした
坏土流れ均質化手段を使用することにより、セラミック
成形用坏土バッチ間の境界面を押出方向に対して垂直に
近くすることができ、セラミック成形用坏土バッチ間の
不良率を減少することができる。
(Effect of the Invention) As is clear from the above description, according to the ceramic extrusion molding apparatus of the present invention, by using the kneaded material flow homogenizing means having a smaller flow resistance toward the outer peripheral portion, the ceramic molding material is formed. The interface between the batches can be made nearly vertical to the extrusion direction, and the defect rate between the ceramic forming clay batches can be reduced.

【図面の簡単な説明】[Brief description of drawings]

第1図(A),(B)は本考案における坏土流れ均質化手段の
一例を示す平面図およびそのA−A′断面図、 第2図は本考案の形成機の口金部分を拡大して示す図、 第3図は本考案の押出成形機によるセラミック坏土バッ
チの押出成形体の断面図、 第4図は従来のセラミック押出成形機の正面図、 第5図は従来の押出成形機によるセラミック坏土バッチ
の押出成形体の断面図、 第6図(A),(B)は従来の坏土流れ均質化手段の一例を示
す平面図およびそのA−A′断面図てある。 15……貫通孔、17……坏土流れ均質化手段 18……スクリーン、19……しぼり部 21……セラミック坏土バッチ 22……第2のセラミック坏土バッチ 23……境界面
1 (A) and 1 (B) are a plan view showing an example of the kneaded clay flow homogenizing means in the present invention and a sectional view taken along the line AA ', and FIG. 2 is an enlarged view of the die part of the forming machine of the present invention. Fig. 3 is a sectional view of an extruded body of a ceramic kneaded clay batch produced by the extruder of the present invention, Fig. 4 is a front view of a conventional ceramic extruder, and Fig. 5 is a conventional extruder. 6A and 6B are a plan view and an AA ′ cross-sectional view showing an example of a conventional clay flow homogenizing means. 15 …… Through hole, 17 …… Pour flow homogenization means 18 …… Screen, 19 …… Squeezing part 21 …… Ceramic clay batch 22 …… Second ceramic clay batch 23 …… Boundary surface

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】マテリアルシリンダと、マテリアルシリン
ダの端部に設けたセラミック構造体を所定形状に押出す
るための口金と、マテリアルシリンダ内であって口金の
上流側に設けた、坏土を解砕するための多数の貫通孔か
らなる坏土流れ均質化手段とを少なくとも具え、セラミ
ック坏土バッチをマテリアルシリンダに投入するセラミ
ック押出成形装置において、前記坏土流れ均質化手段の
流動抵抗を外周部ほど小さくしたことを特徴とするセラ
ミック押出成形装置。
1. A material cylinder, a die for extruding a ceramic structure provided at an end of the material cylinder into a predetermined shape, and a kneaded material provided in an upstream side of the die in the material cylinder. At least a kneading flow homogenizing means consisting of a large number of through holes for, in the ceramic extrusion molding device to put the ceramic kneading batch into the material cylinder, the flow resistance of the kneading flow homogenizing means to the outer peripheral part Ceramic extrusion molding device characterized by being made smaller.
JP1989037692U 1989-03-31 1989-03-31 Ceramic extrusion equipment Expired - Lifetime JPH0628243Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1989037692U JPH0628243Y2 (en) 1989-03-31 1989-03-31 Ceramic extrusion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1989037692U JPH0628243Y2 (en) 1989-03-31 1989-03-31 Ceramic extrusion equipment

Publications (2)

Publication Number Publication Date
JPH02127402U JPH02127402U (en) 1990-10-19
JPH0628243Y2 true JPH0628243Y2 (en) 1994-08-03

Family

ID=31545037

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1989037692U Expired - Lifetime JPH0628243Y2 (en) 1989-03-31 1989-03-31 Ceramic extrusion equipment

Country Status (1)

Country Link
JP (1) JPH0628243Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100500223B1 (en) * 1999-08-30 2005-07-11 니뽄 가이시 가부시키가이샤 Corrugated wall honeycomb structure and production method thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62159604U (en) * 1986-03-31 1987-10-09

Also Published As

Publication number Publication date
JPH02127402U (en) 1990-10-19

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