JPH0523807B2 - - Google Patents
Info
- Publication number
- JPH0523807B2 JPH0523807B2 JP6846885A JP6846885A JPH0523807B2 JP H0523807 B2 JPH0523807 B2 JP H0523807B2 JP 6846885 A JP6846885 A JP 6846885A JP 6846885 A JP6846885 A JP 6846885A JP H0523807 B2 JPH0523807 B2 JP H0523807B2
- Authority
- JP
- Japan
- Prior art keywords
- layer
- slurry
- mold
- particles
- 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.)
- Expired - Lifetime
Links
- 239000002002 slurry Substances 0.000 claims description 45
- 239000000919 ceramic Substances 0.000 claims description 36
- 239000002245 particle Substances 0.000 claims description 30
- 229910052623 talc Inorganic materials 0.000 claims description 12
- 239000010419 fine particle Substances 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 239000000454 talc Substances 0.000 claims description 11
- 239000006082 mold release agent Substances 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 8
- 238000010304 firing Methods 0.000 claims description 5
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 4
- 239000011707 mineral Substances 0.000 claims description 4
- 235000010413 sodium alginate Nutrition 0.000 claims description 4
- 239000000661 sodium alginate Substances 0.000 claims description 4
- 229940005550 sodium alginate Drugs 0.000 claims description 4
- RYYKJJJTJZKILX-UHFFFAOYSA-M sodium octadecanoate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC([O-])=O RYYKJJJTJZKILX-UHFFFAOYSA-M 0.000 claims description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 3
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 2
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 239000012528 membrane Substances 0.000 claims description 2
- 229910003465 moissanite Inorganic materials 0.000 claims description 2
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 2
- GEIAQOFPUVMAGM-UHFFFAOYSA-N ZrO Inorganic materials [Zr]=O GEIAQOFPUVMAGM-UHFFFAOYSA-N 0.000 claims 1
- 239000011505 plaster Substances 0.000 description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 239000011148 porous material Substances 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 4
- 238000005266 casting Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000002270 dispersing agent Substances 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 1
- 229940048086 sodium pyrophosphate Drugs 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000019818 tetrasodium diphosphate Nutrition 0.000 description 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Filtering Materials (AREA)
- Producing Shaped Articles From Materials (AREA)
- Moulds, Cores, Or Mandrels (AREA)
Description
〔産業上の利用分野〕
本発明はせつこう型にセラミツク粉末泥漿を鋳
込んで複層のセラミツクフイルターを製造する方
法の改良に関する。
〔従来の技術〕
従来、酵母や酵素を使う発酵技術の分野におい
て酵母や酵素と製品、例えばアルコールを分離す
るために有機質のフイルターが使用されてきた。
しかし有機質のフイルターは耐熱性、化学的安
定性、耐久性の面で問題があり、セラミツク製の
フイルターに代替したいという要望が強い。
この分野に用いられるセラミツクフイルターは
酵母や酵素を分離するために目の大きさは非常に
小さく数ミクロン程度が要求される。しかも酵母
や酵素が通過しないように最大の孔径、すなわち
最大透過孔径が何ミクロンであるかが重要にな
る。つまりフイルターにピンホールやクラツクが
1ケ所でもあつて最大透過孔径が所定の孔径より
大きくなつていてはならない。
またセラミツクフイルターは有機フイルターよ
り厚くならざるを得ないが、ロ過に伴う圧力損失
を小さくするために出来るだけ薄いものにしなけ
ればならない。薄いものにすれば強度が弱くなる
ので、フイルター層と、フイルター層を補強する
ための層、すなわち支持体層とを一体的に組合せ
た複層のフイルターにする必要がある。
複層フイルターを構成するフイルター層は数ミ
クロンのセラミツク粒子からなる厚さ約10数ミク
ロンの薄いものであり、また支持体層は数10ミク
ロンのセラミツク粒子からなる、厚さ約1〜数mm
のものである。支持体層はこのようにフイルター
層に比べれば非常に厚いものであるが、大きい粒
径のセラミツク粒子からできているので目の大き
さが大きく、フイルター層のロ過能力を低下させ
ることはない。
上記の如き複層のセラミツクフイルターの従来
の製造方法の1つとして、まず数10ミクロンのセ
ラミツク粉末に水、その他の添加剤を加えて混練
した混練物を、例えば押出し成形し乾燥焼成して
支持体層を作り、その後該支持体層に数ミクロン
のセラミツク粉末泥漿物を塗布するか、該泥漿物
中に支持体層をドブ漬けしてセラミツク粉末泥漿
物を付着させ、乾燥焼成する方法が知られてい
る。
他の方法としては本発明出願人が既に出願(特
願昭60−15347)したようにせつこう型に泥漿物
を鋳込んだのち、脱型乾燥焼成する方法である。
この方法はせつこう型にフイルター層を形成する
ためのセラミツク泥漿物を鋳込み、一定時間静置
したのち、せつこう型に付着しなかつた余分の泥
漿物を排出する。次に支持体層を形成するための
セラミツク泥漿物を鋳込み、フイルター層と同様
の手順で支持体層を形成、乾燥し、せつこう型か
ら脱型したのち焼成するものである。
〔発明が解決しようとする問題点〕
しかし前者の製造方法は支持体層を予め焼成し
ておき、フイルター層をあとから支持体層に塗
布、またはドブ漬けするので、支持体層にセラミ
ツク泥漿物を均一に付着させることが困難であ
り、そのためピンホールやクラツクが出来やす
く、最大透過孔径がケタ違いに大きなものになる
率が多く、使用に耐えないものになりやすかつ
た。
またせつこう型にセラミツク泥漿物を鋳込む後
の方法は、成形体をせつこう型から離れやすくす
るために離型剤としてタルクを用いるが、脱型し
た際、このタルクがフイルター層表面に相当量付
着する。このタルクは融点が低いため、成形物を
焼成する前に除去する必要があるが、成形体自
体、この時点では非常に脆弱であるためタルクの
除去には非常な手間がかかるし、往往にしてフイ
ルター層に損傷を与えることになり不良率が高く
なるという欠点があつた。また離型剤として用い
るタルクの層の厚さも薄いため、せつこう型の凹
凸がそのままフイルター層に転写されてしまい層
厚が一定とならず、そのためピンホールやクラツ
クが出来、最大透過孔径が所定のものに比べ異常
に大きいものになる率も高くなるという欠点があ
つた。
〔問題点を解決するための手段〕
本発明者らはせつこう型にセラミツク泥漿物を
鋳込んで複層セラミツクフイルターを製造する方
法につき、さらに種々研究を重ねた結果、前出願
の如く単に1種類の離型剤を付着させるのではな
く、3種類の離型剤を使用して三層からなる離型
層を形成することにより、上記の欠点を解決でき
ることを見出し、本発明に到達した。
すなわち本発明の要旨はせつこう型に、第1層
には偏平状の鉱物質微粒子を、第2層にはセラミ
ツク微粒子を、第3層には透水性の有機膜を順次
付着せしめて離型層を形成し、ついで平均粒径の
異なる少なくとも2種類のセラミツク粒子の泥漿
物のうち、平均粒径の小さい粒子の泥漿物を、該
型に鋳込んで静置してその1部を該離型層を介し
て該型の内部に付着せしめ、付着していない残り
の泥漿物を排出し、次に平均粒径の大きい粒子の
泥漿物を、同様の操作で該型に鋳込んで成形体を
つくり、乾燥し脱型後成形体に付着した離型剤を
除去してから焼成することを特徴とする複層セラ
ミツクフイルターの製造法である。
本発明のせつこう型の鋳込面の第1層に用いら
れる偏平状の鉱物質微粒子はタルクまたはセリサ
イトの1μm程度の微粒子または両者の混合物であ
る。第2層に用いられるセラミツク微粒子は
TiO2、Al2O3、SiO2、SiC2、ZrO2、Si3N4、サイ
アロンのうちの1種または2種以上の混合物であ
る。第3層に用いられる透水性の有機膜はアルギ
ン酸ナトリウムまたはステアリン酸ナトリウムで
ある。
離型層の形成に用いられる各離型剤は水を加え
て泥漿物とするか、水溶液とする。第1層の形成
に用いられる泥漿物は離型剤100重量部に対して
水5000〜200000重量部、好ましくは10000〜
100000重量部である。水が5000重量部未満では濃
すぎるため第1層の層厚が一定にならず、200000
重量部を超えると層厚が薄いため、せつこう型か
らの離型が困難になる。第2層の形成に用いられ
る泥漿物は水の他に離型層の分散をよくするため
に分散剤を添加するとよい。分散剤としては塩
酸、ピロリン酸ナトリウムなどの慣用のものでよ
い。泥漿物は離型剤100重量部に対して水30〜500
重量部、好ましくは30〜100重量部混合する。水
の量が30重量部未満では泥漿物の流動性が悪く、
層厚が一定になりにくく、500重量部を超えると
濃度が薄すぎて第2層形成に時間がかかりすぎ実
用的でない。分散剤は好ましくは塩酸であり、添
加後の泥漿物のPHが約3になるようにすればよ
い。第3層の形成に用いられる離型層の水溶液の
濃度は1.0重量%以下、好ましくは0.1〜0.5重量%
である。濃度が1.0重量%を超えると溶液の粘性
が大きくなりすぎ、膜にダレを生じ膜厚が不均一
になる。
次にパイプ状のセラミツクフイルターを例にあ
げて本発明の製造方法を説明する。ただし本発明
はパイプ状フイルターに限定されるものではな
く、板状等にも適用されるものである。
鋳型として用いられる通常のせつこう型に所要
の孔、例えば12mmφの孔を設け、この型を45℃で
一定重量になるまで乾燥させる。次に乾燥したせ
つこう型の含水率を調整すると同時に、離型層を
形成するため最初にタルクまたはセリサイトある
いはそれらの混合物に水を加えて泥漿物とし、こ
の泥漿物を、乾燥せつこう型重量の10%となるよ
うに秤りとり、その全量を孔の内面に塗布する
か、あるいは孔中に流し込み、吸水着肉させる
(約10μm程度)。これによつて第1層が形成され
る。
次にセラミツク微粒子を含む泥漿物を孔中に鋳
込み、所定厚さにするのに必要な時間静置した
後、付着していない泥漿物を排出し第2層を形成
させる。
続いてアルギン酸ナトリウムまたはステアリン
酸ナトリウムの水溶液を孔中に流し込んで一定時
間静置して約10μm付着させたのち余分の水溶液
を排出し、第3層を形成させる。
以上の操作により形成される離型層の層厚は数
10〜数1000μmであるが、特に第2層の層厚は
30μm以上、好ましくは500〜700μmである。
せつこう型の孔中内面に離型層を形成したの
ち、より細かい平均粒径を有するセラミツク粒子
の泥漿物を孔中に離型層を介して内面に鋳込み、
所定時間静置して泥漿物を約15μm付着させたの
ち、付着しなかつた泥漿物を排出し、フイルター
層を形成する。続いてより粗い平均粒径を有する
セラミツク粒子の泥漿物を孔中に鋳込み、フイル
ター層と同様の操作を行い、約1〜2mm厚の支持
体層を形成することにより成形体が得られる。
なお、以上はフイルター層が1層と支持体層が
1層からなる2層の場合について述べたが、フイ
ルター層自体を複層に、あるいは支持体層を複層
にする場合、またはその両者を複層にする場合
は、上記の操作をそれぞれ繰返せばよい。
次に成形体と一体になつているせつこう型を乾
燥する。乾燥によつてせつこう型と成形体は離型
層の第1層の部分から剥離するので、成形体はせ
つこう型の孔から外部へ抜き出す。抜き出した成
形体は約100℃で十分乾燥したのち、離型層を除
去し電気炉等の加熱炉で焼成する。焼成する条件
は成形体に使用したセラミツク粒子の種類によつ
て異なるが、アルミナの場合であれば約1500℃で
2時間程度である。
焼成することによりフイルター層と支持体層は
一体的に焼結され、複層セラミツクフイルターが
得られる。
〔作 用〕
本発明の方法において、離型層として形成され
る第1層、第2層および第3層のそれぞれの役割
作用は以下の如くである。
第1層はタルクおよび/またはセリサイト微粒
子であり、従来と同様せつこう型と成形体の型離
れを良くするためのものである。
第2層はセラミツク微粒子の比較的厚い層であ
り、以下の2つの役割をする。
その1つは第1層のみを離型層とした場合に
は、離型層の厚さが薄いためせつこう型の凹凸が
成形体にそのまま転写されフイルター層の厚さが
不均一になる。しかるに第2層は比較的厚い層で
あり、このせつこう型の凹凸が第2層で吸収でき
るためフイルター層の厚さが不均一にならない。
その2はフイルター層を形成するための泥漿物
をせつこう型に鋳込んだ際、もし第2層がないと
せつこう型の吸水が激しいため該泥漿物が極く短
時間のうちに吸水付着されるため均一な薄いフイ
ルター層を形成させることが困難である。しかし
該第2層はせつこうと異なり吸水力が小さいの
で、鋳込んだフイルター層用泥漿物の付着が急激
に起こるのを防止することができる。従つてフイ
ルター層の付着厚をコントロールすることが容易
であり、しかも均一な厚さとすることができる。
第3層は透水性の有機膜であるため第2層に用
いたセラミツク微粒子がフイルター層に付着する
のを防止する。
〔実施例〕
実施例 1〜4
外径5.5cm、高さ50cmの円柱の中央に径が1.2cm
の孔のあるせつこう型40ケを用意し、これらを45
℃で3日間乾燥した。
離型層を形成する離型剤は第1層用としてタル
ク(平均粒径1μm、日本タルク社製)とセリサイ
ト(平均粒径3μm、三信鉱工社製)を用意した。
第2層としてα−Al2O3(平均粒径1μm、昭和
軽金属製)、ZrO2(平均粒径1μm、新日本金属化
学社製)およびSiC(平均粒径1μ、不二見研磨材
工業製)を用意した。
第3層用として試薬1級のアルギン酸ナトリウ
ムおよび試薬1級のステアリン酸ナトリウムを用
意した。
これらの離型剤を第1表に示す割合で水と混合
し、泥漿物または水溶液とした。
なお第2層用泥漿物には塩酸を加えてPH3に調
整した。
次にせつこう型の孔の底をゴム栓で塞いだの
ち、第1層用泥漿物を乾燥せつこう型重量の10%
秤り取り孔に注入し、全量を吸水着肉させた。そ
の後第2層用泥漿物を注入し5分間静置した後、
ゴム栓を外しせつこう型に付着しなかつた泥漿物
を排出した。再びせつこう型の孔の底にゴム栓を
した後第3層水溶液を注入し、2分間静置後、ゴ
ム栓を外し余分の水溶液を排出した。
[Industrial Field of Application] The present invention relates to an improvement in the method of manufacturing a multilayer ceramic filter by casting ceramic powder slurry into a plaster mold. [Prior Art] Conventionally, in the field of fermentation technology that uses yeast and enzymes, organic filters have been used to separate yeast and enzymes from products such as alcohol. However, organic filters have problems in terms of heat resistance, chemical stability, and durability, and there is a strong desire to replace them with ceramic filters. Ceramic filters used in this field require very small mesh sizes of several microns in order to separate yeast and enzymes. Moreover, the maximum pore diameter, that is, the maximum permeable pore diameter, is important in microns so that yeast and enzymes do not pass through. In other words, the filter must not have even one pinhole or crack and the maximum permeation pore diameter must not be larger than a predetermined pore diameter. Ceramic filters must be thicker than organic filters, but they must be made as thin as possible to reduce pressure loss due to filtration. If it is made thin, the strength will be weakened, so it is necessary to make a multi-layered filter by integrally combining a filter layer and a layer for reinforcing the filter layer, that is, a support layer. The filter layer constituting the multilayer filter is thin, about 10 microns thick, made of ceramic particles of several microns, and the support layer is made of ceramic particles of several tens of microns, about 1 to several mm thick.
belongs to. The support layer is thus much thicker than the filter layer, but since it is made of ceramic particles with a large particle size, the mesh size is large and does not reduce the filtration ability of the filter layer. . One of the conventional manufacturing methods for multi-layered ceramic filters as described above is to first knead ceramic powder of several tens of microns with water and other additives, then extrude the mixture, dry and bake it, and then support it. A known method is to form a body layer, then apply a ceramic powder slurry of several microns to the support layer, or dip the support layer in the slurry to adhere the ceramic powder slurry, and then dry and fire it. It is being Another method, as already filed by the applicant of the present invention (Japanese Patent Application No. 60-15347), is to cast the slurry into a plaster mold, then remove it from the mold and dry and fire it.
In this method, ceramic slurry to form a filter layer is cast into a plaster mold, and after allowing it to stand for a certain period of time, the excess slurry that has not adhered to the plaster mold is discharged. Next, a ceramic slurry for forming a support layer is cast, the support layer is formed in the same manner as the filter layer, dried, removed from the plaster mold, and then fired. [Problems to be solved by the invention] However, in the former manufacturing method, the support layer is fired in advance, and the filter layer is applied or soaked on the support layer afterwards, so the ceramic slurry is not applied to the support layer. It was difficult to uniformly adhere the material, and as a result, pinholes and cracks were likely to occur, and the maximum permeation pore diameter was often an order of magnitude larger, making it unusable. In addition, in the method after ceramic slurry is cast into a plaster mold, talc is used as a mold release agent to make it easier to release the molded body from the plaster mold, but when the mold is removed, this talc corresponds to the surface of the filter layer. Amount adheres. Since this talc has a low melting point, it needs to be removed before firing the molded product, but the molded product itself is extremely fragile at this point, so removing the talc requires a lot of effort and This has the disadvantage that it damages the filter layer and increases the defective rate. In addition, since the thickness of the talc layer used as a mold release agent is thin, the unevenness of the plaster mold is transferred directly to the filter layer, making the layer thickness inconsistent, resulting in pinholes and cracks, and the maximum permeable pore diameter does not reach the specified level. The disadvantage was that the probability of the product becoming abnormally large compared to the original size was also high. [Means for Solving the Problems] The present inventors have conducted various studies on the method of manufacturing a multi-layer ceramic filter by casting ceramic slurry into a plaster mold, and as a result, the inventors have developed a simple method as in the previous application. We have discovered that the above drawbacks can be solved by forming a release layer consisting of three layers using three types of release agents instead of attaching different types of release agents, and have arrived at the present invention. That is, the gist of the present invention is to sequentially attach flat mineral fine particles to the first layer, ceramic fine particles to the second layer, and water-permeable organic film to the third layer to a plaster mold, and then release the mold. A layer is formed, and then, among the slurry of at least two types of ceramic particles having different average particle diameters, the slurry of particles with a smaller average particle diameter is cast into the mold, left to stand, and a part of the slurry is separated. The slurry is adhered to the inside of the mold through the mold layer, the remaining unattached slurry is discharged, and the slurry with particles having a large average particle size is then cast into the mold in the same manner to form a molded body. This is a method for producing a multilayer ceramic filter, which is characterized in that the molded product is prepared, dried, removed from the mold, the mold release agent adhering to the molded product is removed, and then fired. The flat mineral fine particles used in the first layer of the casting surface of the plaster mold of the present invention are fine particles of about 1 μm of talc or sericite, or a mixture of both. The ceramic fine particles used in the second layer are
It is one or a mixture of two or more of TiO 2 , Al 2 O 3 , SiO 2 , SiC 2 , ZrO 2 , Si 3 N 4 , and Sialon. The water-permeable organic membrane used for the third layer is sodium alginate or sodium stearate. Each mold release agent used for forming the mold release layer is either made into a slurry by adding water or made into an aqueous solution. The slurry used to form the first layer is 5,000 to 200,000 parts by weight of water, preferably 10,000 to 100,000 parts by weight of water per 100 parts by weight of the release agent.
It is 100000 parts by weight. If the water content is less than 5,000 parts by weight, it will be too thick and the thickness of the first layer will not be constant;
If the amount exceeds parts by weight, the layer thickness will be so thin that it will be difficult to release it from the plaster mold. In addition to water, a dispersant may be added to the slurry used to form the second layer in order to improve the dispersion of the release layer. As the dispersant, conventional ones such as hydrochloric acid and sodium pyrophosphate may be used. The slurry is 30 to 500 parts water per 100 parts by weight of mold release agent.
Parts by weight, preferably 30 to 100 parts by weight, are mixed. If the amount of water is less than 30 parts by weight, the fluidity of the slurry will be poor;
It is difficult to keep the layer thickness constant, and if it exceeds 500 parts by weight, the concentration is too thin and it takes too much time to form the second layer, which is not practical. The dispersant is preferably hydrochloric acid, and the pH of the slurry after addition may be about 3. The concentration of the release layer aqueous solution used to form the third layer is 1.0% by weight or less, preferably 0.1 to 0.5% by weight.
It is. When the concentration exceeds 1.0% by weight, the viscosity of the solution becomes too high, causing sag in the film and making the film thickness non-uniform. Next, the manufacturing method of the present invention will be explained using a pipe-shaped ceramic filter as an example. However, the present invention is not limited to pipe-shaped filters, but can also be applied to plate-shaped filters. A regular plaster mold used as a casting mold is provided with a required hole, for example, a hole of 12 mm in diameter, and the mold is dried at 45° C. until it reaches a constant weight. Next, in order to adjust the moisture content of the dried plaster mold and at the same time form a release layer, water is first added to talc or sericite or a mixture thereof to form a slurry, and this slurry is then applied to the dried plaster mold. Weigh out 10% of the weight and apply the entire amount to the inner surface of the hole or pour it into the hole to absorb water and adhere to it (approximately 10 μm). This forms the first layer. Next, a slurry containing fine ceramic particles is cast into the hole and allowed to stand for a period of time necessary to obtain a predetermined thickness, and then the non-adhering slurry is discharged to form a second layer. Subsequently, an aqueous solution of sodium alginate or sodium stearate is poured into the holes and allowed to stand for a certain period of time to form an adhesion of about 10 μm, after which the excess aqueous solution is drained to form a third layer. The thickness of the release layer formed by the above operation is several times
The thickness of the second layer is 10 to several thousand μm.
It is 30 μm or more, preferably 500 to 700 μm. After forming a mold release layer on the inner surface of the hole of the plaster mold, a slurry of ceramic particles having a finer average particle size is cast into the hole through the mold release layer, and
After leaving it to stand for a predetermined period of time so that about 15 μm of slurry adheres, the unattached slurry is discharged to form a filter layer. Subsequently, a slurry of ceramic particles having a coarser average particle size is cast into the holes, and the same operation as for the filter layer is performed to form a support layer with a thickness of about 1 to 2 mm, thereby obtaining a molded body. In addition, the case where the filter layer is one layer and the support layer is two layers has been described above, but when the filter layer itself is multilayered, the support layer is multilayered, or both. When creating multiple layers, repeat the above operations for each layer. Next, the plaster mold integrated with the molded body is dried. Due to drying, the plaster mold and the molded body are separated from the first layer of the mold release layer, so that the molded body is pulled out from the hole of the plaster mold. After the extracted molded body is sufficiently dried at about 100°C, the release layer is removed and fired in a heating furnace such as an electric furnace. The firing conditions vary depending on the type of ceramic particles used in the molded body, but in the case of alumina, the firing conditions are about 1500°C for about 2 hours. By firing, the filter layer and the support layer are sintered integrally, and a multilayer ceramic filter is obtained. [Function] In the method of the present invention, the roles and functions of each of the first layer, second layer and third layer formed as a mold release layer are as follows. The first layer is made of talc and/or sericite fine particles, and is used to improve the separation between the plaster mold and the molded body, as in the conventional method. The second layer is a relatively thick layer of ceramic particles that serves two purposes. One of them is when only the first layer is used as a mold release layer, since the thickness of the mold release layer is thin, the plaster-like irregularities are directly transferred to the molded product, resulting in an uneven thickness of the filter layer. However, the second layer is a relatively thick layer, and since the plaster-like irregularities can be absorbed by the second layer, the thickness of the filter layer does not become non-uniform. Part 2 is that when the slurry to form the filter layer is cast into a plaster mold, if there is no second layer, the plaster mold will absorb water so intensely that the slurry will absorb water and stick to the mold in a very short time. Therefore, it is difficult to form a uniform thin filter layer. However, unlike plaster, the second layer has a low water absorption ability, so it is possible to prevent the cast slurry for the filter layer from adhering rapidly. Therefore, it is easy to control the deposited thickness of the filter layer, and the thickness can be made uniform. Since the third layer is a water-permeable organic film, it prevents the ceramic fine particles used in the second layer from adhering to the filter layer. [Example] Examples 1 to 4 A cylinder with an outer diameter of 5.5 cm and a height of 50 cm has a diameter of 1.2 cm in the center.
Prepare 40 plaster molds with 45 holes, and
It was dried at ℃ for 3 days. As mold release agents for forming the mold release layer, talc (average particle size 1 μm, manufactured by Nippon Talc Co., Ltd.) and sericite (average particle size 3 μm, manufactured by Sanshin Koko Co., Ltd.) were prepared for the first layer. As the second layer, α-Al 2 O 3 (average particle size 1 μm, manufactured by Showa Light Metal), ZrO 2 (average particle size 1 μm, manufactured by Shin Nippon Metal Chemical Co., Ltd.), and SiC (average particle size 1 μm, manufactured by Fujimi Abrasives Industry Co., Ltd.) were used. ) was prepared. For the third layer, sodium alginate, a first class reagent, and sodium stearate, a first class reagent, were prepared. These mold release agents were mixed with water in the proportions shown in Table 1 to form a slurry or an aqueous solution. The slurry for the second layer was adjusted to pH 3 by adding hydrochloric acid. Next, after sealing the bottom of the hole in the plaster mold with a rubber stopper, apply the slurry for the first layer at 10% of the weight of the dry plaster mold.
It was poured into the weighing hole and the entire amount was absorbed into the meat. After that, after pouring the slurry for the second layer and leaving it for 5 minutes,
The rubber stopper was removed and the slurry that did not adhere to the plaster mold was discharged. A rubber plug was again placed at the bottom of the plaster-shaped hole, and the third layer aqueous solution was injected. After standing for 2 minutes, the rubber plug was removed and the excess aqueous solution was drained.
【表】
第2表に上記で使用した離型剤の組合せを示し
た。[Table] Table 2 shows the combinations of the mold release agents used above.
本発明は分離過用の複層セラミツクフイルタ
ーを製造するにあたり、せつこう型に第1層、第
2層、第3層の三層からなる離型層を形成させる
ことにより、所望の最大透過孔径を得られるよう
にしたものである。すなわち従来、所望の最大透
過孔径が得られるようにフイルター層用、支持体
層セラミツク微粒子材料を用意しても、離型剤に
適したものがなかつたため、せつこう型の凹凸が
転写されたり、ピンホールやクラツクの発生原因
になつたり、離型剤タルクを除去する際に成形体
に損傷を与えてしまつていたが、本発明ではこれ
らの全てを解消することができた。
In manufacturing a multi-layer ceramic filter for separation, the present invention forms a release layer consisting of three layers, a first layer, a second layer, and a third layer, on a plaster mold, thereby achieving a desired maximum permeation pore diameter. It is designed so that you can obtain In other words, in the past, even if ceramic fine particle materials for the filter layer and the support layer were prepared to obtain the desired maximum permeation pore diameter, there was no suitable release agent, so plaster-type irregularities were transferred, This caused pinholes and cracks, and damaged the molded product when removing the mold release agent talc, but the present invention has been able to eliminate all of these problems.
Claims (1)
粒子を、第2層にはセラミツク微粒子を、第3層
には透水性の有機膜を順次付着せしめて離型層を
形成し、ついで平均粒径の異なる少なくとも2種
類のセラミツク粒子の泥漿物のうち、平均粒径の
小さい粒子の泥漿物を、該型に鋳込んで静止して
その1部を該離型層を介して該型の内部に付着せ
しめ、付着していない残りの泥漿物を排出し、次
に平均粒径の大きい粒子の泥漿物を、同様の操作
で該型に鋳込んで成形体をつくり、乾燥し脱型
後、成形体に付着した離型剤を除去してから焼成
することを特徴とする複層セラミツクフイルター
の製造法。 2 偏平状の鉱物質微粒子がタルクおよび/また
はセリサイトの微粒子である特許請求の範囲第1
項記載の製造法。 3 第2層に用いるセラミツク微粒子がTiO2、
Al2O3、SiO2、SiC、ZrO2、Si3N4、サイアロン
のうちの1種または2種以上である特許請求の範
囲第1項記載の製造法。 4 透水性の有機膜がアルギン酸ナトリウムまた
はステアリン酸ナトリウムの水溶液によつて成形
されたものである特許請求の範囲第1項記載の製
造法。[Scope of Claims] 1 A plaster-shaped structure, in which flat mineral particles are adhered to the first layer, ceramic particles are attached to the second layer, and a water-permeable organic film is attached to the third layer in order, and then separated. After forming a mold layer, a slurry of at least two types of ceramic particles having different average particle diameters, a slurry of particles with a smaller average particle size, is poured into the mold and kept stationary, and a part of the slurry is separated. The slurry is adhered to the inside of the mold through the mold layer, the remaining unattached slurry is discharged, and the slurry with particles having a large average particle size is then cast into the mold in the same manner to form a molded body. 1. A method for producing a multilayer ceramic filter, which comprises preparing a molded product, drying it, demolding it, removing a mold release agent attached to the molded product, and then firing it. 2. Claim 1, wherein the flat mineral fine particles are fine particles of talc and/or sericite.
Manufacturing method described in section. 3 The ceramic fine particles used in the second layer are TiO 2 ,
The manufacturing method according to claim 1, wherein one or more of Al 2 O 3 , SiO 2 , SiC, ZrO 2 , Si 3 N 4 , and Sialon is used. 4. The manufacturing method according to claim 1, wherein the water-permeable organic membrane is formed from an aqueous solution of sodium alginate or sodium stearate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6846885A JPS61227813A (en) | 1985-04-02 | 1985-04-02 | Production of plurally layered ceramic filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6846885A JPS61227813A (en) | 1985-04-02 | 1985-04-02 | Production of plurally layered ceramic filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61227813A JPS61227813A (en) | 1986-10-09 |
| JPH0523807B2 true JPH0523807B2 (en) | 1993-04-05 |
Family
ID=13374546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6846885A Granted JPS61227813A (en) | 1985-04-02 | 1985-04-02 | Production of plurally layered ceramic filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61227813A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6487565A (en) * | 1987-09-30 | 1989-03-31 | Tokai Konetsu Kogyo Kk | Method for casting sic-c based material |
| JPH0832291B2 (en) * | 1989-07-28 | 1996-03-29 | トヨタ自動車株式会社 | Filter for particulate collection |
| JP4879210B2 (en) * | 2008-03-14 | 2012-02-22 | 日本碍子株式会社 | Manufacturing method of multilayer ceramic filter |
-
1985
- 1985-04-02 JP JP6846885A patent/JPS61227813A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61227813A (en) | 1986-10-09 |
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