JPH034512B2 - - Google Patents
Info
- Publication number
- JPH034512B2 JPH034512B2 JP15606985A JP15606985A JPH034512B2 JP H034512 B2 JPH034512 B2 JP H034512B2 JP 15606985 A JP15606985 A JP 15606985A JP 15606985 A JP15606985 A JP 15606985A JP H034512 B2 JPH034512 B2 JP H034512B2
- Authority
- JP
- Japan
- Prior art keywords
- pores
- porous
- silicon nitride
- honeycomb
- gel
- 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
Links
- 239000011148 porous material Substances 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 11
- 229910052573 porcelain Inorganic materials 0.000 claims description 10
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 8
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 claims description 8
- 239000013078 crystal Substances 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 5
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 239000011863 silicon-based powder Substances 0.000 claims description 3
- 238000010304 firing Methods 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 241000264877 Hippospongia communis Species 0.000 description 10
- 238000000855 fermentation Methods 0.000 description 10
- 230000004151 fermentation Effects 0.000 description 10
- 108090000790 Enzymes Proteins 0.000 description 9
- 102000004190 Enzymes Human genes 0.000 description 9
- 239000000243 solution Substances 0.000 description 7
- 239000000835 fiber Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-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
- 244000005700 microbiome Species 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 229910020068 MgAl Inorganic materials 0.000 description 2
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000011358 absorbing material Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 239000000679 carrageenan Substances 0.000 description 2
- 229920001525 carrageenan Polymers 0.000 description 2
- 229940113118 carrageenan Drugs 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 238000001000 micrograph Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 229910052596 spinel Inorganic materials 0.000 description 2
- 239000011029 spinel Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 1
- 108010093096 Immobilized Enzymes Proteins 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 208000034809 Product contamination Diseases 0.000 description 1
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 235000010418 carrageenan Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 1
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- DVQHRBFGRZHMSR-UHFFFAOYSA-N sodium methyl 2,2-dimethyl-4,6-dioxo-5-(N-prop-2-enoxy-C-propylcarbonimidoyl)cyclohexane-1-carboxylate Chemical compound [Na+].C=CCON=C(CCC)[C-]1C(=O)CC(C)(C)C(C(=O)OC)C1=O DVQHRBFGRZHMSR-UHFFFAOYSA-N 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 description 1
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はバイオリアクター、材、吸音材、断
熱材或は散気管等として利用し得る多孔質磁器構
造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 porous porcelain structure that can be used as a bioreactor, a material, a sound absorbing material, a heat insulating material, an aeration tube, or the like.
(従来の技術)
微生物、酵素などの固定化法として、担体結合
法、架橋法、包括法、複合法等各種の方法があげ
られるが、この中で包括法は格子型とマイクロカ
プセル型に分けられる。(Prior art) There are various methods for immobilizing microorganisms, enzymes, etc., such as carrier binding method, crosslinking method, entrapping method, and composite method. It will be done.
格子型は酵素をゲルの格子の中に包み込む方式
で、セラミツクは耐薬品性、耐微生物不活性等の
長所があるので、ゲル格子の保持体としてセラミ
ツク多孔体が使用されつつある。 The lattice type is a method in which the enzyme is wrapped in a gel lattice, and ceramic porous bodies are increasingly being used as a holder for the gel lattice because ceramic has advantages such as chemical resistance and microbial resistance.
(発明が解決しようとする問題点)
ところで従来の技術に於てはゲルの強度が不足
したり、或いはセラミツク多孔体のゲルの保持力
が不足したりすることが原因で酵素、菌体等が流
出し、製品の汚染、収率の低下、製造コストの上
昇などの問題があつた。(Problems to be solved by the invention) However, in the conventional technology, enzymes, bacterial cells, etc. There were problems such as spillage, product contamination, reduced yields, and increased manufacturing costs.
(問題点を解決しようとするための手段)
本発明は上記の問題点を解決するために鋭意検
討の結果なされたもので、多孔質磁器内に窒化硅
素の繊維状結晶を形成させることについての着想
に基づき、先づ多孔質磁器を製造し、その空孔部
分に硅素粉末を充填し、次にこれを水素と窒素の
混合ガス雰囲気中で焼成し、空孔内に窒化硅素の
繊維状結晶を形成させることに成功し、従来技術
の問題点を克服したものである。(Means for Solving the Problems) The present invention was made as a result of intensive studies to solve the above problems, and is a method for forming fibrous crystals of silicon nitride in porous porcelain. Based on the idea, we first manufactured porous porcelain, filled the pores with silicon powder, and then fired it in a mixed gas atmosphere of hydrogen and nitrogen to create fibrous crystals of silicon nitride in the pores. This technology succeeded in forming a 100% polyurethane, overcoming the problems of the prior art.
(作用)
上記本発明によれば多孔質磁器の空孔内が所望
の活性ある窒化硅素の繊維状結晶(ウイスカー)
によつて充填されているので、ゲルが繊維によつ
て強固に空孔内に固定されるようになり、微生物
酵素等の流出量を大幅に低減させることができ
る。(Function) According to the present invention, the pores of porous porcelain contain desired active fibrous crystals (whiskers) of silicon nitride.
Since the pores are filled with fibers, the gel is firmly fixed in the pores by the fibers, and the amount of microbial enzymes etc. that flows out can be significantly reduced.
実施例 1
硅素粉末(試薬1級200メツシユパス)… 300g
第3級ブチルアルコール… 240ml
ヒドロキシプロピルセルロース(HPS−SL日本
曹達製)… 3g
以上を内容積1のアルミナ磁器ポツトミルに
入れ、(15mmφ99.9%アルミナ球石1Kg使用)72時
間粉砕混合する。このようにして得られたスラリ
ーをビーカーに移し、その中へアルミナ多孔質磁
器(平均気孔径70μm、気孔率62%、サイズ50mm
×80mm×5mm)を浸す。Example 1 Silicon powder (1st grade reagent 200 mesh pass)...300g Tertiary butyl alcohol...240ml Hydroxypropyl cellulose (HPS-SL manufactured by Nippon Soda)...3g More than this were put into an alumina porcelain pot mill with an internal volume of 1 (15mmφ99.9 % alumina coccule (1 kg)) Grind and mix for 72 hours. Transfer the slurry obtained in this way to a beaker and pour into it alumina porous porcelain (average pore diameter 70 μm, porosity 62%, size 50 mm).
×80mm×5mm).
ビーカーを真空脱泡機にかけ、多孔体内の空気
を除去した後大気圧に戻しスラリーを気孔に浸透
させる。 The beaker is placed in a vacuum deaerator to remove the air inside the porous body, and then returned to atmospheric pressure to allow the slurry to permeate into the pores.
このようにして得られた物を窒素ガス60容量
%、水素ガス40容量%の混合ガス雰囲気中で温度
1380℃、1時間の条件で焼成した。焼成品は第1
図〜第3図の(顕微鏡写真)で示すように空孔内
部には微細な窒化硅素繊維が生成充満している。
(各図の倍率×200、×500、×2000)
従つてゲルが繊維によつてしつかりと気孔に固
定されるようになり、微生物、酵素などの流出量
を大幅に低減させることができる。 The product obtained in this way was heated in a mixed gas atmosphere of 60% by volume of nitrogen gas and 40% by volume of hydrogen gas.
It was fired at 1380°C for 1 hour. Baked products are the first
As shown in (micrographs) in Figures to Figure 3, the insides of the pores are filled with fine silicon nitride fibers.
(Magnification of each figure: ×200, ×500, ×2000) Therefore, the gel is firmly fixed in the pores by the fibers, and the amount of microorganisms, enzymes, etc. that leak out can be significantly reduced.
実施例 2
スピネル(MgAl2O4)材料でハニカムを成形
し、酵素の固定化及び醗酵テストを行つた。Example 2 A honeycomb was formed using spinel (MgAl 2 O 4 ) material, and enzyme immobilization and fermentation tests were conducted.
(1) ハニカム構造体の生成焼成
スピネル(MgAl2O4:岩谷化学) 1000g
ポリビニルアルコール 100g
水 500ml
以上を、ニーダで1時間溶解混合し、ペース
トとなす。(1) Creation and firing of honeycomb structure Spinel (MgAl 2 O 4 : Iwatani Chemical) 1000g polyvinyl alcohol 100g water 500ml or more are dissolved and mixed in a kneader for 1 hour to form a paste.
これを簡易押出成形機(手動式)にセツト
し、ドライアイスにて氷点下−15℃に冷却され
た灯油槽中へ押出し、凍結させる。 This is set in a simple extrusion molding machine (manual type), extruded into a kerosene bath cooled to -15°C below freezing with dry ice, and frozen.
ハニカム成形体の寸法は第4図に示したよう
に長さ100mm、直径50φmm、ピツチ3mm、肉厚
0.5mmである。 The dimensions of the honeycomb molded body are as shown in Figure 4: length 100mm, diameter 50φmm, pitch 3mm, wall thickness.
It is 0.5mm.
凍結した成形体2個を冷凍乾燥機に入れ6時
間乾燥させる。 The two frozen molded bodies are placed in a freeze dryer and dried for 6 hours.
乾燥品を、温度1680℃で2時間電気炉にて焼
成する。 The dried product is fired in an electric furnace at a temperature of 1680°C for 2 hours.
焼成体は気孔率60%、平均気孔30μの多孔質
体である。 The fired body is a porous body with a porosity of 60% and an average pore size of 30μ.
なお寸法は、成形時点と変りなかつた。 Note that the dimensions remained the same as at the time of molding.
(2) 硅素の含浸、焼付処理
実施例1と同様の、硅素スラリー並びに含浸
方法にて、焼成品の一方を処理し、同様の条件
で焼付処理をした。(2) Silicon impregnation and baking treatment One of the fired products was treated using the same silicon slurry and impregnation method as in Example 1, and baked under the same conditions.
このものは、気孔の中に窒化硅素繊維が形成
された組織構造をなしている。 This material has a tissue structure in which silicon nitride fibers are formed in pores.
(3) 酵素の固定化
K−カラギーナン 35g
水 1000ml
以上を混合して80℃に加熱し溶解させた後放
冷する。(3) Enzyme immobilization Mix 35 g of K-carrageenan and 1000 ml or more of water, heat to 80°C to dissolve, and then allow to cool.
別に清酒酵母懸濁水液15mlを用意し前記カラ
ギーナン溶液と混合する。 Separately, prepare 15 ml of a sake yeast suspension and mix it with the carrageenan solution.
この混合液に2種類のハニカムをひたし真空
脱泡して空気を排除し、その後大気圧にもどし
気孔に溶液を含浸させる。 Two types of honeycombs are immersed in this mixed solution, vacuum degassed to remove air, and then the pressure is returned to atmospheric pressure to impregnate the pores with the solution.
一方、1.5%KCl溶液2000ml用意し、前記ハ
ニカムを、この溶液にひたし含浸溶液をゲル化
させる。 On the other hand, prepare 2000 ml of 1.5% KCl solution and soak the honeycomb in this solution to gel the impregnating solution.
こうして得られた酵母固定化ゲルを1500mlの
培養液へひたし30℃で5日間培養する。 The yeast-immobilized gel thus obtained was soaked in 1500 ml of culture solution and cultured at 30°C for 5 days.
こうしてハニカム状固定化酵母ゲルが得られ
る。 In this way, a honeycomb-shaped immobilized yeast gel is obtained.
(4) アルコール醗酵テスト
第5図に示すような、醗酵装置を用いグルコ
ースを主体とした醗酵液300mlを入れ醗酵テス
トを行つた。(4) Alcohol fermentation test A fermentation test was carried out using a fermentation apparatus as shown in Figure 5 by adding 300 ml of a fermentation liquid containing glucose as the main ingredient.
装置の概略は第5図に於てハニカム構造体1
を装置2内に取り付ける。装置2の上部にはコ
ンデンサー3が付されており、冷却水を矢印方
向に流して冷却するようになつている。又装置
2の上側より下端に向つて醗酵液が循環するよ
うパイプで接続され、その中間には恒温水槽5
と接続されている熱交換器4、循環ポンプ6か
順次設けられている。又、装置2の下部は空気
ポンプ7とも接続されている。又、醗酵液の装
置2内での上方への流速はtcm/secにしてパ
イプ内の流速は4300ml/minとしてある。 The outline of the device is shown in Fig. 5.
is installed in the device 2. A condenser 3 is attached to the upper part of the device 2, and cooling water is caused to flow in the direction of the arrow for cooling. In addition, the device 2 is connected with a pipe so that the fermentation liquid circulates from the upper side to the lower end, and a constant temperature water tank 5 is installed in the middle.
A heat exchanger 4 and a circulation pump 6 are provided in this order. The lower part of the device 2 is also connected to an air pump 7. Further, the upward flow rate of the fermentation liquid in the device 2 is tcm/sec, and the flow rate in the pipe is 4300 ml/min.
この装置を用いた醗酵テストの結果を示せば
第6図に示すとおりである。 The results of a fermentation test using this apparatus are shown in FIG.
これによれば本発明によるものは高いアルコ
ール濃度が短期間に得られるのに対し、比較的
として示した無処理のものはアルコール生成率
が低下しており、ハニカム構造体を調べたとこ
ろ、本発明に係るものではハニカムセルに閉塞
は全く認められなかつたが比較例のものは固定
化ゲルが気孔から剥離し、ハニカムセルの一部
を閉塞していることが認められた。 According to this, the honeycomb structure according to the present invention can obtain a high alcohol concentration in a short period of time, whereas the untreated one shown as a comparative example has a lower alcohol production rate. In the case of the invention, no blockage was observed in the honeycomb cells, but in the case of the comparative example, it was observed that the immobilized gel had peeled off from the pores and partially blocked the honeycomb cells.
本発明の実施に当つては多孔質磁器の素材の種
類は上記アルミナに限定されるものではなく、チ
タニア、シリカ、ジルコニア等も適宜選択実施す
ることができる。 In carrying out the present invention, the material of the porous porcelain is not limited to the above-mentioned alumina, and titania, silica, zirconia, etc. may also be selected as appropriate.
発明の効果
本発明によるときは多孔質磁器に対し極めて簡
単な方法で窒化硅素の繊維状結晶を空孔内に生成
させ得るとともに、製造された製品は従来の単な
る多孔質磁器の有する空孔内表面積に比べ繊維状
結晶の有する表面積の著るしい増加が見られるこ
と及び繊維状結晶の有する格子欠陥等により吸着
特性結合特性等の優れた多孔質担体を提供するも
のであり、担体自体寸法安定性、細菌への安定
性、PH変化や溶液の科学的侵食に対する安定性、
熱的安定性、劣化した酵素の高温燃焼再利用を可
能ならしめること、固定化された酵素の活性度の
長期安定性など優れた性能を発揮し得るものであ
る。なお、酵素の外、微生物、生化学物質の分離
精製、微生物の固定化をなし得るとともに、他の
応用例として反応管、材、吸音材、断熱材、散
気管等広い分野に対しても応用可能なことは云う
までもない。Effects of the Invention According to the present invention, fibrous crystals of silicon nitride can be generated in the pores of porous porcelain by an extremely simple method, and the manufactured product can be produced in the pores of the conventional simple porous porcelain. The remarkable increase in the surface area of fibrous crystals compared to the surface area and the lattice defects of fibrous crystals provide a porous carrier with excellent adsorption and binding properties, and the carrier itself is dimensionally stable. stability, stability against bacteria, stability against PH changes and chemical attack of the solution,
It can exhibit excellent performance such as thermal stability, enabling reuse of degraded enzymes by high-temperature combustion, and long-term stability of the activity of immobilized enzymes. In addition to enzymes, it can be used to separate and purify microorganisms, biochemical substances, and immobilize microorganisms, and can also be applied to a wide range of fields such as reaction tubes, materials, sound absorbing materials, heat insulation materials, and aeration pipes. Needless to say, it is possible.
第1図〜第3図は窒化硅素繊維の形状を示す顕
微鏡写真。第4図はテストに用いるハニカム構造
体の寸法の斜視図、第5図はアルコール醗酵テス
ト装置の簡略説明図、第6図は醗酵テスト結果の
グラフである。
1……ハニカム構造体、2……装置、3……コ
ンデンサー、4……熱交換器、5……恒温水槽、
6……循環ポンプ、7……空気ポンプ。
Figures 1 to 3 are micrographs showing the shape of silicon nitride fibers. FIG. 4 is a perspective view of the dimensions of the honeycomb structure used in the test, FIG. 5 is a simplified illustration of the alcohol fermentation test apparatus, and FIG. 6 is a graph of the fermentation test results. 1... Honeycomb structure, 2... Device, 3... Condenser, 4... Heat exchanger, 5... Constant temperature water tank,
6...Circulation pump, 7...Air pump.
Claims (1)
水素と窒素混合ガス雰囲気中で焼成することによ
り、空孔内に窒化硅素の繊維状結晶を形成させる
ことを特徴とする多孔質磁器構造体の製造方法。1 Fill the pores of porous porcelain with silicon powder,
A method for manufacturing a porous ceramic structure, characterized by forming fibrous crystals of silicon nitride in pores by firing in a hydrogen and nitrogen mixed gas atmosphere.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15606985A JPS6221769A (en) | 1985-07-17 | 1985-07-17 | Manufacture of porous ceramic structure |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15606985A JPS6221769A (en) | 1985-07-17 | 1985-07-17 | Manufacture of porous ceramic structure |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6221769A JPS6221769A (en) | 1987-01-30 |
JPH034512B2 true JPH034512B2 (en) | 1991-01-23 |
Family
ID=15619620
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15606985A Granted JPS6221769A (en) | 1985-07-17 | 1985-07-17 | Manufacture of porous ceramic structure |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6221769A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2684427B2 (en) * | 1989-09-19 | 1997-12-03 | 株式会社日立製作所 | Composite ceramic structure |
JP3769739B2 (en) * | 1994-11-17 | 2006-04-26 | 住友電気工業株式会社 | Porous ceramic film and manufacturing method thereof |
US5709943A (en) * | 1995-05-04 | 1998-01-20 | Minnesota Mining And Manufacturing Company | Biological adsorption supports |
-
1985
- 1985-07-17 JP JP15606985A patent/JPS6221769A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6221769A (en) | 1987-01-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100363482C (en) | Method for immobilizing lipase using microstructure in hydrophilic/ hydrophobic composite membrane | |
EP2133136B1 (en) | Method for production of a separation membrane | |
US4693983A (en) | Reactor for cultivating biological material such as immobilized cells | |
US5071747A (en) | Porous polymeric support containing biological cells in interconnected voids | |
WO1995035153A3 (en) | Mass transfer method and apparatus | |
ES2688036T3 (en) | Aerated biofilm reactor fiber membrane | |
US6245698B1 (en) | Process for making porous ceramic composites with a bimodal pore size distribution | |
US4980062A (en) | Inorganic membrane | |
Ren et al. | Multiscale immobilized lipase for rapid separation and continuous catalysis | |
JPH034512B2 (en) | ||
CN113624048A (en) | Porous ceramic with straight-hole gradient structure, capillary core and preparation method of porous ceramic | |
JP3770504B2 (en) | Zeolite membrane and method for producing the same | |
RU96103625A (en) | FLOATING TURBULIZABLE MEDIA CARRIER FOR BIOTECHNOLOGICAL PROCESSES | |
JP3905461B2 (en) | Method for producing zeolite membrane | |
Fu et al. | Enzyme catalytic membrane based on a hybrid mesoporous membrane | |
EP0086179B1 (en) | Capillary filter consisting of semipermeable membrane with enzymatic activity, process for its manufacture and its applications | |
US20140374355A1 (en) | Pretreatment device for membrane separation, membrane separating system and membrane separating method | |
JP2002018247A (en) | Method for manufacturing mixture separation membrane apparatus and mixture separation membrane apparatus | |
JP2884622B2 (en) | Manufacturing method of structured catalyst support | |
EP0267470A1 (en) | Porous glass fiber mats for attachment of cells and biologically active substances | |
JPH0123162B2 (en) | ||
RU2114175C1 (en) | Method of nucleic acid cloning | |
JPH0633191B2 (en) | Ceramic sintered body with large porosity and method for producing the same | |
US6709589B1 (en) | Dimensionally stable, cross-flow permeable fluid treatment element | |
JPS62134089A (en) | Bioreactor element and production thereof |