JPH0815537B2 - Method and apparatus for manufacturing ceramic separation membrane - Google Patents

Method and apparatus for manufacturing ceramic separation membrane

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Publication number
JPH0815537B2
JPH0815537B2 JP8164388A JP8164388A JPH0815537B2 JP H0815537 B2 JPH0815537 B2 JP H0815537B2 JP 8164388 A JP8164388 A JP 8164388A JP 8164388 A JP8164388 A JP 8164388A JP H0815537 B2 JPH0815537 B2 JP H0815537B2
Authority
JP
Japan
Prior art keywords
electrode
separation membrane
creeping discharge
particle
producing
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
JP8164388A
Other languages
Japanese (ja)
Other versions
JPH01254212A (en
Inventor
閃一 増田
英夫 山本
Original Assignee
増田 佳子
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Application filed by 増田 佳子 filed Critical 増田 佳子
Priority to JP8164388A priority Critical patent/JPH0815537B2/en
Publication of JPH01254212A publication Critical patent/JPH01254212A/en
Publication of JPH0815537B2 publication Critical patent/JPH0815537B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/45Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
    • C04B41/50Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials
    • C04B41/5025Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials with ceramic materials
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/45Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
    • C04B41/4505Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements characterised by the method of application

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtering Materials (AREA)
  • Porous Artificial Stone Or Porous Ceramic Products (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は液体域は空気中から、その中に存在する各
種細菌等の超微粒子を分離する際に使用するための、数
十Åの超微細孔を形成せるセラミック製分離膜の製造方
法およびその製造装置に関するものである。
TECHNICAL FIELD The present invention relates to an ultrafine pore of several tens of liters for use when separating ultrafine particles of various bacteria present in the liquid region from the air. The present invention relates to a method and an apparatus for manufacturing a ceramic separation membrane for forming a ceramic.

従来の技術 上述のような数10Åの超微細孔を有するセラミック製
分離膜を作るには、従来10ナノメータ程度の粒径の揃っ
た超微粒子を規則的に配列し、それを焼成すれば得られ
ると期待されているが、実際上は不可能であった。そし
て従来のこの種のものの製造方法および製造装置はセラ
ミックの微粒子を高圧で圧縮して多孔質板を形成し、そ
の表面に溶媒を塗布して、それを焼成するものである
が、それは微細孔径の制御が難しく精密な分離膜を製造
することが困難である。
Conventional technology In order to make a ceramic separation membrane with ultra-fine pores of several tens of liters as described above, it is possible to obtain ultra-fine particles with a uniform particle size of about 10 nanometers arranged regularly and firing them. Is expected, but it was impossible in practice. In the conventional manufacturing method and manufacturing apparatus of this kind, ceramic fine particles are compressed at a high pressure to form a porous plate, a solvent is applied to the surface of the porous plate, and it is fired. Is difficult to control and it is difficult to manufacture a precise separation membrane.

発明が解決しようとする課題 この発明の目的は上述のように、従来その製作が不可
能視されていた数10Åの超微細孔を有するセラミック製
分離膜を製造する方法および装置を得ることである。
DISCLOSURE OF THE INVENTION PROBLEM TO BE SOLVED BY THE INVENTION As described above, an object of the present invention is to obtain a method and an apparatus for producing a ceramic separation membrane having ultra-fine pores of several tens of liters, which has heretofore been considered impossible to produce. .

他の目的は微粒子を焼成する際に生ずる微細孔径の制
御を容易にして、その結果として精密な分離膜を得る事
である。
Another object is to facilitate the control of the fine pore size generated when firing the fine particles, and as a result obtain a precise separation membrane.

課題を解決するための手段 この発明のセラミック製分離膜の製造方法はCVD反応
管内で生成したセラミックの超微粒子を沿面放電極と粒
子泳動用電極の間で荷電すると共に、該荷電した超微粒
子を前記両電極間に於ける該粒子泳動用電極寄りに配置
した多孔質燒結体の面に静電付着して、多孔質の超微粒
子堆積層を形成し、該超微粒子堆積層をそのままの状態
で加熱することによって、該多孔質燒結体の面に多孔質
の超微粒子燒結膜を生成することである。
Means for Solving the Problems The method for producing a ceramic separation membrane of the present invention is to charge the ultrafine particles of ceramic produced in a CVD reaction tube between a creeping discharge electrode and an electrode for particle migration, and to charge the charged ultrafine particles. Electrostatically adhered to the surface of the porous sintered body disposed near the electrode for particle migration between the both electrodes to form a porous ultrafine particle deposition layer, and the ultrafine particle deposition layer as it is By heating, a porous ultrafine particle sintered film is formed on the surface of the porous sintered body.

又この発明のセラミック製分離膜の製造装置はCVD反
応ガスの流れの上流側にCVD反応管を具備した超微粒子
生成装置、その下流側に沿面放電極と粒子泳動用電極と
からなる静電成膜装置と、焼成装置をそれぞれ配設し、
該沿面放電極をアルミナ磁器層の肉厚内に埋設した面状
誘導電極と、そのアルミナ磁器層の面に形成された線状
電極とで形成し、それら両電極の間に高周波高圧電源を
接続し、さらに前記沿面放電極と粒子泳動用電極との間
に直流高圧電源を接続したものである。
The apparatus for producing a ceramic separation membrane of this invention is an ultrafine particle generator equipped with a CVD reaction tube on the upstream side of the flow of a CVD reaction gas, and an electrostatic component consisting of a creeping discharge electrode and a particle migration electrode on the downstream side. A membrane device and a firing device are provided,
The creeping discharge electrode is formed by a planar induction electrode embedded in the thickness of the alumina porcelain layer and a linear electrode formed on the surface of the alumina porcelain layer, and a high-frequency high-voltage power supply is connected between these electrodes. Further, a direct current high voltage power source is connected between the creeping discharge electrode and the particle migration electrode.

作用 CVD反応ガスをCVD反応管を具備した超微粒子生成装置
に供給し、その中で生成したセラミックの超微粒子を静
電成膜装置に供給して、その中に設けられている沿面放
電極の沿面コロナ放電によって荷電すると共に、その沿
面放電極と粒子泳動用電極の間の直流電界で粒子泳動用
電極に向かって駆動し、予め該粒子泳動用電極の手前に
配置しておいた多孔質燒結体の表面に堆積して、多孔性
の超微粒子堆積層を形成する。その後多孔性の超微粒子
堆積層を前記多孔質燒結体の表面に堆積したままの状態
で、電気炉等の焼成装置で加熱し、多孔質の超微粒子燒
結膜を生成してセラミック製分離膜を製造するものであ
る。
Action The CVD reaction gas is supplied to the ultra-fine particle generator equipped with the CVD reaction tube, and the ultra-fine particles of the ceramic produced therein are supplied to the electrostatic film-forming device, and the creeping discharge electrode provided therein is While being charged by the surface corona discharge, it is driven toward the particle migration electrode by the DC electric field between the surface discharge electrode and the particle migration electrode, and the porous sintered body is placed in front of the particle migration electrode in advance. Deposit on the surface of the body to form a porous ultrafine particle deposition layer. After that, in a state where the porous ultrafine particle deposition layer is deposited on the surface of the porous sintered body, it is heated by a firing device such as an electric furnace to generate a porous ultrafine particle sintered film to form a ceramic separation membrane. It is manufactured.

実施例 この発明の方法および装置の実施例を添付図面によっ
て説明すると、第1図および第2図に示すごとく反応ガ
ス1の流れの上流側にCVD反応管2とヒータ3とを具備
した超微粒子生成装置4を設け、その反応ガス1をシー
スガス1aと共にCVD反応管2内に供給し、そこで発生し
た例えば窒化珪素の超微粒子pを図示のごとくビーム1b
状にして、前記超微粒子生成装置4の下流側に設けた静
電成膜装置7内の沿面放電極5と粒子泳動用電極6の間
の空間に供給する。また該沿面放電極5をアルミナ磁器
層9の内部に埋設した棒状の誘導電極10と、そのアルミ
ナ磁器層9の外面に形成されたコイル(ピッチ2〜3m
m)状の線状電極11とで形成し、それら両電極10,11の間
に高周波高圧電源12を接続し、その間に高周波高電圧
(10KHZ,15KHZ)を印加すると、沿面放電極5の表面近
傍に高密度の交流沿面コロナを発生する。この際、交流
沿面コロナには正及び負のイオンが混在しているが、沿
面放電極5と粒子泳動用電極6の間に直流高圧電源13で
直流高電圧(1.5kv〜0.5kv)を印加すると、その極性に
したがって沿面放電極5の表面近傍に正または負極性の
みの単極性イオンが取り出せ、この近傍を通過する粒子
は効率良く単極性に荷電される。荷電された超微粒子p
は前記直流電圧によるクーロン力fを受け、本装置の中
央部から放射方向に泳動し、円筒形の多孔質燒結体14の
内面に沈着し、多孔質の超微粒子堆積層15を生成する。
該円筒形燒結体14は矢印A14方向にゆっくり回転しなが
ら上または下方に連続的に移動するので、その内面に均
質な多孔質の超微粒子層15が形成される。この様にして
超微粒子層15が形成された円筒形の多孔質燒結体14はそ
の外側に設けられた焼成装置8で焼成されて互いに隣接
する超微粒子が燒結し、超微細孔を有するセラミック製
分離膜となる。この際形成される分離膜の膜厚は超微粒
子の濃度及び円筒形燒結体14の前記移動速度によって制
御される。またその分離膜の微細孔径は超微粒子の大き
さと粒子の堆積状態で制御する。
EXAMPLE An example of the method and apparatus of the present invention will be described with reference to the accompanying drawings. Ultrafine particles having a CVD reaction tube 2 and a heater 3 on the upstream side of the flow of a reaction gas 1 as shown in FIGS. 1 and 2. A generator 4 is provided, and the reaction gas 1 is supplied into the CVD reaction tube 2 together with the sheath gas 1a, and ultrafine particles p of, for example, silicon nitride generated therein are beam 1b as shown in the figure.
Then, the particles are supplied to the space between the creeping discharge electrode 5 and the particle migration electrode 6 in the electrostatic film forming device 7 provided on the downstream side of the ultrafine particle generating device 4. Further, the creeping discharge electrode 5 is embedded in the alumina porcelain layer 9 and the rod-shaped induction electrode 10 and the coil formed on the outer surface of the alumina porcelain layer 9 (pitch 2-3 m
m) shaped linear electrode 11 and a high frequency high voltage power supply 12 is connected between these electrodes 10 and 11, and a high frequency high voltage (10KHZ, 15KHZ) is applied between them, the surface of the creeping discharge electrode 5 A high-density AC creeping corona is generated in the vicinity. At this time, positive and negative ions are mixed in the AC creeping corona, but a DC high voltage (1.5 kv to 0.5 kv) is applied between the creeping discharge electrode 5 and the particle migration electrode 6 by the DC high voltage power supply 13. Then, according to the polarity, positive or negative unipolar ions only can be taken out in the vicinity of the surface of the creeping discharge electrode 5, and the particles passing through this vicinity are efficiently charged to unipolar. Charged ultrafine particles p
Receives Coulomb force f due to the DC voltage, migrates in the radial direction from the central part of the device, and is deposited on the inner surface of the cylindrical porous sintered body 14 to form a porous ultrafine particle deposition layer 15.
Since the cylindrical sintered body 14 continuously moves upward or downward while slowly rotating in the direction of arrow A14, a uniform porous ultrafine particle layer 15 is formed on the inner surface thereof. The cylindrical porous sintered body 14 on which the ultrafine particle layer 15 is formed in this manner is fired by the firing device 8 provided on the outside thereof, and the ultrafine particles adjacent to each other are fired to form a ceramic having ultrafine pores. It becomes a separation membrane. The thickness of the separation membrane formed at this time is controlled by the concentration of ultrafine particles and the moving speed of the cylindrical sintered body 14. Further, the fine pore size of the separation membrane is controlled by the size of the ultrafine particles and the state of particle accumulation.

その超微粒子の大きさはその生成条件で制御され、ま
た超微粒子堆積層15の形成過程における粒子の堆積状態
は、前記コロナ放電の際のコロナイオン密度と両電極5,
6間の直流印加電圧で制御する。
The size of the ultrafine particles is controlled by the generation conditions, and the deposition state of the particles in the process of forming the ultrafine particle deposition layer 15 is the corona ion density during the corona discharge and both electrodes 5,
Controlled by the DC voltage applied between 6.

以上本発明を第1図乃至第2図の実施例について説明
したが、本発明はそれだけに限定されるものでなく、本
発明の構成の範囲内において具体的手段を変更して実施
することも可能である。
The present invention has been described above with reference to the embodiments shown in FIGS. 1 and 2, but the present invention is not limited thereto and can be carried out by changing the concrete means within the scope of the constitution of the present invention. Is.

第3図乃至第6図に示すものはその例であり、それは
窒化珪素の超微粒子生成装置4、超微粒子の静電成膜装
置7、および超微粒子燒結膜16の焼成装置8から構成さ
れている。
An example is shown in FIGS. 3 to 6, which comprises a silicon nitride ultrafine particle generation device 4, an ultrafine particle electrostatic film forming device 7, and a baking device 8 for the ultrafine particle sintered film 16. There is.

、該焼成装置4で生成した超微粒子は石英管18内におい
て、円筒状の流れ1cになって静電成膜装置7に輸送さ
れ、沿面放電極5の表面近傍に導かれる。ここで超微粒
子ほ単極性に荷電され、沿面放電極5と粒子泳動用電極
6の間に形成された直流電界でクーロン力を受け、石英
管18の中心部に向かって泳動し、燒結体支持具17によっ
て該中心部に予め支持された円筒状多孔質燒結体14の外
面に沈着し、超微粒子堆積層15を形成する。
In the quartz tube 18, the ultrafine particles generated by the firing device 4 are transported to the electrostatic film deposition device 7 in the form of a cylindrical flow 1c and guided to the vicinity of the surface of the creeping discharge electrode 5. Here, the ultrafine particles are charged unipolarly, receive Coulomb force in the DC electric field formed between the creeping discharge electrode 5 and the particle migration electrode 6, migrate toward the center of the quartz tube 18, and support the sintered body. The ultrafine particle deposition layer 15 is formed by depositing on the outer surface of the cylindrical porous sintered body 14 previously supported in the center by the tool 17.

その後円筒状多孔質燒結体14の外面に沈着した状態の
超微粒子堆積層15を、そのままの状態で燒結装置8に移
動しそこで焼結する。
After that, the ultrafine particle deposition layer 15 deposited on the outer surface of the cylindrical porous sintered body 14 is moved to the sintering apparatus 8 as it is and sintered there.

沿面放電極5は第4図乃至第6図に示すごとく円筒状
アルミナ磁器層9で形成せる絶縁体を介して設けた線状
電極11と面状誘導電極10とで構成されている。該両電極
10,11とも厚さ0.05mm以下のタングステン製円筒状のも
ので、内側の線状電極11は第4図および第5図でで示さ
れたような形状をしている。
The creeping discharge electrode 5 is composed of a linear electrode 11 and a planar induction electrode 10 provided via an insulator formed of a cylindrical alumina porcelain layer 9 as shown in FIGS. 4 to 6. Both electrodes
Both 10 and 11 are made of tungsten and have a thickness of 0.05 mm or less, and the inner linear electrode 11 has the shape shown in FIGS. 4 and 5.

誘導電極10と線状電極11との間に電源12で高周波高電
圧を印加すると、内面の線状電極11の表面近傍に高密度
の交流沿面コロナを発生する。
When a high frequency high voltage is applied between the induction electrode 10 and the linear electrode 11 by the power source 12, a high-density AC creeping corona is generated near the surface of the linear electrode 11 on the inner surface.

交流沿面コロナには正及び負のイオンが混在している
が、線状電極11と中心部に設置された棒状の粒子泳動用
電極6の間に直流高電圧を印加すると、その極性に従っ
て沿面放電極5の表面近傍付近に正または負極正のみの
単極性イオンが取り出せ、この近傍を通過こる粒子は効
率よく単極性に荷電される。
Positive and negative ions are mixed in the AC creeping corona, but when a DC high voltage is applied between the linear electrode 11 and the rod-shaped particle migration electrode 6 installed in the center, the creeping is discharged according to the polarity. Only positive or negative positive unipolar ions can be taken out near the surface of the electrode 5, and the particles passing through this vicinity are efficiently charged to unipolar.

荷電された超微粒子は直流電界でクーロン力を受け、
本装置の中心部に向かって泳動し、円筒状の多孔質燒結
体14の外面に付着し、多孔質な粒子堆積層15を生成す
る。
The charged ultrafine particles receive Coulomb force in the DC electric field,
It migrates toward the center of this device, adheres to the outer surface of the cylindrical porous sintered body 14, and forms a porous particle deposition layer 15.

この際円筒状燒結体14は矢印A14方向にゆっくり回転
しながら上または下方に連続的に移動するので、その外
面には均質な粒子堆積層15が形成される。
At this time, the cylindrical sintered body 14 continuously moves upward or downward while slowly rotating in the direction of arrow A14, so that a uniform particle deposition layer 15 is formed on the outer surface thereof.

粒子堆積層15が形成された円筒状燒結体14はそのまま
の状態で焼成装置8に移動し、そこで焼成されて微細孔
を有するセラミック膜16ができる。
The cylindrical sintered body 14 on which the particle deposition layer 15 is formed moves to the firing device 8 as it is, and is fired there to form a ceramic film 16 having fine pores.

発明の効果 本発明は上述の通りであり、CVD法による超微粒子を
静電成膜装置のクローン力で円筒状焼結体の面に堆積
し、その状態で燒結するので、またその超微粒子の径が
揃っているため、燒結後のセラミック製分離膜の膜厚及
び極細孔径の制御が容易である。(別添参考写真1参
照)従来不可能視されていた10数Åのセラミック製分離
膜の製造が可能ですぐれた分離膜が容易に形成できる。
(別途参考写真2参照)さらに荷電された超微粒子をク
ローン力で気相中を泳働するので、その泳働度は熱泳働
度と比べて2桁以上も大きくなる。
EFFECTS OF THE INVENTION The present invention is as described above, and the ultrafine particles produced by the CVD method are deposited on the surface of the cylindrical sintered body by the clonal force of the electrostatic film deposition apparatus and sintered in that state. Since the diameters are uniform, it is easy to control the thickness and the extremely fine pore diameter of the ceramic separation membrane after sintering. (See Attachment Reference Photo 1) It is possible to manufacture ceramic separation membranes of 10 Å, which has been considered impossible in the past, and excellent separation membranes can be easily formed.
(Refer to Reference Photo 2 separately.) Further, charged ultrafine particles swim in the gas phase by the clonal force, so their swimming activity is more than two orders of magnitude higher than their thermal swimming activity.

又さらに本発明によつて得られる分離膜は苛酷な条件
下での膜分離が可能になるので、石油、製薬、食品工業
など非水系への分離膜の導入が実現し、その場合は従来
の高エネルギ消費型の蒸留に代わる可能性がある。更に
又バイオリアクタへの応用や超定温、超臨界などの新し
い分野への応用も可能となる。
Furthermore, since the separation membrane obtained according to the present invention enables the separation of the membrane under severe conditions, the introduction of the separation membrane into a non-aqueous system such as petroleum, pharmaceuticals, food industry is realized, and in that case, It may replace high energy consuming distillation. Furthermore, it can be applied to bioreactors and new fields such as super constant temperature and supercritical.

また更に超微粒子の荷電特性、動力学特性等は物質の
種類に殆んど依存しないで、この発明はアルミナを始め
として酸化チタン、ジルコニア、窒化珪素、シリカな
ど、殆んどの超微粒子に適用できる。
Further, the charging characteristics, kinetic characteristics, etc. of the ultrafine particles are almost independent of the type of substance, and the present invention can be applied to almost all ultrafine particles such as alumina, titanium oxide, zirconia, silicon nitride and silica. .

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

第1図は本発明の実施例の正面図、第2図はその要部の
拡大断面図、第3図は他の実施例の正面図、第4図は第
3図のIV−IV線部の断面図、第5図は第4図のV−V線
部の展開図、第6図は第3図の一部の拡大断面図 1……反応ガス 2……CVD反応管 4……超微粒子生成装置 5……沿面放電極 6……粒子泳動用電極 7……静電成膜装置 8……焼成装置 9……アルミナ磁器層 10……誘導電極 11……線状電極 12……高周波電圧電源 13……直流高圧電源 14……多孔質焼結体 15……超微粒子堆積層 16……超微粒子焼結膜
FIG. 1 is a front view of an embodiment of the present invention, FIG. 2 is an enlarged cross-sectional view of an essential part thereof, FIG. 3 is a front view of another embodiment, and FIG. 4 is a IV-IV line portion of FIG. Fig. 5 is a developed view of the V-V line of Fig. 4, Fig. 6 is an enlarged cross-sectional view of a part of Fig. 1 1 ... Reactive gas 2 ... CVD reaction tube 4 ... Ultra Particle generation device 5 …… Creepage discharge electrode 6 …… Particle migration electrode 7 …… Electrostatic film deposition device 8 …… Firing device 9 …… Alumina porcelain layer 10 …… Induction electrode 11 …… Linear electrode 12 …… High frequency Voltage power supply 13 …… DC high voltage power supply 14 …… Porous sintered body 15 …… Ultra fine particle deposition layer 16 …… Ultra fine particle sintered film

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】CVD反応管内で生成したセラミックの超微
粒子を沿面放電極と粒子泳動用電極の間で荷電すると共
に、該荷電した超微粒子を前記両電極間に於ける該粒子
泳動用電極寄りに配置した多孔質燒結体の面に静電付着
して、多孔質の超微粒子堆積層を形成し、該超微粒子層
をそのままの状態で加熱することによって、該多孔質燒
結体の面に多孔質の超微粒子燒結膜を生成することを特
徴とするセラミック製分離膜の製造方法
1. Ceramic ultrafine particles generated in a CVD reaction tube are charged between a creeping discharge electrode and a particle migration electrode, and the charged ultrafine particles are located between the two electrodes and close to the particle migration electrode. The surface of the porous sintered body is electrostatically adhered to the surface of the porous sintered body to form a porous ultrafine particle deposition layer, and the ultrafine particle layer is heated as it is to form a porous layer on the surface of the porous sintered body. For producing a ceramic separation membrane, characterized by producing a high quality ultra fine particle sintered membrane
【請求項2】沿面放電極がアルミナ磁器層を介して配設
された線状電極と誘導電極とからなり、また該線状電極
に対向して粒子泳動用電極を設けられていることを特徴
とする請求項1記載のセラミック製分離膜の製造方法
2. A creeping discharge electrode is composed of a linear electrode and an induction electrode arranged via an alumina porcelain layer, and a particle migration electrode is provided so as to face the linear electrode. The method for producing a ceramic separation membrane according to claim 1.
【請求項3】沿面放電極が棒状の誘導電極とその外周に
アルミナ磁器層を介して形成された線状電極とからな
り、また粒子泳動用電極が円管状に形成され、その中心
に前記沿面放電極が設けられていることを特徴とする請
求項1記載のセラミック製分離膜の製造方法
3. A creeping discharge electrode is composed of a rod-shaped induction electrode and a linear electrode formed on the outer periphery thereof through an alumina porcelain layer, and a particle migration electrode is formed in a circular tube shape, and the creeping surface is formed at the center thereof. The method for producing a ceramic separation membrane according to claim 1, wherein a discharge electrode is provided.
【請求項4】沿面放電極がアルミナ磁器製円筒の肉厚内
に埋設された面状誘導電極と、その円筒の外面に形成さ
れた線状電極とからなり、それら両電極の間に高周波高
圧電源が接続されていることを特徴とする請求項1記載
のセラミック製分離膜の製造方法
4. A creeping discharge electrode is composed of a planar induction electrode embedded in the thickness of a cylinder made of alumina porcelain and a linear electrode formed on the outer surface of the cylinder, and a high frequency high voltage is provided between these electrodes. The method for producing a ceramic separation membrane according to claim 1, wherein a power source is connected.
【請求項5】沿面放電装置が円筒形のアルミナ磁器層の
肉厚内に面状誘導電極を埋設し、その内周面に線状電極
を形成し、それら両電極の間に高周波高圧電源を接続し
たものであることを特徴とする請求項1記載のセラミッ
ク製分離膜の製造方法
5. A creeping discharge device embeds a planar induction electrode within the thickness of a cylindrical alumina porcelain layer, forms a linear electrode on its inner peripheral surface, and supplies a high-frequency high-voltage power supply between these electrodes. 2. The method for manufacturing a ceramic separation membrane according to claim 1, wherein the separation membranes are connected.
【請求項6】CVD反応ガスの流れの上流側にCVD反応管を
具備した超微粒子生成装置、その下流側に沿面放電極と
粒子泳動用電極とからなる静電成膜装置と、焼成装置を
それぞれ配設し、該沿面放電極をアルミナ磁器層の肉厚
内に埋設した面状電極と、そのアルミナ磁器層の面に形
成された線状電極とで形成し、それら両電極の間に高周
波高圧電源を接続し、さらに前記沿面放電極と粒子泳動
用電極との間に直流高圧電源を接続していることを特徴
とするセラミック製分離膜の製造装置
6. An ultrafine particle generator equipped with a CVD reaction tube on the upstream side of the flow of a CVD reaction gas, an electrostatic film forming apparatus comprising a creeping discharge electrode and a particle migration electrode, and a baking apparatus on the downstream side thereof. Each of the surface discharge electrodes is provided by embedding the creeping discharge electrode in the thickness of the alumina porcelain layer and a linear electrode formed on the surface of the alumina porcelain layer, and a high frequency wave is placed between the electrodes. A high-voltage power supply is connected, and a direct-current high-voltage power supply is connected between the creeping discharge electrode and the particle migration electrode.
【請求項7】沿面放電極が棒状誘導電極とその外周にア
ルミナ磁器層を介して形成された線状電極とからなり、
それら両電極の間に高周波高圧電源が接続されているこ
とを特徴とする請求項6記載のセラミック製分離膜の製
造装置
7. A creeping discharge electrode comprises a rod-shaped induction electrode and a linear electrode formed on the outer periphery of the rod-shaped induction electrode via an alumina porcelain layer,
A high-frequency high-voltage power supply is connected between the both electrodes, and the apparatus for producing a ceramic separation membrane according to claim 6.
【請求項8】沿面放電極がアルミナ磁器製円筒の肉厚内
に埋設された面状誘導電極と、その円筒の内面に形成さ
れた線状電極とからなり、それら両電極の間に高周波高
圧電源が接続されていることを特徴とする請求項6記載
のセラミック製分離膜の製造装置
8. A creeping discharge electrode comprises a planar induction electrode embedded in the wall thickness of a cylinder made of alumina porcelain and a linear electrode formed on the inner surface of the cylinder. 7. The apparatus for producing a ceramic separation membrane according to claim 6, wherein a power source is connected.
JP8164388A 1988-04-02 1988-04-02 Method and apparatus for manufacturing ceramic separation membrane Expired - Lifetime JPH0815537B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8164388A JPH0815537B2 (en) 1988-04-02 1988-04-02 Method and apparatus for manufacturing ceramic separation membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8164388A JPH0815537B2 (en) 1988-04-02 1988-04-02 Method and apparatus for manufacturing ceramic separation membrane

Publications (2)

Publication Number Publication Date
JPH01254212A JPH01254212A (en) 1989-10-11
JPH0815537B2 true JPH0815537B2 (en) 1996-02-21

Family

ID=13752022

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8164388A Expired - Lifetime JPH0815537B2 (en) 1988-04-02 1988-04-02 Method and apparatus for manufacturing ceramic separation membrane

Country Status (1)

Country Link
JP (1) JPH0815537B2 (en)

Also Published As

Publication number Publication date
JPH01254212A (en) 1989-10-11

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