JPH0787896B2 - Solid electrolyte membrane deposition equipment - Google Patents
Solid electrolyte membrane deposition equipmentInfo
- Publication number
- JPH0787896B2 JPH0787896B2 JP10768789A JP10768789A JPH0787896B2 JP H0787896 B2 JPH0787896 B2 JP H0787896B2 JP 10768789 A JP10768789 A JP 10768789A JP 10768789 A JP10768789 A JP 10768789A JP H0787896 B2 JPH0787896 B2 JP H0787896B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte membrane
- solid electrolyte
- porous substrate
- reaction
- electrode
- 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
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Description
【発明の詳細な説明】 [産業上の利用分野] この発明は、固体電解質膜堆積装置、特に、従来のEVD
法に基づく装置において、固体電解質膜を高速度で堆積
し得る固体電解質膜堆積装置に関するものである。The present invention relates to a solid electrolyte membrane deposition apparatus, and in particular to a conventional EVD.
The present invention relates to a solid electrolyte membrane deposition apparatus capable of depositing a solid electrolyte membrane at high speed in a method-based apparatus.
[従来の技術] 第3図は、例えば、ウエスチングハウス社(Westinghou
se Electric Corporation)のエイ・オー・アイゼンベ
ルグ(A・O・Isenberg)により発明されたEVD法ESS S
ymp.Electrode Materials Processes Energy Conver.Sc
orage 77−6(1977)P.572)の概略図である。[Prior Art] FIG. 3 shows, for example, Westinghouse.
se Electric Corporation) EVD method ESS S invented by AO Isenberg
ymp.Electrode Materials Processes Energy Conver.Sc
orage 77-6 (1977) P.572).
図において、符号(1)は石英ガラス製反応管、(2)
はグラファイト製反応管、(3)はハロゲン材料(4)
を含むグラファイト管、(5)は繊維状グラファイトプ
ラグ、(6)は穴のあいたグラファイトプラグ、(7)
及び(8)はプラグを通じて微粒ベッドを押すグラファ
イト棒及びバネである。また、(9)は開口率30%の多
孔質基体管であり、セラミックセメント(13)により緻
密な支持管(12)で支持されている。(10)は多孔質基
体管(9)に水蒸気を導入するためのアルミナ管であ
る。In the figure, reference numeral (1) is a quartz glass reaction tube, (2)
Is a graphite reaction tube, (3) is a halogen material (4)
Graphite tube containing, (5) fibrous graphite plug, (6) perforated graphite plug, (7)
And (8) are graphite rods and springs that push the granule bed through the plugs. Further, (9) is a porous substrate tube having an opening ratio of 30% and is supported by a dense support tube (12) by ceramic cement (13). (10) is an alumina tube for introducing water vapor into the porous substrate tube (9).
次にこの従来装置の動作について説明する。Next, the operation of this conventional device will be described.
まず、反応ガスCl2とキヤリアガスArとをグラファイト
管(3)に導入し、反応 MeO2+2C(s)+Cl2(g)→MeCl2(g)+2CO(g) により、ジルコニウム(Zr)及びイツトリウム(Y)の
塩化物蒸気を発生させ反応管(2)へ供給する。同時
に、多孔質基体管(9)の内側にアルミナ管(10)を通
して水蒸気を供給すると、第4図に示すように、2段階
の反応により固体電解質膜が成長する。ただし、第4図
において、符号Iは第1段の反応後の状態を、IIは第2
段の反応後の状態を示す。First, the reaction gas Cl 2 and the carrier gas Ar were introduced into the graphite tube (3), and the reaction MeO 2 + 2C (s) + Cl 2 (g) → MeCl 2 (g) + 2CO (g) was used to produce zirconium (Zr) and yttrium. Chloride vapor of (Y) is generated and supplied to the reaction tube (2). At the same time, when water vapor is supplied to the inside of the porous substrate tube (9) through the alumina tube (10), a solid electrolyte membrane grows by a two-step reaction as shown in FIG. However, in FIG. 4, reference numeral I indicates the state after the reaction in the first stage, and II indicates the second state.
The state after reaction of the stage is shown.
この反応を記すと、まず、多孔質基体管(9)の内側の
水蒸気が多孔質基体管(9)の孔を通過し、多孔質基体
管(9)の表面で、塩化物蒸気中のZr及びY塩化物との
反応(第1段のCVD反応) MeCl2+H2O→MeO+2HCl により固体膜を形成して孔をふさぐ。To describe this reaction, first, the water vapor inside the porous substrate tube (9) passed through the pores of the porous substrate tube (9), and at the surface of the porous substrate tube (9), Zr in chloride vapor was introduced. And reaction with Y chloride (first stage CVD reaction) A solid film is formed by MeCl 2 + H 2 O → MeO + 2HCl to close the pores.
次に酸素分圧の差により固体膜に電子導電性が現れるた
め、第2段の反応 H2O+2e-→H2+O= HeCl2+O=→MeO+Cl2+2e- に示すように、第1段で生成した固体膜の水蒸気側の表
面状に現れた電子によりH2Oは還元され、それにより生
じた酸素イオン(O2-)が成長膜表面へ拡散し反応が継
続する。Next, because the electronic conductivity appears in the solid film due to the difference in oxygen partial pressure, as shown in the reaction H 2 O + 2e − → H 2 + O = HeCl 2 + O = → MeO + Cl 2 + 2e − in the second step, The H 2 O is reduced by the electrons appearing on the surface of the generated solid film on the water vapor side, and oxygen ions (O 2− ) generated thereby are diffused to the surface of the grown film to continue the reaction.
このときの堆積速度の一例を示すと、圧力が5Torr以
下、堆積温度がイットリア安定化ジルコニア(Yttrium
Stabilized Zirconia)1200℃の場合で堆積速度0.5〜2
μm/分程度である。As an example of the deposition rate at this time, the pressure is 5 Torr or less and the deposition temperature is yttria-stabilized zirconia (Yttrium-stabilized zirconia).
Stabilized Zirconia) Deposition rate of 0.5 to 2 at 1200 ℃
It is about μm / min.
[発明が解決しようとする課題] 従来の固体電解質膜堆積技術としてのEVD法で得られる
固体電解質膜は、他法によって得られる固体電解質膜に
比べて緻密であるという長所がある一方、膜中の電子移
動速度が堆積速度を律速しており、その堆積速度は0.5
〜2μm/分程度であって、工業化するには遅いという問
題点があり、この問題点を解決したいという課題を有し
ていた。[Problems to be Solved by the Invention] The solid electrolyte membrane obtained by the EVD method, which is a conventional solid electrolyte membrane deposition technique, has an advantage that it is denser than solid electrolyte membranes obtained by other methods. The electron transfer rate of is controlling the deposition rate, and the deposition rate is 0.5
There is a problem that it is about 2 μm / min and it is slow to be industrialized, and there is a problem to solve this problem.
この発明は、上記のような課題を解決するためになされ
たもので、反応領域における電子の移動速度を高めて、
高速堆積可能な固体電解質膜堆積装置を得ることを目的
とする。The present invention has been made to solve the above problems, by increasing the moving speed of electrons in the reaction region,
An object is to obtain a solid electrolyte membrane deposition apparatus capable of high-speed deposition.
[課題を解決するための手段] この発明に係る固体電解質膜堆積装置は、従来のEVD法
による固体電解質膜堆積装置の反応管(1)の外部に2
本の電極リングを設けて金属化合物ガス側の反応室にプ
ラズマを発生させ、そこへ探針電極を導入すると共に、
同時に金属化合物ガス側表面に多孔質電極を設けること
によって、成長する固体電解質膜を取りまく外部電子電
流回路を形成しているものである。[Means for Solving the Problem] A solid electrolyte membrane deposition apparatus according to the present invention is provided with a 2 mm external reaction tube (1) of a conventional solid electrolyte membrane deposition apparatus using the EVD method.
A plasma is generated in the reaction chamber on the metal compound gas side by providing a book electrode ring, and the probe electrode is introduced into the plasma,
At the same time, a porous electrode is provided on the metal compound gas side surface to form an external electron current circuit surrounding the growing solid electrolyte membrane.
[作 用] この発明装置は、上記のように構成されているので、プ
ラズマ並びに探針電極、及び多孔質電極により、電子の
外部回路が形成され、電子の移動速度が増大することに
よって、酸素イオン(O2-)の拡散、反応によるチャー
ジ・アップは容易に解消され、堆積速度は増加する。[Operation] Since the device of the present invention is configured as described above, an external circuit of electrons is formed by the plasma, the probe electrode, and the porous electrode, and the moving speed of the electrons increases, so that oxygen Ion (O 2- ) diffusion and charge-up due to reaction are easily eliminated, and the deposition rate increases.
[実施例] 以下、この発明をその一実施例を示す図に基づいて説明
する。[Embodiment] The present invention will be described below with reference to the drawings showing an embodiment thereof.
第1図はこの発明の一実施例を示す図であり、符号
(1)〜(13)は上記従来装置に同一符号で示したもの
と同一又は同等のものである。FIG. 1 is a diagram showing an embodiment of the present invention, in which reference numerals (1) to (13) are the same as or equivalent to those shown in the conventional apparatus by the same reference numerals.
符号(14)は石英ガラス製反応管(1)の外周に2個、
多孔質基体管(9)をその両者の内側に含むように設け
られている電極リング例えばPt電極リング、(15)はこ
のPt電極リング(14)に接続されている13.56MHz高周波
(RF)電源であり、(16)はプラズマ内に挿入されてい
る探針電極、(17)は多孔質基体管(9)外表面に設け
られている多孔質電極であり、探針電極(16)及び多孔
質電極(17)で外部電子電流回路が形成される。また、
(18)呼及び(19)はこの回路中に設けられた電流計及
び可変抵抗器である。なお、石英ガラス製反応管
(1)、Pt電極リング(14)はすべて約1100℃まで過熱
可能な炉内に位置している。Reference numeral (14) is two on the outer circumference of the quartz glass reaction tube (1),
Electrode ring, for example Pt electrode ring, provided so as to include the porous substrate tube (9) inside both of them, (15) is a 13.56MHz radio frequency (RF) power source connected to this Pt electrode ring (14) (16) is a probe electrode inserted in the plasma, and (17) is a porous electrode provided on the outer surface of the porous substrate tube (9). An external electronic current circuit is formed by the quality electrode (17). Also,
(18) Call and (19) are an ammeter and a variable resistor provided in this circuit. The quartz glass reaction tube (1) and the Pt electrode ring (14) are all located in a furnace capable of overheating to about 1100 ° C.
上記のように構成されているこの発明の固体電解質堆積
装置においては、13.56MHz高周波電源(15)より2本の
Pt電極リング(14)に高周波パワーを入力しプラズマを
発生させる。In the solid electrolyte deposition apparatus of the present invention configured as described above, two units of the 13.56 MHz high frequency power source (15) are used.
High frequency power is input to the Pt electrode ring (14) to generate plasma.
多孔質基体管(9)の外側と内側にそれぞれ塩化物蒸気
及び水蒸気を供給すると、第1段のCVD法までは、ほぼ
従来のEVD法による場合と同様の手順で甲の埋込みが行
なわれる。When chloride vapor and water vapor are supplied to the outer side and the inner side of the porous substrate tube (9) respectively, up to the first-stage CVD method, the instep is embedded in substantially the same procedure as in the conventional EVD method.
第2段の反応では、まず電解質膜内表面で供給した酸素
の吸着、分解が起こり酸素イオンが発生する。In the second-step reaction, the oxygen supplied on the inner surface of the electrolyte membrane is adsorbed and decomposed to generate oxygen ions.
この酸素イオンは電解質膜外表面へと固体電解質中を拡
散により移動し、さらに、表面で電子を放出し、反応 MeCl2+O=→MeO+Cl2+2e- によって、金属酸化膜を形成する。The oxygen ions move to the outer surface of the electrolyte membrane by diffusion in the solid electrolyte, and further release electrons on the surface to form a metal oxide film by the reaction MeCl 2 + O = → MeO + Cl 2 + 2e − .
放出された電子は、チャージアップすることなく、プラ
ズマ電極により形成された外部電子電流回路を通じて容
易に電解質膜内側へと移動するので、蒸気の金属酸化物
固体電解質膜の形成反応は速やかに進行する。この際、
外部電子電流回路を流れる電流量を電流計で計測し、か
つ、負荷抵抗を用いてその電流量を調節することによっ
て、膜成長速度の制御が可能である。The emitted electrons easily move to the inside of the electrolyte membrane through the external electron current circuit formed by the plasma electrode without being charged up, so that the vapor metal oxide solid electrolyte membrane formation reaction proceeds rapidly. . On this occasion,
The film growth rate can be controlled by measuring the amount of current flowing through the external electronic current circuit with an ammeter and adjusting the amount of current using a load resistance.
なお、上記実施例では、プラズマを発生させるために2
個の電極リング(14)を用いているが、これを円筒に縦
に2枚に切った形の電極にかえ、反応室近傍の反応管の
上下にこの2枚の電極を設置してもプラズマは発生させ
ることができる。In addition, in the above embodiment, in order to generate plasma,
A single electrode ring (14) is used, but it can be replaced by an electrode that is cut vertically into a cylinder, and the two electrodes can be installed above and below the reaction tube near the reaction chamber. Can be generated.
また、上記実施例では、固体電解質膜を成長させる基体
を円筒管に形成していたが、これに限らるものではな
く、平板状でもよく、その場合、上記実施例と同じ効果
が期待できることは言うまでもない。Further, in the above-mentioned embodiment, the base body for growing the solid electrolyte membrane was formed into a cylindrical tube, but the present invention is not limited to this, and it may be a flat plate, in which case the same effect as that of the above-mentioned embodiment can be expected. Needless to say.
なお、上記説明では、この固体電解質膜堆積装置の発明
は、固体電解膜の堆積技術に関して述べてきたが、酸素
センサーの製造技術としても利用できる。In the above description, the invention of the solid electrolyte membrane deposition apparatus has been described with respect to the solid electrolyte membrane deposition technology, but it can also be used as the oxygen sensor manufacturing technology.
また、この実施例のように、外部電子電流回路に電流計
及び可変の抵抗器を設けるならば、上記回路に流れる電
流を計測しあるいは制御することによって、膜成長速度
を計測したり、あるいは、制御することができる効果を
有している。If an ammeter and a variable resistor are provided in the external electronic current circuit as in this embodiment, the film growth rate is measured by measuring or controlling the current flowing in the circuit, or Has the effect of being controllable.
[発明の効果] この発明は、以上説明したように構成され、金属加工物
ガス側の反応空間にプラズマを発生させると共に該発生
部に探針電極を設け、かつ、同時に金属化合物ガス側表
面に多孔質電極を設けることによって、固体電解膜を取
りまく外部電子電流回路を形成しているので、膜成長速
度を高めることができ、また、従来法より反応質の温度
を下げても同程度の膜成長速度が可能であり、更に、多
孔質基体外表面の反応室の酸素分圧がそれほど低くなく
ても、よく酸素のもれの制限を緩和できるという効果を
奏することができる。[Advantages of the Invention] The present invention is configured as described above, generates plasma in the reaction space on the metal workpiece gas side, and provides a probe electrode on the generation part, and at the same time, on the metal compound gas side surface. Since the external electrode current circuit surrounding the solid electrolyte membrane is formed by providing the porous electrode, the film growth rate can be increased, and even if the temperature of the reactant is lowered as compared with the conventional method, the same level of film can be obtained. A growth rate is possible, and further, even if the oxygen partial pressure of the reaction chamber on the outer surface of the porous substrate is not so low, the effect of well suppressing the leakage of oxygen can be exerted.
第1図はこの発明の一実施例を示す縦断面図、第2図は
第1図の多孔質基体管(9)及び多孔質電極(17)の詳
細図、第3図は従来のEVD法に用いられる反応装置を示
す縦断面図、第4図は第3図のEVD法の原理を示す説明
図である。 図において、(1)は石英ガラス製反応管、(3)はグ
ラファイト管、(4)はハロゲン材料、(9)は多孔質
基体(多孔質基体管)、(14)は電極リング(Pt電極リ
ング)、(15)は高周波電源、(16)は探針電極、(1
7)は多孔質電極、(18)は外部電子電流回路における
電流計、(19)は同回路における可変抵抗器。 なお、各図中、同一符号は同一又は相当部分を示す。FIG. 1 is a longitudinal sectional view showing an embodiment of the present invention, FIG. 2 is a detailed view of the porous substrate tube (9) and porous electrode (17) of FIG. 1, and FIG. 3 is a conventional EVD method. FIG. 4 is a longitudinal sectional view showing a reaction apparatus used in FIG. 4, and FIG. 4 is an explanatory view showing the principle of the EVD method of FIG. In the figure, (1) is a quartz glass reaction tube, (3) is a graphite tube, (4) is a halogen material, (9) is a porous substrate (porous substrate tube), and (14) is an electrode ring (Pt electrode). Ring), (15) high frequency power supply, (16) probe electrode, (1
7) is a porous electrode, (18) is an ammeter in an external electronic current circuit, and (19) is a variable resistor in the circuit. In each figure, the same reference numerals indicate the same or corresponding parts.
Claims (1)
コニウム、イットリウムなどの金属化合物ガスを、ま
た、他方の空間に酸素を供給し、上記多孔質基体両面の
酸素分圧の差により固体電解質膜中を酸素イオン
(O2-)が拡散し、上記多孔質基体の金属化合物ガス側
表面に金属酸化物固体電解質膜を成長させる電気化学蒸
着法(EVD法)に基づく固体電解質膜堆積装置におい
て、金属化合物ガス側の反応空間にプラズマを発生させ
ると共に該発生部に探針電極を設け、かつ、同時に金属
化合物ガス側多孔質基体表面に多孔質電極を設けること
によって、成長する固体電解質膜を取りまく外部電子電
流回路を形成していることを特徴とする固体電解質膜堆
積装置。1. A metal compound gas such as zirconium or yttrium is supplied to one space partitioned by a porous substrate, and oxygen is supplied to the other space, so that a solid is produced by a difference in oxygen partial pressure between both surfaces of the porous substrate. Oxygen ion (O 2− ) is diffused in the electrolyte membrane to grow a metal oxide solid electrolyte membrane on the metal compound gas side surface of the porous substrate, which is based on the electrochemical deposition method (EVD method). In, a solid electrolyte membrane is grown by generating plasma in the reaction space on the metal compound gas side and providing a probe electrode on the generation part and simultaneously providing a porous electrode on the surface of the metal compound gas side porous substrate. A solid electrolyte membrane deposition device, characterized in that an external electronic current circuit surrounding the device is formed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10768789A JPH0787896B2 (en) | 1989-04-28 | 1989-04-28 | Solid electrolyte membrane deposition equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10768789A JPH0787896B2 (en) | 1989-04-28 | 1989-04-28 | Solid electrolyte membrane deposition equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02290242A JPH02290242A (en) | 1990-11-30 |
| JPH0787896B2 true JPH0787896B2 (en) | 1995-09-27 |
Family
ID=14465425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10768789A Expired - Lifetime JPH0787896B2 (en) | 1989-04-28 | 1989-04-28 | Solid electrolyte membrane deposition equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0787896B2 (en) |
-
1989
- 1989-04-28 JP JP10768789A patent/JPH0787896B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02290242A (en) | 1990-11-30 |
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