JPH0734278A - High temperature steam electrolytic cell - Google Patents

High temperature steam electrolytic cell

Info

Publication number
JPH0734278A
JPH0734278A JP5175431A JP17543193A JPH0734278A JP H0734278 A JPH0734278 A JP H0734278A JP 5175431 A JP5175431 A JP 5175431A JP 17543193 A JP17543193 A JP 17543193A JP H0734278 A JPH0734278 A JP H0734278A
Authority
JP
Japan
Prior art keywords
high temperature
temperature steam
oxide
interconnector
unit
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.)
Withdrawn
Application number
JP5175431A
Other languages
Japanese (ja)
Inventor
Akihiro Yamashita
晃弘 山下
Nobuaki Murakami
信明 村上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5175431A priority Critical patent/JPH0734278A/en
Publication of JPH0734278A publication Critical patent/JPH0734278A/en
Withdrawn legal-status Critical Current

Links

Landscapes

  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

PURPOSE:To improve the airtightness of an electrolytic cell by adding SiO2 or MgO to oxide interconnectors which are used for joining unit electrolytic cells to each other in series while applying a pressure at a high temp. and joining the unit cells with the glass melt of the above oxide. CONSTITUTION:This high temp. steam electrolytic cell comprises the unit electrolytic cells and the oxide interconnectors 4 for joining the unit cells to each other in series. Each of the above unit electrolytic cells is provided with the cathode 3 on one surface of and the anode 2 on the other surface of the tubular oxygen ion conductive solid electrolyte 1. Further, SiO2 or MgO is added to the above interconnectors 4 and the unit electrolytic cells are joined with the glass melt of SiO2 or MgO and accordingly, the airtightness of the high temp. steam electrolytic cell can be improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は高温水蒸気電解セルの改
良に関する。
FIELD OF THE INVENTION This invention relates to improvements in high temperature steam electrolysis cells.

【0002】[0002]

【従来の技術】高温水蒸気電解セルの作動原理を図2に
示す。電極を設けた酸素イオン導電性固体電解質1を9
00℃から1000℃の高温にして、この固体電解質1
を隔壁として一方に水蒸気、もう一方に空気を供給し、
水蒸気側電極(陰極)3が負電位となるように電極間に
外部直流電源5により電圧を印加すると、陰極3で水蒸
気が電気分解され、酸素ガスと酸化ガスが生成する。生
成したガスのうち酸素ガスは酸素イオン化して固体電解
質1を拡散し、空気側電極(陽極)2で電子を放出して
酸素ガスとなる。残る水素ガスは製品水素として使用さ
れる。このような高温水蒸気電解セルを用いて効率よく
水蒸気電解を行うためには、単位セルを電気的に直列に
接続する必要がある。
2. Description of the Related Art The operating principle of a high temperature steam electrolysis cell is shown in FIG. Oxygen ion conductive solid electrolyte 1 provided with electrodes 9
This solid electrolyte 1 was heated to a high temperature of 00 ° C to 1000 ° C.
As a partition wall, supply steam to one side and air to the other side,
When a voltage is applied between the electrodes by the external DC power supply 5 so that the water vapor side electrode (cathode) 3 has a negative potential, the water vapor is electrolyzed at the cathode 3 to generate oxygen gas and oxidizing gas. Of the generated gas, oxygen gas is oxygen-ionized and diffuses in the solid electrolyte 1, and electrons are emitted at the air-side electrode (anode) 2 to become oxygen gas. The remaining hydrogen gas is used as product hydrogen. In order to efficiently perform steam electrolysis using such a high temperature steam electrolysis cell, it is necessary to electrically connect the unit cells in series.

【0003】セル構造には2つの様式がある。1つは円
筒型支持体構造と言われるもので、多孔質管を支持体と
してその上に単位セルを構成し、各々のセルをインター
コネクタで直列に接続する方法で、もう1つは、円筒型
非支持体構造と言われるもので、単位セル自身が支持体
構造となり各々のセルをインターコネクタで直列に接続
する方法である。高温水蒸気電解セルとして作動させる
場合には、水素ガスが外部に漏洩しないことが必要であ
るが、円筒型支持体構造では支持体上に成膜した電解質
及びインターコネクタを充分な気密性をもった構造とす
ることが困難であることから、セル及びインターコネク
タ自体からの水素ガス漏洩を少なくすることは難しい。
これに対して円筒型非支持体構造はセル及びインターコ
ネクタを直列に接続する前に充分緻密化させることが可
能であることから、セルとインターコネクタの接合箇所
からの水素ガス漏洩がなければ、気密性に優れた直列接
合セルの製造が可能である。なお、セルとインターコネ
クタの接合には、電解質管とインターコネクタ管を高温
で加圧接合する方法があり、これにより気密性に優れた
直列セル構造が作製できる。
There are two modes of cell structure. One is called a cylindrical support structure, in which a porous tube is used as a support to form unit cells thereon, and each cell is connected in series by an interconnector. The other is a cylinder. This is called a type non-support structure, in which the unit cells themselves become a support structure and each cell is connected in series by an interconnector. When operating as a high temperature steam electrolysis cell, it is necessary that hydrogen gas does not leak to the outside, but the cylindrical support structure has sufficient airtightness for the electrolyte and interconnector formed on the support. Since it is difficult to make the structure, it is difficult to reduce the leakage of hydrogen gas from the cell and the interconnector itself.
On the other hand, since the cylindrical unsupported structure can be sufficiently densified before connecting the cell and the interconnector in series, if there is no leakage of hydrogen gas from the joint between the cell and the interconnector, It is possible to manufacture a series junction cell having excellent airtightness. For joining the cell and the interconnector, there is a method of joining the electrolyte tube and the interconnector tube under pressure at a high temperature, whereby a series cell structure having excellent airtightness can be produced.

【0004】[0004]

【発明が解決しようとする課題】高温水蒸気電解セルの
特徴は上述した通りであるが、高温加圧接合により電解
セルを連結する場合、接合箇所でのガスリークが発生し
てはならない。本発明は高温加圧接合によりインターコ
ネクタを介して電解セルを連結して構成される高温水蒸
気電解セルにおいて、電解セルとインターコネクタ接合
箇所からのガスリークを防止しうる高温水蒸気電解セル
を提供しようとするものである。
The features of the high temperature steam electrolysis cell are as described above. However, when the electrolysis cells are connected by high temperature pressure bonding, no gas leak should occur at the joint. The present invention is to provide a high temperature steam electrolysis cell capable of preventing gas leakage from a portion where the electrolysis cell and the interconnector are joined, in a high temperature steam electrolysis cell configured by connecting electrolysis cells through an interconnector by high temperature pressure joining. To do.

【0005】[0005]

【課題を解決するための手段】本発明は酸素イオン導電
性固体電解質管の片面に陰極、他面に陽極を設けた単位
電解セルと、この単位電解セルを直列に接続するための
酸化物インターコネクタからなる高温水蒸気電解セルに
おいて、酸化物インターコネクタにSiO2 またはMg
Oを添加されてなることを特徴とする高温水蒸気電解セ
ルである。
The present invention is directed to a unit electrolytic cell having a cathode on one side and an anode on the other side of an oxygen ion conductive solid electrolyte tube, and an oxide intercalator for connecting the unit electrolytic cells in series. In a high temperature steam electrolysis cell consisting of a connector, SiO 2 or Mg was added to the oxide interconnector.
A high-temperature steam electrolysis cell characterized in that O is added.

【0006】本発明において使用される酸化物インター
コネクタの材質としてはLaCrO 3 、La0.8 Ca
0.2 CrO3 、La0.8 Sr0.2 CrO3 、La0.8
0.2CrO3 などが例示され、これら酸化物インター
コネクタに添加されるSiO2またはMgOの添加量は
それぞれ5〜10wt%の範囲が好ましい。
The oxide interface used in the present invention
LaCrO as the material of the connector 3, La0.8Ca
0.2CrO3, La0.8Sr0.2CrO3, La0.8M
g0.2CrO3And the like.
SiO added to the connector2Or the amount of MgO added is
The range of 5 to 10 wt% is preferable respectively.

【0007】[0007]

【作用】電解セル、インターコネクタを高温加圧接合に
より直列に接合した高温水蒸気電解セルにおいて、イン
ターコネクタ材料にSiO2 またはMgOを添加するこ
とにより、電解セルとインターコネクタの接合が、Si
2 またはMgOのガラス溶融物で接合されるため、気
密性に優れた電解セルが形成される。
In a high-temperature steam electrolysis cell in which an electrolysis cell and an interconnector are joined in series by high-temperature pressure joining, SiO 2 or MgO is added to the interconnector material to bond the electrolysis cell and the interconnector to Si.
Since they are joined by a glass melt of O 2 or MgO, an electrolytic cell having excellent airtightness is formed.

【0008】[0008]

【実施例】本発明の一実施例を図1によって説明する。
図1は本発明高温水蒸気電解セルの一実施例の断面図を
示す。固体電解質1はZrO2 にY2 3 を14wt%
の割合で混合し、空気中1800℃で10時間焼成して
得られた酸化物粉体を平均粒子径が1μm以下となるよ
うに粉砕し、これを静水圧加圧装置により円筒形に成形
し、さらにリング形状に加工したものである。固体電解
質リングは直径約20mm、肉厚500μmから300
μmである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG.
FIG. 1 shows a cross-sectional view of one embodiment of the high temperature steam electrolysis cell of the present invention. Solid electrolyte 1 is ZrO 2 with 14 wt% of Y 2 O 3
Oxide powder obtained by mixing in air at 1800 ° C. for 10 hours and crushed to an average particle size of 1 μm or less, and molded into a cylindrical shape by a hydrostatic pressure device. , Further processed into a ring shape. The solid electrolyte ring has a diameter of about 20 mm and a wall thickness of 500 μm to 300 μm.
μm.

【0009】陽極2はLaMnO3 酸化物で、酸化ラン
タン、酸化マンガンをLa:Mn=1:1となるように
混合し1300℃空気中で10時間焼成し、粉砕により
平均粒子径が1μm以下となるようにしたものを、塗布
して焼き付けてなるものである。陰極3はNi/YSZ
サーメットを焼き付けてなるものである。インターコネ
クタ4はLaCrO3 系酸化物で、酸化ランタン、酸化
クロムをLa:Cr=1:1となるように混合し、これ
にSiO2 またはMgOをそれぞれ2〜3wt%添加し
て1300℃空気中で10時間焼成し、粉砕により平均
粒子径が1μm以下となるようにしたものを静水圧加圧
装置により円筒形に成形し、さらにリング形状に加工し
たものである。
The anode 2 is an LaMnO 3 oxide, and lanthanum oxide and manganese oxide are mixed so that La: Mn = 1: 1, and the mixture is baked in air at 1300 ° C. for 10 hours. It is formed by applying and baking the above. The cathode 3 is Ni / YSZ
It is made by baking cermet. In interconnector 4 LaCrO 3 type oxide, lanthanum oxide, chromium oxide La: Cr = 1: 1 and were mixed so that, thereto to SiO 2 or MgO was added, respectively 2~3wt% 1300 ℃ in air It was fired for 10 hours, pulverized to have an average particle size of 1 μm or less, molded into a cylindrical shape by a hydrostatic pressure device, and further processed into a ring shape.

【0010】固体電解質リングとインターコネクタリン
グを積層し、1300℃から1500℃、空気中で接合
圧力0.2kgf/cm2 で接合を行うことにより、本
発明の高温水蒸気電解セルが得られる。従来の酸化物イ
ンターコネクタであるLaCrO3 の焼結体の相対密度
は64%であったが、SiO2 またはMgOを添加した
場合の本発明のインターコネクタの相対密度は95%に
なった。
The high temperature steam electrolysis cell of the present invention can be obtained by stacking a solid electrolyte ring and an interconnector ring and bonding them at a bonding pressure of 0.2 kgf / cm 2 in air at 1300 ° C. to 1500 ° C. The relative density of the sintered body of LaCrO 3 which is a conventional oxide interconnector was 64%, but the relative density of the interconnector of the present invention when SiO 2 or MgO was added was 95%.

【0011】[0011]

【発明の効果】上述したように、本発明によれば、高温
水蒸気電解セルにおいて、酸化物インターコネクタにM
gOまたはSiO2 を混合することにより、固体電解質
とインターコネクタ管の接合が容易になり、ガスリーク
のない高温水蒸気電解セルを提供することができる。
As described above, according to the present invention, in the high temperature steam electrolysis cell, M is added to the oxide interconnector.
By mixing gO or SiO 2 , it becomes easy to join the solid electrolyte and the interconnector tube, and it is possible to provide a high temperature steam electrolysis cell without gas leakage.

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

【図1】本発明の一実施例の高温水蒸気電解セルの断面
図。
FIG. 1 is a sectional view of a high temperature steam electrolysis cell according to an embodiment of the present invention.

【図2】高温水蒸気電解セルの原理の説明図。FIG. 2 is an explanatory view of the principle of a high temperature steam electrolysis cell.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 酸素イオン導電性固体電解質管の片面に
陰極、他面に陽極を設けた単位電解セルと、この単位電
解セルを直列に接続するための酸化物インターコネクタ
からなる高温水蒸気電解セルにおいて、酸化物インター
コネクタにSiO2 またはMgOを添加されてなること
を特徴とする高温水蒸気電解セル。
1. A high temperature steam electrolysis cell comprising a unit electrolysis cell having a cathode on one side and an anode on the other side of an oxygen ion conductive solid electrolyte tube, and an oxide interconnector for connecting the unit electrolysis cells in series. 2. A high-temperature steam electrolysis cell characterized in that SiO 2 or MgO is added to the oxide interconnector.
JP5175431A 1993-07-15 1993-07-15 High temperature steam electrolytic cell Withdrawn JPH0734278A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5175431A JPH0734278A (en) 1993-07-15 1993-07-15 High temperature steam electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5175431A JPH0734278A (en) 1993-07-15 1993-07-15 High temperature steam electrolytic cell

Publications (1)

Publication Number Publication Date
JPH0734278A true JPH0734278A (en) 1995-02-03

Family

ID=15995989

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5175431A Withdrawn JPH0734278A (en) 1993-07-15 1993-07-15 High temperature steam electrolytic cell

Country Status (1)

Country Link
JP (1) JPH0734278A (en)

Similar Documents

Publication Publication Date Title
JPS6340848Y2 (en)
CN106374120A (en) Structure of self-sealed flat-shaped solid oxide fuel cell/electrolytic cell
JP3495654B2 (en) Cell tube seal structure
JPH09277226A (en) Manufacture of solid electrolyte type fuel cell
SE9802103L (en) New electrolytes made of composite ceramics for electricity-producing fuel cells
JPH0734278A (en) High temperature steam electrolytic cell
JPH0794196A (en) Solid electrolyte fuel cell stack
JPH07235316A (en) Cylindrical solid electrolyte fuel cell
JPH09231987A (en) Seal structure of solid electrolyte fuel cell and its manufacture
JP3244310B2 (en) Solid oxide fuel cell
JPH02168568A (en) Fuel battery with solid electrolyte
JPH0436962A (en) Fuel cell with solid electrolyte
JPH11126617A (en) Solid electrolyte-type fuel cell and its manufacture
JP3101358B2 (en) Solid oxide fuel cell separator
JPH0837011A (en) Fuel cell base board in hollow flat plate form
JPH10223239A (en) Cylindrical solid oxide electrolyte fuel cell
JPH0734281A (en) High temperature steam electrolytic cell
JPH01267964A (en) Fuel battery with solid electrolyte
JPH10172578A (en) Fuel electrode material of solid electrolyte type electrochemical cell
JP2675546B2 (en) Solid electrolyte fuel cell
JPH0412468A (en) High-temperature fuel cell
JPH09245812A (en) Flat solid electrolyte fuel cell
JPH03225771A (en) High temperature type fuel cell
JP2948439B2 (en) Solid electrolyte fuel cell
JP3419238B2 (en) Cylindrical vertical stripe solid electrolyte fuel cell

Legal Events

Date Code Title Description
A300 Application deemed to be withdrawn because no request for examination was validly filed

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20001003