JPS6077108A - Oxygen concentration pump - Google Patents
Oxygen concentration pumpInfo
- Publication number
- JPS6077108A JPS6077108A JP18042683A JP18042683A JPS6077108A JP S6077108 A JPS6077108 A JP S6077108A JP 18042683 A JP18042683 A JP 18042683A JP 18042683 A JP18042683 A JP 18042683A JP S6077108 A JPS6077108 A JP S6077108A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- pump
- solid electrolyte
- zro2
- concentration pump
- 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.)
- Pending
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
【発明の詳細な説明】
本発明1士酸素ポンプ、特に高い導電性を有することに
より酸素に対する選択透過性の良好な新規な物質を用い
た酸素ポンプに係るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an oxygen pump, and particularly to an oxygen pump using a novel substance that has high conductivity and thus has good permselectivity for oxygen.
酸素に対する選択透過性を有する隔壁(PI )を用い
、空気中の酸素を濃縮したり、或は逆に酸素含有ガス中
から脱酸素を行なうことは例えば医療の分野や、食品、
化学、電子工業等の各分野において種々提案され、或い
は一部は実用Lヂ イJL 七 鉛 丁 し1 ス
そしてこの様な隔膜としては、例えばポリオルガノシロ
キサン等の有機高分子から成る隔膜が取り扱い上、又性
能−F好ましい材料とされているが、この様な有機高分
子材料は一般に隔膜をはさんで差圧を設けねばならない
等の欠点がある。Concentrating oxygen in the air or deoxidizing oxygen-containing gas using a partition wall (PI) that has selective permeability to oxygen is used, for example, in the medical field, food, etc.
Various proposals have been made in various fields such as chemistry and the electronics industry, and some of them have been put into practical use.As such diaphragms, for example, diaphragms made of organic polymers such as polyorganosiloxane are handled. Although the above and performance-F properties are said to be preferable materials, such organic polymer materials generally have drawbacks such as the need to provide a differential pressure across a diaphragm.
これに対し、 Y2O3やCaO等によって安定化され
た所謂安定化ジルコニアを隔膜として用い、隔膜の両面
に電圧を印加する方法が提案されている。この材料は成
る程度の酸素選択透過性を有し、耐熱性が十分である利
点がある反面、この材料を実用に供する為には一般に6
00°C以り。In contrast, a method has been proposed in which so-called stabilized zirconia stabilized with Y2O3, CaO, etc. is used as a diaphragm and voltage is applied to both sides of the diaphragm. Although this material has the advantage of having a certain degree of selective oxygen permeability and sufficient heat resistance, it is generally difficult to put this material to practical use.
Above 00°C.
好ましくは800°C以上の高温雰囲気下におくことが
要求される。更にこの種の材料は電極を用いて実用に供
される為、800 ’CCヒト高温を用いることになる
とその材質に著しい制限が課せられ、又操作的にも煩雑
である等不利な点が多い。Preferably, it is required to be placed in a high temperature atmosphere of 800°C or higher. Furthermore, since this type of material is put to practical use using electrodes, there are many disadvantages such as significant restrictions on the material when using 800' CC human high temperature, and the operation is complicated. .
木発明者は、この様な耐熱性を有する材ネ′1であって
上記不利な点を改善し得る材料を見出すことを目的とし
て種々研究、検討した結果、特定組成を有する弗化酸化
物が前記目的を達成し得ることを見出しした。As a result of various studies and examinations aimed at finding a material with such heat resistance that could improve the above-mentioned disadvantages, the inventor of wood discovered that a fluorinated oxide having a specific composition was found. It has been found that the above object can be achieved.
かくして本発明は、一般式(Zr02)100−”(’
MF3 h (但しM=Yであって!=13〜25.或
いはM=Ybであってx=16〜25.Xはモル%)で
示される酸素イオン導電性固体電解質を用いた酸素ポン
プを提供するにある。Thus, the present invention provides general formula (Zr02)100-"('
Provides an oxygen pump using an oxygen ion conductive solid electrolyte represented by MF3h (where M=Y and !=13 to 25. or M=Yb and x=16 to 25.X is mol%) There is something to do.
本発明において上記組成を逸脱する場合には導電性の低
下が著しくなったり、不均一組成を示し、熱衝撃性が低
下するので実用的でない。In the present invention, if the composition deviates from the above-mentioned range, the conductivity will be significantly lowered, the composition will be non-uniform, and the thermal shock resistance will be lowered, which is not practical.
上記組成範囲を有する場合には導電性や焼結性がほぼ安
定又は一定しており、実用性を十分布している。そして
材料の特性や経済性の点からMがイツトリウム(Y)の
場合x−14〜1B1Mがイッテルビウム(Yb)の場
合には!=17〜19を採用するのが特に好ましい。When the composition is within the above range, the conductivity and sinterability are almost stable or constant, and the composition is sufficiently practical. From the viewpoint of material properties and economic efficiency, if M is yttrium (Y), then x-14~1B1M is ytterbium (Yb)! It is particularly preferable to employ =17 to 19.
本発明による導電性物質の製法は、酸化ジルコニウムと
弗化イツトリウム又は弗化イッテルビウムを夫々粉砕混
合し、不活性ガス雰囲気下1100〜1400°Cに3
時間程度保持することにより得ることが出来る0例えば
(ZrO2)B5 (YF3 )+5を得る場合には0
.85モル(7) ZrO2と0.15モルのYF3を
粉砕混合し、アルゴン雰囲気下に1200℃において3
時間程度焼成せしめることによりに容易に得ることが出
来る。又ZrO2、ZrF4 と Y2O3やYb20
:+の混合物を同様に焼成焼結せしめることにより製造
し得る。但しこの場合、 ZrF4が比較的揮発性であ
る為、ZrF4の損失や目標組成に正確に達しな一1/
1ことがあるので注意を要する。The method for producing a conductive material according to the present invention involves pulverizing and mixing zirconium oxide and yttrium fluoride or ytterbium fluoride, respectively, and heating the mixture at 1100 to 1400°C in an inert gas atmosphere for 30 minutes.
0 that can be obtained by holding it for about an hour.For example, if you want to obtain (ZrO2)B5 (YF3)+5, then 0
.. 85 mol (7) ZrO2 and 0.15 mol YF3 were pulverized and mixed, and 3
It can be easily obtained by firing it for about an hour. Also ZrO2, ZrF4, Y2O3 and Yb20
:+ can be produced by firing and sintering the mixture in the same manner. However, in this case, since ZrF4 is relatively volatile, loss of ZrF4 and failure to accurately reach the target composition may occur.
There is one thing that you need to be careful about.
又これら、固体電解質の形状付与は、例えば薄膜状物を
得る際にはプラズマ溶射法、真空蒸着法、スパッタリン
グ法等を、比較的厚い形状の場合にはホットプレス法、
ラバープレス法。In addition, these solid electrolytes can be shaped using, for example, plasma spraying, vacuum evaporation, sputtering, etc. to obtain a thin film, and hot pressing, etc. to obtain a relatively thick shape.
Rubber press method.
熱間静水圧焼結法等を適宜採用することが出来る。A hot isostatic pressure sintering method or the like can be appropriately employed.
本発明に用いられる固体電解質の厚さは一般に1p〜5
■程度が適当である。厚さが前記範囲に満たない場合に
は、不均一でガス漏れが起り易くなり、逆に前記範囲を
超える場合には抵抗損失が著しく大きくなる虞れがある
ので何れも好ましくない。The thickness of the solid electrolyte used in the present invention is generally 1p to 5p.
■The level is appropriate. If the thickness is less than the above range, gas leakage is likely to occur due to non-uniformity, while if it exceeds the above range, resistance loss may become significantly large, which is not preferable.
又、本発明に用いられる陽極の材質としては、例えば白
金、銀、コバルトなどの金属材料La(:ov3などの
ペロブスカイト系材料等が又陰極の材質としては例えば
白金、銀、ニッケルなど金属材料、LaCoO3などの
ペロブスカイト系骸化物材料等を適宜採用することが出
来る。In addition, the material for the anode used in the present invention includes, for example, a metal material such as platinum, silver, and cobalt, and a perovskite material such as La(:OV3), and the material for the cathode includes, for example, a metal material such as platinum, silver, and nickel. A perovskite skeleton material such as LaCoO3 can be appropriately employed.
又これら陰、陽極は何れもガスが透過することが必要で
あり、この為これら電極の有する物性としては、多孔質
で半融しにくく固体電解質との密着性がよいものを採用
するのが適当である。又、これら電極の厚さは一般に数
千人〜100ル程度を採用するのが適当である。In addition, it is necessary for gas to permeate through both of these anodes and cathodes, and for this reason, it is appropriate that these electrodes have physical properties that are porous, difficult to semi-melt, and have good adhesion to the solid electrolyte. It is. The thickness of these electrodes is generally about several thousand to about 100 μl.
これらの電極は固体電解質に対しスクリーン印刷法、ス
パッタリング法等の手段により設けることが出来る。These electrodes can be provided on the solid electrolyte by means such as screen printing or sputtering.
次に本発明を実施例により説明する。Next, the present invention will be explained by examples.
実施例l
ZrO20,8f1モルとYF30.14モルの粉末を
ボールミルを用いて粉砕混合した後、ラバープレス法を
用いて直径20os、厚さ2mmのペレットに成型した
。これをアルゴン雰囲気中1200″Cで3時間焼成し
た。この焼結体のX線回折図は第1図に示す通りであり
、組成は(ZrO2) 86
(YF3 )0.14であった。これにpt粉末を焼き
付けた後ざらにptリード線を取りつけ、焼結アルミナ
製チューブにアルミナセメントを用い装着し酸素ポンプ
を作製した。これを炉心管が石英製の電気炉に挿入し、
600°Cに加熱保持し、内側に酸素2%−アルゴン
88%の混合ガスを10hu /分の流量で供給し、外
側に酸素20PPffiを含むアルゴンガスを100+
JL /分の流量で供給した。1時間後内部極をアノー
ド、外部様をカソードとして端子間に2vの電圧を印加
した結果、アノード側に酸素が0.18cc/分の割合
で発生した。Example 1 Powders of 1 mole of ZrO20.8f and 0.14 mole of YF were pulverized and mixed using a ball mill, and then molded into pellets with a diameter of 20 os and a thickness of 2 mm using a rubber press method. This was fired at 1200''C in an argon atmosphere for 3 hours. The X-ray diffraction pattern of this sintered body was as shown in Figure 1, and the composition was (ZrO2) 86 (YF3) 0.14. After baking PT powder into the tube, we attached a PT lead wire to the surface and attached it to a sintered alumina tube using alumina cement to create an oxygen pump.This was inserted into an electric furnace with a quartz core tube.
Heating and holding at 600°C, a mixed gas of 2% oxygen and 88% argon was supplied to the inside at a flow rate of 10hu/min, and argon gas containing 20PPffi of oxygen was supplied to the outside at 100+
It was supplied at a flow rate of JL/min. After one hour, a voltage of 2V was applied between the terminals with the inner electrode as the anode and the outer electrode as the cathode, and as a result, oxygen was generated on the anode side at a rate of 0.18 cc/min.
実施例2
ZrO70,82モルと YbF、 0.18モルのj
’a i=を宇流側1と同じ方法で混合、成型、焼成し
た。焼結体のX線回折図は第2図に示す通りであり、組
成は(ZrCl2 )。、8□(YbF、 )。、18
であった。Example 2 70.82 moles of ZrO and 0.18 moles of YbF
'a i= was mixed, molded, and fired in the same manner as Uryu side 1. The X-ray diffraction pattern of the sintered body is as shown in FIG. 2, and the composition is (ZrCl2). , 8□(YbF, ). , 18
Met.
これを用いて酸素ポンプを作製した後実施例1と同様な
条件下で7メード側に酸素2%を含むアルゴンガスを、
カソード側に20ppmの酸素を含むアルゴンガスを供
給し、端子間に2Vの電圧を印加した結果、7メード側
に0 、18cc/分の割合で酸素が発生した。After making an oxygen pump using this, under the same conditions as in Example 1, argon gas containing 2% oxygen was added to the 7-made side.
As a result of supplying argon gas containing 20 ppm of oxygen to the cathode side and applying a voltage of 2 V between the terminals, oxygen was generated on the 7-made side at a rate of 0.18 cc/min.
第1.2図は実施例中に示した本発明に用いられた組成
物のX線回折図である。
手続補正日動式)
昭和59¥−2月λV日
特許庁長官 若杉和夫殿
1、事件の表示
昭和58#許願第180426号
2、発明の名称
酪素濃縮ポンプ
3、補正をする者
事件との関係 特許出願人
住 所 東京都千代田区丸の内二丁目132号名称 (
004)旭硝子株式会社
4、代理人
〒105
住 所 東京都港区虎ノ門−丁目16番 2号虎ノ門千
代田ビル
昭和59年1月31日 (JA送日)
6、補正により増加する発明の数 なし7、補正の対象
明細書
8、補正の内容 明細書の浄書(内容に変更なし)以上Figure 1.2 is an X-ray diffraction diagram of the composition used in the present invention shown in the Examples. Procedural amendment date and time) 1980 ¥-February λV Director-General of the Patent Office Mr. Kazuo Wakasugi 1, Indication of the case 1987 #Grant Application No. 180426 2, Name of the invention Butyric Concentration Pump 3, Person making the amendment Relationship to the case Patent applicant address: 132 Marunouchi 2-chome, Chiyoda-ku, Tokyo Name (
004) Asahi Glass Co., Ltd. 4, Agent 105 Address No. 2 Toranomon Chiyoda Building, 16-chome, Toranomon, Minato-ku, Tokyo January 31, 1981 (JA Date) 6. Number of inventions increased by amendment None 7 , Subject of amendment: Specification 8, Contents of amendment: Reprint of the specification (no change in content) and above
Claims (1)
(但しM=Yであッテx=113〜25.或いはM=Y
bテあって!=18〜25、xはモル%)で示される酸
素イオン導電性固体電解質を用いた酸素濃縮ポンプ。1. General formula (Zr02) 100-! (MF3)!
(However, M=Y and x=113~25. Or M=Y
There's b-te! = 18 to 25, x is mol %) An oxygen concentrator pump using an oxygen ion conductive solid electrolyte.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18042683A JPS6077108A (en) | 1983-09-30 | 1983-09-30 | Oxygen concentration pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18042683A JPS6077108A (en) | 1983-09-30 | 1983-09-30 | Oxygen concentration pump |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6077108A true JPS6077108A (en) | 1985-05-01 |
Family
ID=16083044
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18042683A Pending JPS6077108A (en) | 1983-09-30 | 1983-09-30 | Oxygen concentration pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6077108A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04228409A (en) * | 1990-05-24 | 1992-08-18 | Air Prod And Chem Inc | Refining of mass-production argon |
| US5441610A (en) * | 1992-02-28 | 1995-08-15 | Renlund; Gary M. | Oxygen supply and removal method and apparatus |
-
1983
- 1983-09-30 JP JP18042683A patent/JPS6077108A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04228409A (en) * | 1990-05-24 | 1992-08-18 | Air Prod And Chem Inc | Refining of mass-production argon |
| US5441610A (en) * | 1992-02-28 | 1995-08-15 | Renlund; Gary M. | Oxygen supply and removal method and apparatus |
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