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JPH0513575B2 - - Google Patents
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JPH0513575B2 - - Google Patents

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Publication number
JPH0513575B2
JPH0513575B2 JP62142286A JP14228687A JPH0513575B2 JP H0513575 B2 JPH0513575 B2 JP H0513575B2 JP 62142286 A JP62142286 A JP 62142286A JP 14228687 A JP14228687 A JP 14228687A JP H0513575 B2 JPH0513575 B2 JP H0513575B2
Authority
JP
Japan
Prior art keywords
oxygen
sample
hydrogen
flow path
gas flow
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
JP62142286A
Other languages
Japanese (ja)
Other versions
JPS63307351A (en
Inventor
Shinya Izumida
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP62142286A priority Critical patent/JPS63307351A/en
Publication of JPS63307351A publication Critical patent/JPS63307351A/en
Publication of JPH0513575B2 publication Critical patent/JPH0513575B2/ja
Granted legal-status Critical Current

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  • Investigating And Analyzing Materials By Characteristic Methods (AREA)
  • Sampling And Sample Adjustment (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、電気化学的酸素ポンプを用いた酸素
分析装置の改良による、酸素および水素同時分析
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a simultaneous oxygen and hydrogen analyzer which is an improvement of an oxygen analyzer using an electrochemical oxygen pump.

[従来の技術] 最近、金属や合金、またはそれらの化合物、あ
るいはセレン、テルルなどの半金属などに含まれ
る酸素量を、高精度でかつ絶対値測定することが
可能な新しいタイプの酸素分析層値が開発された
(大塚伸也、幸塚善作、Transaction of the
Japan Institute of Metals、Vol−25、No.9639〜
684頁、1984年9月発行)。
[Prior Art] Recently, a new type of oxygen analysis layer has been developed that can measure the amount of oxygen contained in metals, alloys, their compounds, semimetals such as selenium and tellurium, etc. with high precision and in absolute value. (Shinya Otsuka, Zensaku Kozuka, Transaction of the
Japan Institute of Metals, Vol−25, No.9639~
684 pages, published September 1984).

この酸素分析装置は、第7図に示すように、キ
ヤリアガスを循環させる閉ガス流路31に、第8
図に示すような、たとえばジルコニアにカルシ
ア、マグネシア、イツトリアなどの安定化剤を固
溶させてなる固体電解質35を用いた電気化学的
酸素ポンプ32を介在せしめ、該酸素ポンプ32
に一定の直流電圧Vを印加することにより、閉ガ
ス流路31内から酸素を排出して閉ガス流路31
内の酸素分圧を十分に低い一定値に保つことがで
きるようにしたものである。測定前には、キヤリ
アガス中の酸素が排出され、閉ガス流路31内は
十分に低い一定の酸素分圧に保たれ、その状態で
閉ガス流路31内に試料33が導入される。導入
された試料33から放出された酸素(融点の高い
試料にあつては試料溶解炉34で溶解させること
によつて酸素が迅速に放出される。)は、キヤリ
アガスによつて酸素ポンプ32まで運ばれ、酸素
ポンプ32により閉ガス流路31外に排出され
て、閉ガス流路31内は再び一定の低酸素分圧に
保たれる。この酸素排出に要した酸素ポンプ32
の電気量を測定する(たとえば電流iを介して測
定することにより、試料33中の酸素量が、迅速
かつ高精度で絶対値測定される。
As shown in FIG. 7, this oxygen analyzer has an eighth
As shown in the figure, for example, an electrochemical oxygen pump 32 using a solid electrolyte 35 formed by dissolving a stabilizer such as calcia, magnesia, or ittria in zirconia is interposed, and the oxygen pump 32
By applying a constant DC voltage V to the closed gas flow path 31, oxygen is exhausted from the closed gas flow path 31.
This makes it possible to maintain the oxygen partial pressure inside the tank at a sufficiently low constant value. Before measurement, the oxygen in the carrier gas is exhausted and the inside of the closed gas flow path 31 is maintained at a sufficiently low constant oxygen partial pressure, and the sample 33 is introduced into the closed gas flow path 31 in this state. Oxygen released from the introduced sample 33 (in the case of a sample with a high melting point, oxygen is quickly released by melting it in the sample melting furnace 34) is transported to the oxygen pump 32 by a carrier gas. The oxygen is discharged to the outside of the closed gas flow path 31 by the oxygen pump 32, and the inside of the closed gas flow path 31 is again maintained at a constant low oxygen partial pressure. Oxygen pump 32 required for this oxygen discharge
By measuring the quantity of electricity (for example via the current i), the amount of oxygen in the sample 33 is determined quickly and precisely in absolute value.

このような酸素分析装置においてはキヤリアガ
スとしては水素を含有する還元性ガスを用いると
便利である。キヤリアガス中に水素が含有されて
いると、特に金属等の試料に含まれる酸素を測定
する場合、試料中の酸素がキヤリアガス中の水素
と反応してH2Oガスとなり、試料中からの酸素
の放出が効率的に行なわれ、このH2Oガスはキ
ヤリアガスによつて酸素ポンプへと運ばれる。酸
素ポンプで固体電解質の閉ガス流路側界面で再び
H2Oが還元されて酸素が放出され、その酸素が
酸素ポンプによつて閉ガス流路外に排出される。
In such an oxygen analyzer, it is convenient to use a reducing gas containing hydrogen as the carrier gas. If hydrogen is contained in the carrier gas, especially when measuring oxygen contained in a sample such as a metal, the oxygen in the sample will react with the hydrogen in the carrier gas to form H 2 O gas, and the oxygen in the sample will be removed. Efficient release occurs and this H 2 O gas is carried by the carrier gas to the oxygen pump. Again at the interface of the closed gas flow path of the solid electrolyte using the oxygen pump.
The H 2 O is reduced to release oxygen, which is pumped out of the closed gas flow path by an oxygen pump.

次に水素ポンプについて以下に述べる。 Next, the hydrogen pump will be described below.

酸素ストロンチウム、酸化セリウムを主成分と
したプロトン導電性固体電解質などは、固体電解
質隔壁の両側に直流電圧を印加することによつ
て、水素または水蒸気雰囲気下で固体電解質隔壁
の一方側から他方側へ水素を移動可能なことが知
られている(Solid State Ionics 9&10、1983
年、1021〜1026頁)。
Proton-conductive solid electrolytes containing strontium oxygen or cerium oxide as main components can be transferred from one side of the solid electrolyte partition wall to the other in a hydrogen or water vapor atmosphere by applying a DC voltage to both sides of the solid electrolyte partition wall. It is known that hydrogen can be transferred (Solid State Ionics 9 & 10, 1983
(2013, pp. 1021-1026).

水素ポンプの例として第9図に示すように、三
酸化セリウムストロンチウムを母体とした水素イ
オン導電性固体質40を隔壁として、その両側を
セラミツクス管43ではさみ、固体電解質40と
セラミツクス管43との間はガラスのパツキン4
4でシールされ、ガス室A、ガス室Bが形成され
ている。固体電解質40は、加熱炉45に収容さ
れ、固体電解質40の両面にはPt多孔質電極4
6が設けられ、リード線47が接続されている。
ガス室Aおよびガス室Bには、アルゴンと水素の
混合ガスが流れており、リード線47を通して直
流電圧を印加すると、その電圧の大きさおよび極
性に応じて、固体電解質40の一方の側(または
他方の側)から他方の側(または一方の側)へ、
固体電解質40の中を水素イオンが移動する。す
なわち、固体電解質40の水素イオン導電性によ
つて、一方のガス室(または他方のガス室)中の
水素を、他方のガス室(または一方のガス室)へ
移動させることができる。
As an example of a hydrogen pump, as shown in FIG. 9, a hydrogen ion conductive solid material 40 made of cerium strontium trioxide is used as a partition wall, and both sides of the hydrogen ion conductive solid material 40 are sandwiched between ceramic tubes 43. There is a glass patch between 4
4 to form a gas chamber A and a gas chamber B. The solid electrolyte 40 is housed in a heating furnace 45, and Pt porous electrodes 4 are provided on both sides of the solid electrolyte 40.
6 is provided, and a lead wire 47 is connected thereto.
A mixed gas of argon and hydrogen flows in the gas chambers A and B, and when a DC voltage is applied through the lead wire 47, one side of the solid electrolyte 40 ( or the other side) to the other side (or one side),
Hydrogen ions move within the solid electrolyte 40. That is, hydrogen in one gas chamber (or the other gas chamber) can be moved to the other gas chamber (or one gas chamber) due to the hydrogen ion conductivity of the solid electrolyte 40.

この発明においては、かかる水素ポンプの原理
を、従来の酸素分析装置に応用する。
In this invention, the principle of such a hydrogen pump is applied to a conventional oxygen analyzer.

[発明が解決しようとする問題点] 上記のような酸素分析装置においては、H2O
の形で運ばれる試料33からの放出酸素が酸素ポ
ンプ32部で還元され、閉ガス流炉31内には元
のH2だけが残るので、キヤリアガス中の水素は
本質的には消費されない。しかしながら、長時
間、酸素分析装置を使用しているうちに、閉ガス
流路31を構成する配管等から、キヤリアガス中
の水素が洩れたり、拡散透過したりすることがあ
り、キヤリアガス中の水素濃度が所定の範囲より
も低下してしまうおそれがある。水素濃度が低下
しすぎると、前述の如き試料33からの酸素の放
出効率が低下するため、常時キヤリアガス中の水
素濃度を所定の範囲に保つ必要がある。
[Problems to be solved by the invention] In the oxygen analyzer as described above, H 2 O
Since the released oxygen from the sample 33 carried in the form of is reduced in the oxygen pump 32 section and only the original H2 remains in the closed gas flow furnace 31, the hydrogen in the carrier gas is essentially not consumed. However, while using the oxygen analyzer for a long time, hydrogen in the carrier gas may leak or diffuse permeate from the piping etc. that make up the closed gas flow path 31, resulting in hydrogen concentration in the carrier gas. may fall below a predetermined range. If the hydrogen concentration decreases too much, the efficiency of releasing oxygen from the sample 33 as described above will decrease, so it is necessary to always maintain the hydrogen concentration in the carrier gas within a predetermined range.

また、酸素ポンプに水素を含んだキヤリアガス
が長時間流れることによつて、酸素ポンプ固体電
解質の閉ガス流路側が水素によつて還元され、酸
素ポンプの性能が低下するおそれがある。
Furthermore, when the carrier gas containing hydrogen flows through the oxygen pump for a long time, the closed gas flow path side of the oxygen pump solid electrolyte is reduced by hydrogen, which may reduce the performance of the oxygen pump.

このような問題点に着目し検討を加えた結果、
上記の酸素分析装置に電気化学的水素ポンプを付
加することによつて、これらの問題点を解決でき
ることが判明し、さらに試料中の酸素濃度のみな
らず水素濃度についてもその絶対値測定が可能で
あることが本発明者によつて判明した。
As a result of focusing on and considering these issues, we found that
It has been found that these problems can be solved by adding an electrochemical hydrogen pump to the oxygen analyzer mentioned above, and it is also possible to measure the absolute value of not only the oxygen concentration but also the hydrogen concentration in the sample. The inventor has discovered that there is.

本発明は、試料からの酸素の放出効率の低下を
防止することができ、かつ酸素ポンプ固体電解質
の閉ガス流路側がキヤリアガス中の水素によつて
還元されることによる酸素ポンプの性能の低下を
防止することができ、さらに試料中の酸素濃度お
よび水素濃度の絶対値を同時に測定できる酸素お
よび水素分析装置を提供することを目的とする。
The present invention can prevent a decrease in the efficiency of releasing oxygen from a sample, and can also prevent a decrease in the performance of the oxygen pump due to reduction of the closed gas flow path side of the oxygen pump solid electrolyte by hydrogen in the carrier gas. It is an object of the present invention to provide an oxygen and hydrogen analyzer that can prevent such problems and simultaneously measure the absolute values of oxygen and hydrogen concentrations in a sample.

[問題点を解決するための手段] 上記の目的を達成するために、この発明におい
ては、キヤリアガスを循環させる閉ガス流路に、
該閉ガス流路に試料を導入する試料導入手段と、
前記閉ガス流路内の酸素を閉ガス流路外に排出す
る、固体電解質を用いた電気化学的酸素ポンプと
を、互いに直列に配置した分析装置において、ガ
ス循環方向に対して前記試料導入手段の上流側お
よび下流側の前記閉ガス流路に、それぞれ固体電
解質を用いた電気化学的水素ポンプを設けたこと
を特徴とする酸素および水素同時分析装置が提供
される。また、この発明においては、上記目的を
達成するために、キヤリアガスを循環させる閉ガ
ス流路に、該閉ガス流路に試料を導入する試料導
入手段と、該試料導入手段からの試料を溶解させ
試料中の酸素を閉ガス流路内に放出させる試料溶
解炉と、前記閉ガス流路内の酸素を閉ガス流路外
に排出する、固体電解質を用いた電気化学的ポン
プとを、互いに直列に配置した酸素分析装置にお
いて、ガス循環方向に対して前記試料溶解炉の上
流側および下流側の前記閉ガス流路に、それぞれ
固体電解質を用いた電気化学的水素ポンプを設け
たことを特徴とする酸素および水素同時分析装置
が提供される。
[Means for Solving the Problems] In order to achieve the above object, the present invention includes a closed gas flow path for circulating carrier gas,
sample introduction means for introducing a sample into the closed gas flow path;
In an analyzer in which an electrochemical oxygen pump using a solid electrolyte that discharges oxygen in the closed gas flow path to the outside of the closed gas flow path is arranged in series with the sample introduction means in the gas circulation direction. Provided is a simultaneous oxygen and hydrogen analysis device, characterized in that electrochemical hydrogen pumps using solid electrolytes are provided in the closed gas flow paths on the upstream and downstream sides of the gas flow path. In addition, in order to achieve the above object, the present invention includes a sample introduction means for introducing a sample into the closed gas flow path in which a carrier gas is circulated, and a sample introduced from the sample introduction means is dissolved. A sample melting furnace that releases oxygen in the sample into a closed gas flow path and an electrochemical pump using a solid electrolyte that discharges oxygen in the closed gas flow path outside the closed gas flow path are connected in series with each other. in the oxygen analyzer disposed in the oxygen analyzer, wherein electrochemical hydrogen pumps using solid electrolytes are provided in the closed gas flow paths on the upstream and downstream sides of the sample melting furnace with respect to the gas circulation direction, respectively. A simultaneous oxygen and hydrogen analyzer is provided.

[実施例] 以下に、本発明の装置の一実施態様を、金属な
どに含まれる酸素および水素を同時に分析する場
合について図面を参照して説明する。
[Example] Hereinafter, one embodiment of the apparatus of the present invention will be described with reference to the drawings for the case where oxygen and hydrogen contained in metals and the like are simultaneously analyzed.

第1図は、本発明の一実施例に係る酸素および
水素同時分析装置(以下、本装置という)を示し
ている。図は本装置の全体構成図を示しており、
各方向切換弁は試料の酸素量および水素量分析時
(以下、分析時という)の状態を示している。
FIG. 1 shows a simultaneous oxygen and hydrogen analysis device (hereinafter referred to as the present device) according to an embodiment of the present invention. The figure shows the overall configuration of this device.
Each directional switching valve indicates the state at the time of analysis of the oxygen content and hydrogen content of the sample (hereinafter referred to as the time of analysis).

第1図において、太線で示した経路が、試料の
分析時の、例えばアルゴンガスなどのキヤリアガ
スが循環される閉ガス流路1を示している。各方
向切換弁2,3は、本実施例では4方弁からなつ
ており、試料の分析時には図に示すように閉ガス
流路1内のキヤリアガスを太線矢印Aの方向に流
し、最初閉ガス流路1内のガスをキヤリアガスで
置換する際には実線矢印Bの方向に流す。
In FIG. 1, a path indicated by a thick line indicates a closed gas flow path 1 through which a carrier gas such as argon gas is circulated during analysis of a sample. Each of the directional switching valves 2 and 3 is a four-way valve in this embodiment, and when analyzing a sample, the carrier gas in the closed gas flow path 1 is made to flow in the direction of the bold arrow A, as shown in the figure, and the closed gas is initially When replacing the gas in the flow path 1 with the carrier gas, the gas is caused to flow in the direction of the solid line arrow B.

閉ガス流路1には、測定時のキヤリアガスの循
環方向Aに沿つて、キヤリアガスを循環させる循
環ポンプ4、系内に水素を導入する電気化学的水
素ポンプ21(以下、水素ポンプという)、金属、
合金、またはそれらの化合物からなる試料6を閉
ガス流路1内に導入する試料導入手段7、試料6
を加熱装置8による加熱により試料溶解管9内で
溶解させ試料6中の酸素および水素を放出させる
試料溶解炉10、試料6から放出されキヤリアガ
スによつて運ばれて来た水素を閉ガス流路1外に
排出する固体電解質22を用いた水素ポンプ2
3、試料6から放出され、キヤリアガスによつて
運ばれてきた酸素を閉ガス流路1外に排出する固
体電解質11を用いた電気化学的酸素ポンプ12
(以下、酸素ポンプという)が直列に配置されて
いる。
The closed gas flow path 1 includes, along the carrier gas circulation direction A during measurement, a circulation pump 4 that circulates carrier gas, an electrochemical hydrogen pump 21 (hereinafter referred to as hydrogen pump) that introduces hydrogen into the system, and a metal pump. ,
A sample introduction means 7 for introducing a sample 6 made of an alloy or a compound thereof into the closed gas flow path 1, and a sample 6
A sample melting furnace 10 melts the sample 6 in a sample melting tube 9 by heating with a heating device 8 to release oxygen and hydrogen in the sample 6, and a closed gas flow path in which the hydrogen released from the sample 6 and carried by the carrier gas is melted in a sample melting tube 9. 1 Hydrogen pump 2 using a solid electrolyte 22 discharged to the outside
3. Electrochemical oxygen pump 12 using a solid electrolyte 11 that discharges oxygen released from the sample 6 and carried by the carrier gas to the outside of the closed gas flow path 1
(hereinafter referred to as oxygen pumps) are arranged in series.

循環ポンプ4の上流側には、循環ポンプ4によ
つて循環されるキヤリアガスの流量(流速)を測
定可能な流量計5が設けられている。また、酸素
ポンプ12と循環ポンプ4との間には、キヤリア
ガスを閉ガス流路1内に導入するキヤリアガス導
入口13が接続されており、フイルタ14、方向
切換弁2を介してキヤリアガスが導入されるよう
になつている。この閉ガス流路1をキヤリアガス
で置換する際には、方向切換弁2,3は矢印Bの
ように切替えられるが、その経路の終端部には減
圧吸引口15が接続されており、キヤリアガス供
給によつて追い出されてきた閉ガス流路1内のガ
スが、フイルタ16、吸引ポンプ17を介して系
外に排出される。
A flow meter 5 that can measure the flow rate (flow velocity) of the carrier gas circulated by the circulation pump 4 is provided upstream of the circulation pump 4 . Further, a carrier gas inlet 13 for introducing carrier gas into the closed gas flow path 1 is connected between the oxygen pump 12 and the circulation pump 4, and the carrier gas is introduced through the filter 14 and the directional switching valve 2. It is becoming more and more like this. When replacing this closed gas flow path 1 with carrier gas, the directional control valves 2 and 3 are switched as shown by arrow B, but a reduced pressure suction port 15 is connected to the end of the path to supply carrier gas. The gas in the closed gas flow path 1 that has been expelled by the pump is discharged to the outside of the system via the filter 16 and the suction pump 17.

試料導入手段7は、大気に対して密閉可能な容
器状に構成されており、試料6を載置し回動等に
より試料6を下方に落下させる試料受け18が設
けられている。試料導入手段7の下部に、試料溶
解炉10が接続されている。試料溶解炉10の加
熱装置8と試料導入手段7との間には、加熱装置
8側から試料導入手段7側への伝熱を抑制すると
ともに、試料溶解炉10からの金属蒸気などを凝
縮させて下流側への流出を抑制する適当な冷却手
段19が設けられている。
The sample introducing means 7 is configured in the shape of a container that can be sealed against the atmosphere, and is provided with a sample receiver 18 on which the sample 6 is placed and allows the sample 6 to fall downward by rotation or the like. A sample melting furnace 10 is connected to the lower part of the sample introducing means 7. There is a space between the heating device 8 of the sample melting furnace 10 and the sample introducing means 7 to suppress heat transfer from the heating device 8 side to the sample introducing means 7 side and to condense metal vapor etc. from the sample melting furnace 10. Appropriate cooling means 19 are provided to suppress outflow to the downstream side.

上述した水素ポンプ21は、第2図に示すよう
に、加熱炉21aと、この加熱炉21a内に収容
された円筒状の固体電解質20を備えている。固
体電解質20の内外面には、多孔質電極a1,a
2が設けられ、それぞれの電極にはリード線a
5,a6が接続されている。リード線a5,a6
の間には、電圧印加手段としての直流電源a3が
接続され、またその直流電源と直列に電流測定手
段としての電流計a4が接続されている。
As shown in FIG. 2, the above-described hydrogen pump 21 includes a heating furnace 21a and a cylindrical solid electrolyte 20 housed within the heating furnace 21a. On the inner and outer surfaces of the solid electrolyte 20, porous electrodes a1, a
2 is provided, and each electrode has a lead wire a.
5 and a6 are connected. Lead wire a5, a6
A DC power supply a3 serving as a voltage applying means is connected between the two, and an ammeter a4 serving as a current measuring means is connected in series with the DC power supply.

水素ポンプ21の固体電解質20の外面側に
は、常時たとえば0.01〜10%の水素を含むアルゴ
ンガスを流しておき、固体電解質20の内側電極
にマイナス、外側電極にプラスの直流電圧を印加
することにより、固体電解質20の外面側近傍を
流れる水素を含むアルゴンガス中の水素を、固体
電解質20の水素イオン伝導を介して閉ガス流路
内へ導入できるようになつている。
Argon gas containing, for example, 0.01 to 10% hydrogen is constantly flowing through the outer surface of the solid electrolyte 20 of the hydrogen pump 21, and a negative DC voltage is applied to the inner electrode of the solid electrolyte 20 and a positive DC voltage to the outer electrode. As a result, hydrogen in the hydrogen-containing argon gas flowing near the outer surface of the solid electrolyte 20 can be introduced into the closed gas flow path through hydrogen ion conduction of the solid electrolyte 20.

次に、水素ポンプ23は、第3図に示すよう
に、加熱炉23bと、この加熱炉23b内に収容
された円筒状の固体電解質22を備えている。固
体電解質22の内外面には、多孔質電極b1,b
2が設けられ、それぞれの電極にはリード線b
5,b6が接続されている。リード線b5,b6
の間には、それぞれ電圧印加手段としての直流電
源b3が接続され、またその直流電源と直列に電
流測定手段としての電流計b4または電気量測定
手段としての電気量計(図示せず)が接続されて
いる。
Next, as shown in FIG. 3, the hydrogen pump 23 includes a heating furnace 23b and a cylindrical solid electrolyte 22 housed within the heating furnace 23b. Porous electrodes b1, b are provided on the inner and outer surfaces of the solid electrolyte 22.
2 is provided, and each electrode has a lead wire b
5 and b6 are connected. Lead wires b5, b6
A DC power supply b3 as a voltage applying means is connected between them, and an ammeter b4 as a current measuring means or a electricity meter (not shown) as a means for measuring an electrical quantity is connected in series with the DC power supply. has been done.

そして、水素ポンプ23の固体電解質22の外
面側には、常時たとえばアルゴンガスを流してお
き、固体電解質22の内側電極にプラス、外側電
極にマイナスの直流電圧を印加することにより、
閉ガス流路内を流れるキヤリアガス中の水素を、
固体電解質22の水素イオン伝導を介して閉ガス
流路外へ排出できるようになつている。
Then, by constantly flowing, for example, argon gas through the outer surface of the solid electrolyte 22 of the hydrogen pump 23, and applying a positive DC voltage to the inner electrode of the solid electrolyte 22 and a negative DC voltage to the outer electrode,
The hydrogen in the carrier gas flowing in the closed gas flow path is
The solid electrolyte 22 can be discharged to the outside of the closed gas flow path through hydrogen ion conduction.

次に、酸素ポンプ12は、第4図に示すよう
に、加熱炉12cと、この加熱炉12c内に収容
された円筒状の固体電解質11を備えている。固
体電解質11の内外面には、多孔質電極c1,c
2が設けられ、それぞれの電極にはリード線c
5,c6が接続されている。リード線c5,c6
の間には、それぞれ電圧印加手段としての直流電
源c3が接続され、またその直流電源と直列に電
流測定手段としての電流計c4または電気量測定
手段としての電気量計(図示せず)が接続されて
いる。
Next, as shown in FIG. 4, the oxygen pump 12 includes a heating furnace 12c and a cylindrical solid electrolyte 11 housed within the heating furnace 12c. Porous electrodes c1, c are provided on the inner and outer surfaces of the solid electrolyte 11.
2 is provided, and each electrode has a lead wire c
5 and c6 are connected. Lead wire c5, c6
A DC power supply c3 as a voltage applying means is connected between them, and an ammeter c4 as a current measuring means or a electricity meter (not shown) as a means for measuring an electrical quantity is connected in series with the DC power supply. has been done.

そして酸素ポンプ12の固体電解質11の外側
電極にプラス、内側電極にマイナスの直流電圧を
印加することにより、閉ガス流路内を流れるキヤ
リアガス中の酸素を、固体電解質11の酸素イオ
ン伝導を介して閉ガス流路外へ排出できるように
なつている。
By applying a positive DC voltage to the outer electrode of the solid electrolyte 11 of the oxygen pump 12 and a negative DC voltage to the inner electrode, oxygen in the carrier gas flowing in the closed gas flow path is transferred through oxygen ion conduction of the solid electrolyte 11. It is designed to be able to be discharged outside the closed gas flow path.

上記のように構成された実施例装置の作用につ
いて以下に説明する。
The operation of the embodiment device configured as described above will be explained below.

まず、試料の分析前には、酸素ポンプ12によ
りキヤリアガスから酸素が排出され、閉ガス流路
1内の酸素分圧は十分に低い一定値に保たれ、こ
のとき酸素ポンプ12には一定のベース電流が流
れている。
First, before analyzing a sample, oxygen is discharged from the carrier gas by the oxygen pump 12, and the oxygen partial pressure in the closed gas flow path 1 is kept at a sufficiently low constant value. Current is flowing.

第5図にリード線c5,c6を流れる電流に対
応した固体電解質11を流れる電流とその電流
成分の時間tに関する変化の様子を示す。固体電
解質11には印加電圧に対応した、時間tに依存
しない一定の電子電流Ie*が常に流れている。固
体電解質11から放出される酸素によるイオン電
流は、上記測定条件下では事実上時間tに依存せ
ず、一定とみなしてよく、また大気中から閉ガス
流路1内にわずかに漏洩してくる酸素の排出に伴
うイオン電流も時間tに依存せず一定である。し
たがつて、これら2つの寄与により測定中に常時
流れているイオン電流をI′0とすると、測定の間
に常に固体電解質11に流れる電流は I0∽=Ie*+I′0 となる。
FIG. 5 shows the current flowing through the solid electrolyte 11 corresponding to the current flowing through the lead wires c5 and c6, and how the current component changes with respect to time t. A constant electron current Ie * corresponding to the applied voltage and independent of time t always flows through the solid electrolyte 11. The ionic current due to oxygen released from the solid electrolyte 11 is virtually independent of time t under the above measurement conditions and can be regarded as constant, and also slightly leaks from the atmosphere into the closed gas flow path 1. The ionic current accompanying the discharge of oxygen is also constant and independent of time t. Therefore, if the ionic current that constantly flows during the measurement due to these two contributions is I' 0 , then the current that always flows through the solid electrolyte 11 during the measurement is I 0 ∽=Ie * +I' 0 .

また水素ポンプ21に一定の電流を常時流すこ
とによつて、閉ガス流路1内に常時水素が導入さ
れている。この水素はキヤリアガスト共に溶解炉
を通過して流れ水素ポンプ23に至り、ここで水
素ポンプ23で閉ガス流路1外へ排出される。し
たがつて溶解炉を流れるキヤリアガス中の水素濃
度は、常時或る所定の範囲内に保たれ、かつ酸素
ポンプには水素の存在しないキヤリアガスが流れ
る。このとき水素ポンプ23には一定のベース電
流IH∽が流れている。第6図にリード線b5,b
6を流れる電流に対応した、固体電解質22を流
れる電流Iと、その電流成分の時間tに関する変
化の様子を示す。固体電解質22にはキヤリアガ
ス中の水素の排出による水素イオン電流IH′の他
に、時間tに依存しない一定の電子電流I′eや、
その他の電荷担体として酸素イオンなどによる電
流I′ionも含まれる場合があり、これも時間tに
依存しない。したがつて、これら2つの寄与によ
る測定中に常時流れている電流をI'とすると測定
の間に常に固体電解質22に流れる電流は IH∽=IH′+I′となる。
Furthermore, hydrogen is constantly introduced into the closed gas flow path 1 by constantly supplying a constant current to the hydrogen pump 21. This hydrogen passes through the melting furnace together with the carrier gas and reaches the hydrogen pump 23, where it is discharged out of the closed gas flow path 1 by the hydrogen pump 23. Therefore, the hydrogen concentration in the carrier gas flowing through the melting furnace is always kept within a certain predetermined range, and the carrier gas without hydrogen flows through the oxygen pump. At this time, a constant base current I H ∽ flows through the hydrogen pump 23. Figure 6 shows lead wires b5 and b.
6 shows the current I flowing through the solid electrolyte 22 corresponding to the current flowing through the solid electrolyte 22 and how the current component changes with respect to time t. In the solid electrolyte 22, in addition to the hydrogen ion current I H ' due to the discharge of hydrogen in the carrier gas, there is also a constant electron current I'e that does not depend on time t,
Other charge carriers may include current I'ion due to oxygen ions, etc., which also does not depend on time t. Therefore, if the current constantly flowing during the measurement due to these two contributions is I', the current constantly flowing through the solid electrolyte 22 during the measurement is I H ∽=I H ′+I′.

この状態で試料6が試料溶解炉10に落下さ
れ、試料6が溶解されて試料6中の酸素および水
素が放出される。試料から放出された水素はキヤ
リアガスによつて水素ポンプ23へと運ばれ水素
ポンプ23により閉ガス流路1外へ排出される。
このとき水素ポンプ23の電流は急速に立ち上が
り、水素ポンプ23のポンプ機能によつて水素が
排出されるのに伴い、時間t′2後には速やかにも
とのベース電流IH∽にもどる。ここで、固体電解
質22の平均水素イオン輸率をTpとすると、理
論的に次式が成立する。
In this state, the sample 6 is dropped into the sample melting furnace 10, the sample 6 is melted, and the oxygen and hydrogen in the sample 6 are released. Hydrogen released from the sample is carried by the carrier gas to the hydrogen pump 23 and discharged to the outside of the closed gas flow path 1 by the hydrogen pump 23.
At this time, the current of the hydrogen pump 23 rises rapidly, and as hydrogen is discharged by the pumping function of the hydrogen pump 23, it quickly returns to the original base current I H ∽ after time t' 2 . Here, if the average hydrogen ion transfer number of the solid electrolyte 22 is Tp, the following equation holds theoretically.

TH=IH/(IH+Ie) ただし IH:放出水素を閉ガス流路1外に排出する際にそ
の放出水素によつて水素ポンプ23に流れるイ
オン電流 Ie:イオン電流IHに依存する電子電
流 したがつて、使用に際してTH≒1の条件下で
水素ポンプを作動させると、一定電流値IH∽から
増大した電流IHはすべて試料6中に水素によるも
のとみなせる。しかして、その時の水素イオン電
流IHによる電気量QHは、試料6から発生した水素
量をXHグラム、フアラデー定数をF、水素の原
子量をMHとすると、 QH=XH・F/MH=∫t2t1′IHdt となり、これから、試料6中の水素濃度を知るこ
とができるわけである。TH≒1の条件が満足で
きない条件下では、あらかじめ校正しておき、そ
のときの補正係数Kを用いて QH=K・XH・F/MH=∫t2t1′IHdt となり、これから、試料6中の水素濃度を求める
ことができる。
T H = I H / (I H + Ie) where I H : Ion current flowing through the hydrogen pump 23 due to the released hydrogen when the released hydrogen is discharged outside the closed gas flow path 1 Ie: Depends on the ionic current I H Therefore, when the hydrogen pump is operated under the condition of T H ≈1, all of the current I H that increases from a constant current value I H ∽ can be considered to be due to the hydrogen in the sample 6. Therefore, the quantity of electricity Q H due to the hydrogen ion current I H at that time is Q H = X H・F, where the amount of hydrogen generated from sample 6 is X H grams, Faraday's constant is F , and the atomic weight of hydrogen is M H. /M H =∫ t2t1 ′I Hdt , and from this, the hydrogen concentration in sample 6 can be determined. Under conditions where the condition of T H ≒ 1 cannot be satisfied, calibrate in advance and use the correction coefficient K at that time to obtain Q H = K・X H・F/M H =∫ t2t1 ′I Hdt , From this, the hydrogen concentration in sample 6 can be determined.

また試料から放出された酸素はキヤリアガスに
よつて酸素ポンプ12へと運ばれ酸素ポンプ12
により閉ガス流路1外へ排出され、このとき酸素
ポンプ12の電流は第5図に示すように、急速に
立ち上がり酸素ポンプ12のポンプ機能によつて
酸素が排出されるのに伴い、時間t2後には速やか
にもとのベース電流にもどる。ここで、固体電解
質11の平均酸素イオン輸率をT0とすると、理
論的に次式が成立する。
In addition, the oxygen released from the sample is transported to the oxygen pump 12 by a carrier gas.
At this time, as shown in FIG. 5, the current of the oxygen pump 12 rises rapidly and as oxygen is discharged by the pumping function of the oxygen pump 12, the current of the oxygen pump 12 is discharged to the outside of the closed gas flow path 1. After 2 , the current returns to the original base current. Here, if the average oxygen ion transfer number of the solid electrolyte 11 is T 0 , the following equation holds theoretically.

T0=I0/(I0+Ie) ただし I0:放出酸素を閉ガス流路1外に排出する際にそ
の放出酸素によつて酸素ポンプ12に流れるイ
オン電流 Ie:イオン電流I0に依存する電子電流 したがつて、使用に際してT0≒1の条件下で
酸素ポンプを作動させると、一定電流値I0∽から
増大した電流I0はすべて試料6中の酸素によるも
のとみなせる。しかして、その時の酸素イオン電
流I0による電気量Q0は、試料6から発生した酸素
をX0グラム、フアラデー定数をF、酸素の原子
量をM0とすると、 Q0=X0・2F/M0=∫t2 t1I0dt となり、これから、試料6中の酸素濃度を知るこ
とができる。
T 0 = I 0 / (I 0 + Ie) where I 0 : Ion current flowing through the oxygen pump 12 by the released oxygen when the released oxygen is discharged outside the closed gas flow path 1 Ie: Depends on the ionic current I 0 Therefore, when the oxygen pump is operated under the condition of T 0 ≈1, the current I 0 that increases from the constant current value I 0 ∽ can be considered to be entirely due to the oxygen in the sample 6. Therefore, the quantity of electricity Q 0 due to the oxygen ion current I 0 at that time is Q 0 = X 0・2F/ M 0 =∫ t2 t1 I 0 dt From this, the oxygen concentration in the sample 6 can be determined.

以上においては、金属などに含まれている酸素
および水素の濃度を測定する場合について説明し
たが、この発明の装置によれば、全く同様にして
ガス中の酸素および水素の濃度を測定するとがで
きる。ただし、その場合は試料注入器として一定
量のガスを注入することができるものを使用す
る。
In the above, the case of measuring the concentration of oxygen and hydrogen contained in metal etc. has been explained, but according to the apparatus of the present invention, the concentration of oxygen and hydrogen in gas can be measured in exactly the same way. . However, in that case, use a sample injector that can inject a certain amount of gas.

試料溶解炉は必要でない。 A sample melting furnace is not required.

[発明の効果] この発明の装置は、閉ガス流路を採用し、その
閉ガス流路にリード線を備えた酸素ポンプおよび
水素ポンプを配置しているから、ガス流路側にお
ける固体電解質と電極との界面の化学ポテンシヤ
ルを常時一定に保つことができるようになり、し
かもその状態で試料を投入するから、酸素ポンプ
にあつては固体電解質が示す電子伝導性、固体電
解質そのものから放出される酸素や大気中から漏
洩してくる酸素の影響を受けないで酸素濃度を測
定でき、また水素ポンプにあつては、固体電解質
に流れる電子電流や、その他の電荷担体による電
流の影響を受けないで水素濃度を測定することが
できる。そのため、測定感度および測定精度に優
れ、また、標準試料を全く必要とせず、酸素濃度
および水素濃度の絶対値を測定することができ
る。
[Effects of the Invention] The device of the present invention employs a closed gas flow path, and an oxygen pump and a hydrogen pump equipped with lead wires are disposed in the closed gas flow path, so that the solid electrolyte and electrodes on the gas flow path side are Since the chemical potential at the interface with the solid electrolyte can be kept constant at all times, and the sample is introduced in that state, in the case of an oxygen pump, the electronic conductivity of the solid electrolyte and the oxygen released from the solid electrolyte itself can be kept constant. Oxygen concentration can be measured without being affected by oxygen leaking from the air or the atmosphere, and in the case of hydrogen pumps, hydrogen concentration can be measured without being affected by electron current flowing through the solid electrolyte or current by other charge carriers. Concentration can be measured. Therefore, the measurement sensitivity and measurement accuracy are excellent, and the absolute values of oxygen concentration and hydrogen concentration can be measured without any need for a standard sample.

また試料溶解炉の上流側に設けた水素ポンプに
よつて閉ガス流路内に水素を導入し、試料溶解炉
の下流側の水素ポンプによつて閉ガス流路外に水
素を排出するため、試料溶解部を流れるキヤリア
ガス中の水素濃度は、常に所定の濃度範囲内に保
たれる。そのため、試料中の酸素がキヤリアガス
中の水素と反応してH2Oガスとなるため、試料
中の酸素の放出が効率良く行なわれる。また、キ
ヤリアガス中には極く微量の酸素が常に存在する
ため、試料中の水素はキヤリアガス中の酸素と反
応してH2Oガスとなるため、試料中の水素の放
出も効率良く行なわれることになる。
In addition, hydrogen is introduced into the closed gas flow path by a hydrogen pump installed upstream of the sample melting furnace, and hydrogen is discharged outside the closed gas flow path by a hydrogen pump installed downstream of the sample melting furnace. The hydrogen concentration in the carrier gas flowing through the sample dissolving section is always maintained within a predetermined concentration range. Therefore, oxygen in the sample reacts with hydrogen in the carrier gas to form H 2 O gas, so that oxygen in the sample is efficiently released. In addition, since a very small amount of oxygen is always present in the carrier gas, the hydrogen in the sample reacts with the oxygen in the carrier gas to form H 2 O gas, so the hydrogen in the sample is efficiently released. become.

また酸素ポンプには水素を含まないキヤリアガ
スが流れるため、酸素ポンプ固体電解質の閉ガス
流路側が水素によつて還元されることがなく、常
時、酸素ポンブの性能を維持することができる。
Further, since a carrier gas that does not contain hydrogen flows through the oxygen pump, the closed gas flow path side of the oxygen pump solid electrolyte is not reduced by hydrogen, and the performance of the oxygen pump can be maintained at all times.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の一実施態様を金属などに含
まれる酸素および水素を分析する場合について示
す、一部断面を含む酸素および水素同時分析装置
の全体構成図、第2図および第3図は、上記第1
図に示した電気化学的水素ポンプの概略縦断面
図、第4図は、上記第1図に示した電気化学的酸
素ポンプの概略縦断面図、第5図は、上記酸素ポ
ンプに発生する電流Iの時間tに対する変化を示
すグラフ、第6図は、上記水素ポンプに発生する
電流Iの時間tに対する変化を示すグラフ、第7
図は、従来から知られている酸素分析装置の全体
構成図、第8図は、第7図の装置の酸素ポンプの
概略縦断面図、第9図は、従来から知られている
水素ポンプの概略縦断面図、である。 1……閉ガス流路、2,3……方向切換弁、4
……循環ポンプ、5……流量計、6……試料、7
……試料導入手段、8……加熱装置、9……試料
溶解管、10……試料溶解炉、11……固体電解
質、12……酸素ポンプ、13……キヤリアガス
導入口、14……フイルタ、15……減圧吸引
口、16……フイルタ、17……吸引ポンプ、1
8……試料受け、19……冷却手段、20……固
体電解質、21……水素ポンプ、22……固体電
解質、23……水素ポンプ。
FIG. 1 is an overall configuration diagram of a simultaneous oxygen and hydrogen analysis device including a partial cross section, showing an embodiment of the present invention for analyzing oxygen and hydrogen contained in metals, etc. FIG. 2 and FIG. is the above first
FIG. 4 is a schematic vertical cross-sectional view of the electrochemical hydrogen pump shown in FIG. 1, FIG. 5 is a schematic vertical cross-sectional view of the electrochemical oxygen pump shown in FIG. A graph showing changes in I with respect to time t, FIG. 6 is a graph showing changes in current I generated in the hydrogen pump with respect to time t, FIG.
The figure is an overall configuration diagram of a conventionally known oxygen analyzer, FIG. 8 is a schematic vertical sectional view of the oxygen pump of the device in FIG. 7, and FIG. 9 is a diagram of a conventionally known hydrogen pump. It is a schematic longitudinal cross-sectional view. 1... Closed gas flow path, 2, 3... Directional switching valve, 4
... Circulation pump, 5 ... Flow meter, 6 ... Sample, 7
... Sample introduction means, 8 ... Heating device, 9 ... Sample melting tube, 10 ... Sample melting furnace, 11 ... Solid electrolyte, 12 ... Oxygen pump, 13 ... Carrier gas inlet, 14 ... Filter, 15...Decompression suction port, 16...Filter, 17...Suction pump, 1
8...Sample receiver, 19...Cooling means, 20...Solid electrolyte, 21...Hydrogen pump, 22...Solid electrolyte, 23...Hydrogen pump.

Claims (1)

【特許請求の範囲】 1 キヤリアガスを循環させる閉ガス流路に、該
閉ガス流路に試料を導入する試料導入手段と、前
記閉ガス流路内の酸素を閉ガス流路外に排出す
る、固体電解質を用いた電気化学的酸素ポンプと
を、互いに直列に配置した分析装置において、ガ
ス循環方向に対して前記試料導入手段の上流側お
よび下流側の前記閉ガス流路に、それぞれ固体電
解質を用いた電気化学的水素ポンプを設けたこと
を特徴とする酸素および水素同時分析装置。 2 キヤリアガスを循環させる閉ガス流路に、該
閉ガス流路に試料を導入する試料導入手段と、該
試料導入手段からの試料を溶解させ試料中の酸素
を閉ガス流路内に放出させる試料溶解炉と、前記
閉ガス流路内の酸素を閉ガス流路外に排出する、
固体電解質を用いた電気化学的酸素ポンプとを、
互いに直列に配置した酸素分析装置において、ガ
ス循環方向に対して前記試料溶解炉の上流側およ
び下流側の前記閉ガス流路に、それぞれ固体電解
質を用いた電気化学的水素ポンプを設けたことを
特徴とする酸素および水素同時分析装置。
[Scope of Claims] 1. Sample introducing means for introducing a sample into a closed gas flow path through which carrier gas is circulated, and discharging oxygen in the closed gas flow path to the outside of the closed gas flow path. In an analyzer in which an electrochemical oxygen pump using a solid electrolyte is arranged in series with each other, a solid electrolyte is provided in the closed gas flow path on the upstream side and the downstream side of the sample introducing means with respect to the gas circulation direction. A simultaneous oxygen and hydrogen analysis device characterized by being equipped with an electrochemical hydrogen pump. 2. A sample introduction means for introducing a sample into a closed gas flow path through which carrier gas is circulated, and a sample for dissolving the sample from the sample introduction means and releasing oxygen in the sample into the closed gas flow path. a melting furnace, and discharging oxygen in the closed gas flow path to the outside of the closed gas flow path;
An electrochemical oxygen pump using a solid electrolyte,
In oxygen analyzers arranged in series with each other, electrochemical hydrogen pumps using solid electrolytes are provided in the closed gas flow paths upstream and downstream of the sample melting furnace with respect to the gas circulation direction, respectively. Features: Oxygen and hydrogen simultaneous analyzer.
JP62142286A 1987-06-09 1987-06-09 Instrument for simultaneous analysis of oxygen and hydrogen Granted JPS63307351A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62142286A JPS63307351A (en) 1987-06-09 1987-06-09 Instrument for simultaneous analysis of oxygen and hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62142286A JPS63307351A (en) 1987-06-09 1987-06-09 Instrument for simultaneous analysis of oxygen and hydrogen

Publications (2)

Publication Number Publication Date
JPS63307351A JPS63307351A (en) 1988-12-15
JPH0513575B2 true JPH0513575B2 (en) 1993-02-22

Family

ID=15311840

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62142286A Granted JPS63307351A (en) 1987-06-09 1987-06-09 Instrument for simultaneous analysis of oxygen and hydrogen

Country Status (1)

Country Link
JP (1) JPS63307351A (en)

Also Published As

Publication number Publication date
JPS63307351A (en) 1988-12-15

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