JPH0450979B2 - - Google Patents
Info
- Publication number
- JPH0450979B2 JPH0450979B2 JP60211115A JP21111585A JPH0450979B2 JP H0450979 B2 JPH0450979 B2 JP H0450979B2 JP 60211115 A JP60211115 A JP 60211115A JP 21111585 A JP21111585 A JP 21111585A JP H0450979 B2 JPH0450979 B2 JP H0450979B2
- Authority
- JP
- Japan
- Prior art keywords
- sample
- tube
- oxygen
- 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
Links
- 229910052760 oxygen Inorganic materials 0.000 claims description 65
- 239000001301 oxygen Substances 0.000 claims description 65
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 63
- 239000007789 gas Substances 0.000 claims description 49
- 238000001304 sample melting Methods 0.000 claims description 32
- 239000012159 carrier gas Substances 0.000 claims description 22
- 239000007784 solid electrolyte Substances 0.000 claims description 4
- 239000000155 melt Substances 0.000 claims description 2
- 238000001816 cooling Methods 0.000 description 22
- 238000010438 heat treatment Methods 0.000 description 13
- 238000004090 dissolution Methods 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000003779 heat-resistant material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 150000002926 oxygen Chemical class 0.000 description 2
- 229910052711 selenium Inorganic materials 0.000 description 2
- 239000011669 selenium Substances 0.000 description 2
- 229910052714 tellurium Inorganic materials 0.000 description 2
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 241001480748 Argas Species 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052752 metalloid Inorganic materials 0.000 description 1
- 150000002738 metalloids Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- RUDFQVOCFDJEEF-UHFFFAOYSA-N yttrium(III) oxide Inorganic materials [O-2].[O-2].[O-2].[Y+3].[Y+3] RUDFQVOCFDJEEF-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Investigating And Analyzing Materials By Characteristic Methods (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
分析装置の改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an improvement in 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、テルル等の半金属に含まれる酸素
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装置が開発された(大塚
伸也、幸塚善作著、Transaction of the Japan
Institute of Metals.Vol−25,No.9639頁〜648頁、
1984年9月発行)。[Prior Art] Recently, a new type of oxygen analyzer has been developed that can measure the amount of oxygen contained in metals, alloys, their compounds, or metalloids such as selenium and tellurium with high precision and in absolute value. Developed (Shinya Otsuka, Zensaku Kozuka, Transaction of the Japan
Institute of Metals.Vol−25, No.9639-648,
(Published September 1984).
この酸素分析装置は、キヤリヤガスを循環させ
る閉ガス流路に、固体電解質を用いた電気化学的
酸素ポンプを介在せしめ、該酸素ポンプに一定の
直流電圧を印加することにより、閉ガス流路内か
ら酸素を排出して閉ガス流路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、キヤリヤガス中の酸素が排
出され、閉ガス流路内は十分に低い一定の酸素分
析圧に保たれ、その状態で閉ガス流路内に試料が
導入される。導入された試料は、試料溶解炉で加
熱溶解され、試料から酸素が放出される。試料か
ら放出された酸素は、キヤリヤガスによつて酸素
ポンプまで運ばれ、酸素ポンプにより閉ガス流路
外に排出されて、閉ガス流路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
ンプの電気量を測定することにより、試料中の酸
素量が、迅速かつ高精度で絶対値測定される。 This oxygen analyzer has an electrochemical oxygen pump using a solid electrolyte interposed in a closed gas flow path that circulates carrier gas, and by applying a constant DC voltage to the oxygen pump, By discharging oxygen, the oxygen partial pressure within the closed gas flow path can be maintained at a sufficiently low constant value. Before measurement, the oxygen in the carrier gas is exhausted, the inside of the closed gas flow path is maintained at a sufficiently low constant oxygen analysis pressure, and the sample is introduced into the closed gas flow path in this state. The introduced sample is heated and melted in a sample melting furnace, and oxygen is released from the sample. The oxygen released from the sample is carried by the carrier gas to the oxygen pump, and is discharged from the closed gas flow path by the oxygen pump, so that the inside of the closed gas flow path is again maintained at a constant low oxygen partial pressure. By measuring the amount of electricity required by the oxygen pump to discharge this oxygen, the amount of oxygen in the sample can be measured as an absolute value quickly and with high precision.
上記の酵素分析装置において、閉ガス流路への
試料導入手段部から試料溶解炉にかけての構造
は、従来第4図に示すように構成されていた。図
において、31が酸素ポンプ32を介在させた閉
ガス流路を示しており、キヤリヤガスの循環方向
Aに沿つて、上流側に試料33の導入手段34、
その下流側に試料溶解炉35が接続されている。
この試料溶解炉35は、シリカなどの耐熱材料か
らなるU字管状の試料溶解管36と、加熱装置3
7から成つている。また、試料溶解管36の下流
部は、溶解された試料の蒸気が下流側に流れるの
を抑えるために、金属蒸気等を凝縮させて試料溶
解炉35側に戻す冷却手段38が設けられてい
る。 In the enzyme analyzer described above, the structure from the sample introducing means to the closed gas flow path to the sample melting furnace has conventionally been constructed as shown in FIG. In the figure, 31 indicates a closed gas flow path in which an oxygen pump 32 is interposed, and along the carrier gas circulation direction A, an introduction means 34 for a sample 33 is provided on the upstream side;
A sample melting furnace 35 is connected to the downstream side thereof.
This sample melting furnace 35 includes a U-shaped sample melting tube 36 made of a heat-resistant material such as silica, and a heating device 3.
It consists of 7. Further, a cooling means 38 is provided downstream of the sample melting tube 36 to condense metal vapor and return it to the sample melting furnace 35 side in order to suppress the vapor of the melted sample from flowing downstream. .
[発明が解決しようとする問題点]
ところが、上記のように構成された酸素分析装
置においては、試料溶解管36がU字管から構成
されているので、試料溶解管36部の幅が大きく
なり、試料溶解炉35全体の小型化が難しい。試
料溶解管36、試料溶解炉35が大型であると、
熱容量が大きくなつて加熱効率が悪いという問題
がある。[Problems to be Solved by the Invention] However, in the oxygen analyzer configured as described above, since the sample dissolving tube 36 is composed of a U-shaped tube, the width of the sample dissolving tube 36 portion becomes large. However, it is difficult to downsize the sample melting furnace 35 as a whole. If the sample melting tube 36 and sample melting furnace 35 are large,
There is a problem that the heat capacity becomes large and the heating efficiency becomes poor.
また、U字管に曲げなければないため、材料に
よつては製作面で困難性が伴うとともに、U字管
底部の試料溶解部およびそのまわりに設けられる
加熱装置37の内面側構造が複雑になるという問
題もある。 In addition, since it has to be bent into a U-shaped tube, it may be difficult to manufacture depending on the material, and the inner structure of the sample melting section at the bottom of the U-shaped tube and the heating device 37 installed around it is complicated. There is also the issue of becoming.
さらに、冷却手段38が設けられる冷却部にお
いては、単なる管構造であるため、管中央部を流
れるガスや試料の蒸気を効率よく冷却するのが難
しいという問題もある。冷却部での冷却効率を上
げるため管径を大きくして冷却表面積を大にする
と、試料溶解管36の容積が不必要に大きくな
り、キヤリヤガスの望ましい流速が得られない等
の不都合を招き、また管外面側にフイン等を設け
ると、その分試料溶解炉35全体および冷却手段
38が大型になるという問題を招く。 Furthermore, since the cooling section in which the cooling means 38 is provided has a simple tube structure, there is a problem in that it is difficult to efficiently cool the gas or sample vapor flowing through the center of the tube. If the tube diameter is increased to increase the cooling surface area in order to increase the cooling efficiency in the cooling section, the volume of the sample dissolution tube 36 will become unnecessarily large, leading to inconveniences such as not being able to obtain the desired flow rate of the carrier gas. Providing fins or the like on the outer surface of the tube causes the problem that the entire sample melting furnace 35 and the cooling means 38 become larger.
本発明は、このような問題点に着目し、試料溶
解管および試料溶解管まわりの構造を簡素化する
と同時に小型化することができ、しかも加熱部、
冷却部での熱効率を高めることのできる酸素分析
装置を提供することを目的とする。 The present invention focuses on these problems, and allows the structure of the sample dissolution tube and its surroundings to be simplified and downsized at the same time.
An object of the present invention is to provide an oxygen analyzer that can increase thermal efficiency in a cooling section.
[問題点を解決するための手段]
この目的に沿う本発明の酸素分析装置は、キヤ
リヤガスを循環させる閉ガス流路に、該閉ガス流
路内に試料を導入する試料導入手段と、該試料導
入手段から導入された試料を溶解させる試料溶解
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、互に直列に配置した酸素分析装置にお
いて、前記試料溶解炉には試料溶解管を立設し、
該試料溶解管を、前記試料導入手段からの試料を
前記試料溶解管の底部に設けた試料溶解部に導く
内管と、前記試料溶解管部で溶解された試料から
のガスを前記内管との間を通して前記酸素ポンプ
側へと導く外管との二重管構造にしたものから成
つている。[Means for Solving the Problems] The oxygen analyzer of the present invention that meets this objective includes a sample introduction means for introducing a sample into a closed gas flow path in which a carrier gas is circulated, and a sample introduction means for introducing a sample into the closed gas flow path; A sample melting furnace that melts the sample introduced from the introducing means and 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 are connected in series with each other. In the installed oxygen analyzer, a sample melting tube is installed upright in the sample melting furnace,
The sample dissolving tube includes an inner tube that guides the sample from the sample introducing means to a sample dissolving section provided at the bottom of the sample dissolving tube, and an inner tube that conducts gas from the sample dissolved in the sample dissolving tube section. It has a double pipe structure with an outer pipe leading to the oxygen pump side through the space between the outer pipe and the outer pipe.
[作用]
このように構成された酸素分析装置において
は、二重管構造の内管内が、試料溶解部への試料
の導入通路として、内管と外管との間の横断面環
状の通路が、溶解された試料からのガス流路とし
て用いられる。[Function] In the oxygen analyzer configured as described above, the inside of the inner tube with a double tube structure serves as a passage for introducing the sample into the sample dissolving section, and the passage having an annular cross section between the inner tube and the outer tube serves as a passage for introducing the sample into the sample dissolving section. , used as a gas flow path from the dissolved sample.
この二重管において、内管、外管それぞれにつ
いてみれば、単なる管構造であるから、試料溶解
管全体としては簡素な構造をとることができ、し
かも内管から導入された試料からの放出ガスを、
その内管と外管との間から酸素ポンプ側へと送る
ことができるので、従来のU字管構造におけるU
字管の巾に比べ、二重管の外径を大巾に小とする
ことができる。したがつて、二重管底部に設けら
れる試料溶解部は、簡素な構造にされるとともに
小型化され、熱容量も必要最小限とされて熱効率
が従来構造に比べ高められる。 In this double-tube, the inner tube and outer tube each have a simple tube structure, so the sample dissolution tube as a whole can have a simple structure, and the gas released from the sample introduced from the inner tube of,
Since the oxygen can be sent from between the inner tube and the outer tube to the oxygen pump side, it is possible to
The outer diameter of the double tube can be made much smaller than the width of the double tube. Therefore, the sample melting section provided at the bottom of the double tube has a simple structure and is miniaturized, and the heat capacity is also minimized, so that the thermal efficiency is increased compared to the conventional structure.
また、試料からの放出ガスは、内管と外管との
間の環状通路を流れるので、流れ全体が、冷却面
である外管内周面近傍を通ることになり、管径を
大きくして冷却表面積をとくに増大させることな
く効率のよい冷却が行われる。 In addition, since the gas released from the sample flows through the annular passage between the inner tube and the outer tube, the entire flow passes near the inner peripheral surface of the outer tube, which is the cooling surface. Efficient cooling is achieved without particularly increasing the surface area.
[実施例]
以下に、本発明に係る望ましい実施例を、図面
を参照して説明する。[Embodiments] Preferred embodiments of the present invention will be described below with reference to the drawings.
第1図ないし第3図は、本発明の一実施例に係
る酸素分析装置を示している。第1図は酸素分析
装置の全体構成を示しており、各方向切換弁は、
試料の酸素量分析時の状態を示している。 1 to 3 show an oxygen analyzer according to an embodiment of the present invention. Figure 1 shows the overall configuration of the oxygen analyzer, and each directional valve is
This shows the state at the time of oxygen content analysis of the sample.
第1図において、太線で示した経路が、試料の
酸素量分析時に、たとえば0.01〜10%の水素を含
むアルガスガスなどのキヤリヤガスが循環される
閉ガス流路1を示している。各方向切換弁2,
3,4は、本実施例では4方向弁から成つてお
り、試料の酸素量分析時には図に示すように閉ガ
ス流路1内のキヤリヤガスを矢印Aの方向に流
す。 In FIG. 1, the path indicated by the thick line indicates a closed gas flow path 1 through which a carrier gas such as argas gas containing 0.01 to 10% hydrogen is circulated during oxygen content analysis of a sample. Each direction switching valve 2,
3 and 4 are four-way valves in this embodiment, which cause the carrier gas in the closed gas flow path 1 to flow in the direction of arrow A as shown in the figure when analyzing the oxygen content of a sample.
閉ガス流路1には、測定時のキヤリヤガスの循
環方向Aに沿つて、キヤリヤガスを循環させる循
環ポンプ5、金属、合金、またはそれらの化合
物、あるいはセレン、テルル等の半金属から成る
試料6を閉ガス流路1内に導入する試料導入手段
7、試料導入手段7からの試料6を溶解させ、試
料中の酸素を放出させる試料溶解炉8、試料6か
ら放出されキヤリヤ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、たとえばジルコ
ニアにイツトリア、マグネシア、カルシアなどの
安定化剤を固溶させてなる固体電解質を用いた電
気化学的酸素ポンプ9、が直列に介在されてい
る。 The closed gas flow path 1 includes a circulation pump 5 for circulating carrier gas along the carrier gas circulation direction A during measurement, and a sample 6 made of a metal, an alloy, a compound thereof, or a semimetal such as selenium or tellurium. A sample introduction means 7 is introduced into the closed gas flow path 1, a sample melting furnace 8 is used to melt the sample 6 from the sample introduction means 7 and release oxygen in the sample, and a sample melting furnace 8 is used to dissolve the sample 6 from the sample introduction means 7 and release oxygen from the sample 6, which is carried by the carrier gas. An electrochemical oxygen pump 9 using a solid electrolyte made of, for example, zirconia in which a stabilizer such as yttria, magnesia, or calcia is dissolved, is interposed in series to discharge the oxygen to the outside of the closed gas flow path 1. There is.
循環ポンプ5の上流側には、循環ポンプ5によ
つて循環されるキヤリヤガスの流量(流速)を測
定可能な流量計10が設けられている。また、酸
素ポンプ9と循環ポンプ5との間には、キヤリヤ
ガスを閉ガス流路1内に導入するキヤリヤガス導
入口11が接続されており、フイルタ12、方向
切換弁2を介してキヤリヤガスが導入されるよう
になつている。 A flow meter 10 that can measure the flow rate (flow velocity) of the carrier gas circulated by the circulation pump 5 is provided upstream of the circulation pump 5 . Further, a carrier gas inlet 11 for introducing carrier gas into the closed gas flow path 1 is connected between the oxygen pump 9 and the circulation pump 5, and the carrier gas is introduced through the filter 12 and the directional control valve 2. It is becoming more and more like this.
なお、この閉ガス流路1をキヤリヤガスで置換
する際には、方向切換弁2,3,4は矢印Bのよ
うに切換えられるが、その経路の終端部には減圧
吸引口13が接続されており、キヤリヤガス供給
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14、吸引ポンプ15を介して系外
に排出される。 Note that when replacing this closed gas flow path 1 with carrier gas, the directional control valves 2, 3, and 4 are switched as shown by arrow B, but the reduced pressure suction port 13 is connected to the end of the path. The gas in the closed gas flow path 1 that has been expelled by the carrier gas supply is discharged to the outside of the system via the filter 14 and the suction pump 15.
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16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 16 on which the sample 6 is placed and allows the sample 6 to fall downward by rotation or the like.
試料導入手段7の下部に、試料溶解炉8が設け
られている。試料溶解炉8には、試料導入手段7
からの試料6を試料溶解部17に導くとともに、
試料溶解部17で溶解された試料6からの放出ガ
スを酸素ポンプ9側へと導く試料溶解管18と、
試料溶解部17を加熱する加熱装置19が設けら
れている。 A sample melting furnace 8 is provided below the sample introduction means 7. The sample melting furnace 8 includes a sample introducing means 7.
While guiding the sample 6 from the sample to the sample dissolving section 17,
a sample dissolving tube 18 that guides the released gas from the sample 6 dissolved in the sample dissolving section 17 to the oxygen pump 9 side;
A heating device 19 for heating the sample melting section 17 is provided.
試料溶解管18は、内管20と外管21との二
重管構造に構成されており、内管20の内部通路
22が試料溶解部17への試料導入路として、内
管20と外管21との間の通路23が酸素ポンプ
側通路24に通じる放出ガス排出路として構成さ
れている。内管20および外管21は、アルミ
ナ、石英等の耐熱管から構成されており、上端の
試料導入手段7の枠体との接続部は、Oリング2
5,26によつてそれぞれシールされている。 The sample dissolving tube 18 has a double tube structure including an inner tube 20 and an outer tube 21, and an internal passage 22 of the inner tube 20 serves as a sample introduction path to the sample dissolving section 17. A passage 23 between the oxygen pump 21 and the oxygen pump side passage 21 is configured as a discharge gas exhaust passage communicating with the oxygen pump side passage 24. The inner tube 20 and the outer tube 21 are made of heat-resistant tubes made of alumina, quartz, etc., and the connection part with the frame of the sample introduction means 7 at the upper end is connected with the O-ring 2.
5 and 26, respectively.
外管21の下端部は、封止管構造になつてお
り、この部分が試料溶解部17に構成されてい
る。試料溶解部17には、本実施例では、外管2
1とは別体の耐熱材料から成るつぼ27が挿入さ
れており、るつぼ27内で試料6が溶解されるよ
うになつている。 The lower end of the outer tube 21 has a sealed tube structure, and this portion constitutes the sample dissolving section 17. In this embodiment, the sample dissolving section 17 includes an outer tube 2.
A crucible 27 made of a heat-resistant material separate from crucible 1 is inserted, and the sample 6 is melted within the crucible 27.
試料溶解管18の上部には、加熱装置19側か
ら試料導入手段7側への伝熱を抑制するととも
に、試料溶解部17からの試料の蒸気等を凝縮さ
せて下流側への流出を抑制する冷却手段28が設
けられている。冷却手段28は、本実施例では冷
却フアンから構成されているが、他の任意の手
段、たとえば水冷ジヤケツト、他の冷媒を用いた
ジヤケツト等からなる手段であつてもよい。 The upper part of the sample melting tube 18 is provided with a structure that suppresses heat transfer from the heating device 19 side to the sample introducing means 7 side, and condenses sample vapor etc. from the sample melting section 17 to suppress its outflow to the downstream side. Cooling means 28 are provided. Although the cooling means 28 is constituted by a cooling fan in this embodiment, it may be any other means such as a water cooling jacket, a jacket using another refrigerant, or the like.
上記のように構成された実施例装置の作用につ
いて説明する。 The operation of the embodiment device configured as described above will be explained.
まず、酸素ポンプ9を運転してキヤリヤガス中
の酸素を排出し、閉ガス流路1内を十分に低い一
定の酸素分圧に保つておく。 First, the oxygen pump 9 is operated to exhaust oxygen in the carrier gas, and the inside of the closed gas flow path 1 is maintained at a sufficiently low constant oxygen partial pressure.
試料6は、試料受け16から落下され、内管2
0内の試料導入路22を通して試料溶解部17、
つまりるつぼ27内に導かれる。るつぼ27は、
加熱装置19によつて、所定の温度に加熱されて
おり、試料6が溶解される。溶解された試料6か
らは、酸素が放出され、放出酸素はキヤリヤガス
の流れにのつて、内管20と外管21との間の放
出ガス排出路23へと導かれ、通路24を介して
閉ガス流路1内を酸素ポンプ9へと運ばれ、その
酸素ポンプ9によつて閉ガス流路1外に排出され
る。この排出に要した酸素ポンプ9の電気量か
ら、試料6中の酸素量を知る。 The sample 6 is dropped from the sample receiver 16 and placed in the inner tube 2.
0 through the sample introduction path 22, the sample dissolving section 17,
In other words, it is guided into the crucible 27. Crucible 27 is
The sample 6 is heated to a predetermined temperature by the heating device 19, and the sample 6 is melted. Oxygen is released from the dissolved sample 6, and the released oxygen is guided along the flow of the carrier gas to the released gas exhaust passage 23 between the inner tube 20 and the outer tube 21, and is closed via the passage 24. The gas is carried through the gas flow path 1 to the oxygen pump 9 and discharged to the outside of the closed gas flow path 1 by the oxygen pump 9. The amount of oxygen in the sample 6 is determined from the amount of electricity required by the oxygen pump 9 for this discharge.
試料溶解管18は、内管20と外管21との二
重管構造とされた外管底部が試料溶解部17に構
成されているので、従来のようにU字管構造をと
らなくても、閉ガス流路1のキヤリヤガス流れ方
向に沿つて試料6を試料溶解部17へ、試料溶解
部17で溶解された試料6からの放出ガスを酸素
ポンプ9側へと導くことができる。とくに、放出
ガス排出路23が試料導入路22まわりに構成さ
れることになり、従来U字管構造に比べ試料溶解
管18全体が大幅に小型化される。また、内管2
0、外管21は単なる円管構造であるから、構造
も簡素化され、とくに、試料溶解部17である外
管底部外面構造が簡素になる。小型化により、試
料溶解部17の熱容量は試料6の溶解に必要な最
小限のものでよく、加熱装置19の容量も小型化
される。また、外管21底部の外面構造が簡素で
あることにより、加熱装置19からの加熱効率が
高められるとともに、加熱装置19自体の構造が
簡素化される。 The sample dissolving tube 18 has a double tube structure consisting of an inner tube 20 and an outer tube 21, and the bottom of the outer tube is configured as the sample dissolving section 17, so there is no need for a conventional U-shaped tube structure. The sample 6 can be guided to the sample dissolving section 17 along the carrier gas flow direction of the closed gas flow path 1, and the gas released from the sample 6 dissolved in the sample dissolving section 17 can be guided to the oxygen pump 9 side. In particular, the released gas exhaust path 23 is constructed around the sample introduction path 22, and the entire sample dissolution tube 18 is significantly reduced in size compared to the conventional U-shaped tube structure. In addition, inner pipe 2
0. Since the outer tube 21 has a simple circular tube structure, the structure is simplified, and in particular, the outer surface structure of the bottom portion of the outer tube, which is the sample dissolving section 17, is simplified. Due to the miniaturization, the heat capacity of the sample melting section 17 may be the minimum required for melting the sample 6, and the capacity of the heating device 19 is also miniaturized. Moreover, since the outer surface structure of the bottom of the outer tube 21 is simple, the heating efficiency from the heating device 19 is increased, and the structure of the heating device 19 itself is simplified.
また、溶解された試料6からの放出ガスは、キ
ヤリヤガスとともに内管20と外管21との間の
環状の通路である放出ガス排出路23から酸素ポ
ンプ9側へと導かれる。環状通路であるから従来
のような管中央部の流れはなく、ガスの流れ全量
が外管21の内周面近傍を流れる。外管21の上
部は冷却手段28によつて冷却されるので、この
部分で内部を流れるガスは効率よく冷却され、試
料6からの蒸気等が効率よく凝縮されて試料溶解
部17側に戻される。効率のよい冷却が行われる
ため、とくに管径の増大等による冷却表面積増大
の必要がなくなり、試料溶解管18は小形化され
ながら同時に冷却効率も高められる。 Further, the released gas from the dissolved sample 6 is guided to the oxygen pump 9 side from the released gas exhaust path 23, which is an annular passage between the inner tube 20 and the outer tube 21, together with the carrier gas. Since it is an annular passage, there is no flow in the center of the tube as in the conventional case, and the entire amount of gas flows near the inner circumferential surface of the outer tube 21. Since the upper part of the outer tube 21 is cooled by the cooling means 28, the gas flowing inside is efficiently cooled in this part, and the steam etc. from the sample 6 is efficiently condensed and returned to the sample melting section 17 side. . Since efficient cooling is performed, there is no need to increase the cooling surface area by increasing the tube diameter, and the sample dissolution tube 18 can be downsized while simultaneously improving cooling efficiency.
[発明の効果]
以上説明したように、本発明の酸素分析装置に
よるときは、試料溶解管を二重管構造にして、外
管底部で効率よく試料を溶解させ、内管と外管と
の間の環状通路にて効率よくガスの流れを冷却で
きるようにしたので、試料溶解管およびそのまわ
りに設けられる加熱装置、冷却手段等の構造の簡
素化と小型化を達成することができ、試料溶解部
にあつては構造の簡素化による伝熱効率の向上お
よび小型化によるエネルギ効率の向上、冷却部に
あつては小型装置のままで環状通路構造による冷
却効率の向上、をはかることができるという効果
が得られる。[Effects of the Invention] As explained above, when using the oxygen analyzer of the present invention, the sample dissolution tube has a double tube structure, the sample is efficiently dissolved at the bottom of the outer tube, and the inner tube and outer tube are separated. By making it possible to efficiently cool the gas flow in the annular passage between the tubes, it is possible to simplify and downsize the structure of the sample dissolution tube and the heating device, cooling means, etc. installed around it. In the melting section, it is possible to improve heat transfer efficiency by simplifying the structure and improve energy efficiency by making it smaller, and in the cooling section, it is possible to improve cooling efficiency by using an annular passage structure while maintaining a small device. Effects can be obtained.
第1図は本発明の一実施例に係る酸素分析装置
の全体構成図、第2図は第1図の装置の試料溶解
管まわりの拡大縦断面図、第3図は第2図の装置
の部分拡大縦断面図、第4図は従来から知られて
いる酸素分析装置の概略全体構成図、である。
1……閉ガス流路、2,3,4……方向切換
弁、5……循環ポンプ、6……試料、7……試料
導入手段、8……試料溶解炉、9……酸素ポン
プ、16……試料受け、17……試料溶解部、1
8……試料溶解管、19……加熱装置、20……
内管、21…外管、22……試料導入路、23…
…放出ガス排出路、27……るつぼ、28……冷
却手段。
FIG. 1 is an overall configuration diagram of an oxygen analyzer according to an embodiment of the present invention, FIG. 2 is an enlarged longitudinal cross-sectional view of the sample dissolution tube and surroundings of the device shown in FIG. FIG. 4 is a partially enlarged longitudinal cross-sectional view, and is a schematic overall configuration diagram of a conventionally known oxygen analyzer. 1... Closed gas flow path, 2, 3, 4... Directional switching valve, 5... Circulation pump, 6... Sample, 7... Sample introduction means, 8... Sample melting furnace, 9... Oxygen pump, 16... Sample receiver, 17... Sample dissolving section, 1
8... Sample dissolution tube, 19... Heating device, 20...
Inner tube, 21... Outer tube, 22... Sample introduction path, 23...
...released gas exhaust path, 27...crucible, 28...cooling means.
Claims (1)
閉ガス流路内に試料を導入する試料導入手段と、
該試料導入手段から導入された試料を溶解させる
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、互に直列に配置した酸素分析
装置において、前記試料溶解炉には試料溶解管を
立設し、該試料溶解管を、前記試料導入手段から
の試料を前記試料溶解管の底部に設けた試料溶解
部に導く内管と、前記試料溶解部で溶解された試
料からのガスを前記内管との間を通して前記酸素
ポンプ側へと導く外管との二重管構造にしたこと
を特徴とする酸素分析装置。1. Sample introduction means for introducing a sample into a closed gas flow path in which a carrier gas is circulated;
A sample melting furnace that melts the sample introduced from the sample introduction means and 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 are connected to each other. In the oxygen analyzer arranged in series, a sample melting tube is installed upright in the sample melting furnace, and the sample melting tube is transferred from the sample introduction means to a sample melting section provided at the bottom of the sample melting tube. An oxygen analyzer characterized in that it has a double-tube structure including an inner tube that guides the gas from the sample dissolved in the sample dissolving section and an outer tube that guides gas from the sample dissolved in the sample dissolving section to the oxygen pump side through the space between the inner tube and the oxygen pump. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60211115A JPS6271840A (en) | 1985-09-26 | 1985-09-26 | Oxygen analyzer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60211115A JPS6271840A (en) | 1985-09-26 | 1985-09-26 | Oxygen analyzer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6271840A JPS6271840A (en) | 1987-04-02 |
| JPH0450979B2 true JPH0450979B2 (en) | 1992-08-17 |
Family
ID=16600650
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60211115A Granted JPS6271840A (en) | 1985-09-26 | 1985-09-26 | Oxygen analyzer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6271840A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2593927Y2 (en) * | 1991-08-09 | 1999-04-19 | 東進物産 株式会社 | Control device with automatic open prohibition circuit for in-vehicle automatic doors |
| KR100484855B1 (en) * | 2003-02-04 | 2005-04-22 | 동부아남반도체 주식회사 | An analyzer of an ion implanting apparatus |
-
1985
- 1985-09-26 JP JP60211115A patent/JPS6271840A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6271840A (en) | 1987-04-02 |
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