JPH06242060A - Hydrocarbon sensor - Google Patents

Hydrocarbon sensor

Info

Publication number
JPH06242060A
JPH06242060A JP50A JP3362293A JPH06242060A JP H06242060 A JPH06242060 A JP H06242060A JP 50 A JP50 A JP 50A JP 3362293 A JP3362293 A JP 3362293A JP H06242060 A JPH06242060 A JP H06242060A
Authority
JP
Japan
Prior art keywords
sensor
hydrocarbon
gas
concentration
hydrocarbon gas
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.)
Granted
Application number
JP50A
Other languages
Japanese (ja)
Other versions
JP3308624B2 (en
Inventor
Hironari Iwahara
弘育 岩原
Takashi Hibino
高士 日比野
Tamotsu Yajima
保 矢嶋
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.)
Nagoya University NUC
TYK Corp
Original Assignee
Nagoya University NUC
TYK Corp
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 Nagoya University NUC, TYK Corp filed Critical Nagoya University NUC
Priority to JP03362293A priority Critical patent/JP3308624B2/en
Publication of JPH06242060A publication Critical patent/JPH06242060A/en
Application granted granted Critical
Publication of JP3308624B2 publication Critical patent/JP3308624B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide a hydrocarbon sensor for detecting gas concentration without requiring any external power supply for measuring the resistance of sensor element regardless of the drift of sensor resistance by measuring the concentration of hydrocarbon gas through the use of electromotive force generated spontaneously from the sensor itself. CONSTITUTION:A pair of porous electrodes 2, 3 touch a proton conductive solid electrolyte 1 at a position where the solid electrolyte 1 is sandwiched. One of the pair of porous electrodes 2, 3 is composed of an electrode catalyst which is inactive to combustion of hydrocarbon gas to be measured whereas the other electrode is composed of an active electrode catalyst. The active electrode 2 of hydrocarbon sensor is employed as a catalyste and concentration of hydrocarbon is measured through the use of electromotive force induced in the sensor by the difference between the partial pressure of steam above the inactive electrode 3 and the partial pressure of steam produced at the time of combustion of hydrocarbon gas.

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、ガス中の炭化水素ガス
の濃度を測定する炭化水素センサに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrocarbon sensor for measuring the concentration of hydrocarbon gas in gas.

【0002】[0002]

【従来の技術】半導体型センサ及び接触燃焼式可燃性ガ
スセンサ等の炭化水素ガスセンサは、従来数多く報告さ
れており、実際に実用化されているものも多い。接触燃
焼式のセンサの場合は、可燃性ガスの燃焼によりセンサ
素子の温度が上昇し、この温度上昇に伴い、センサ素子
の抵抗が変化することを利用するものであり、センサの
外部回路から抵抗測定用の電流を流し、そのときの電圧
変化からセンサ素子の抵抗値を求めることにより、炭化
水素濃度を測定する方法である。半導体型センサの場合
には、例えばSnO2に種々の燃焼触媒を担持させた素
子を高温に保ち、そのセンサ素子を炭化水素ガスに曝し
たときに、炭化水素ガスが燃焼すると半導体素子表面に
吸着した酸素を消費することにより生じるセンサ素子の
抵抗変化を利用してガス濃度を測定する。これらのセン
サは、酸化錫を基体としたセンサ素子の表面に種々の燃
焼触媒を担持させ、その触媒の活性の差を利用すること
により、炭化水素ガスの燃焼時にセンサ素子の吸着酸素
量が変化することに伴うセンサ素子の抵抗変化からガス
濃度を検知するものである。
2. Description of the Related Art Many hydrocarbon gas sensors such as semiconductor type sensors and catalytic combustion type combustible gas sensors have been reported so far, and many of them have been put into practical use. In the case of a contact combustion type sensor, the temperature of the sensor element rises due to the combustion of combustible gas, and the resistance of the sensor element changes with this temperature rise. This is a method of measuring the hydrocarbon concentration by passing a current for measurement and obtaining the resistance value of the sensor element from the voltage change at that time. In the case of a semiconductor type sensor, for example, when an element supporting various combustion catalysts on SnO 2 is kept at a high temperature and the sensor element is exposed to a hydrocarbon gas, when the hydrocarbon gas burns, it is adsorbed on the semiconductor element surface. The gas concentration is measured by utilizing the resistance change of the sensor element caused by the consumption of the oxygen. In these sensors, various combustion catalysts are carried on the surface of the sensor element based on tin oxide, and the difference in the activity of the catalysts is used to change the amount of oxygen adsorbed by the sensor element during combustion of hydrocarbon gas. The gas concentration is detected from the change in resistance of the sensor element due to the change.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上述し
た従来技術では、センサ素子に電流を印加し、そのとき
の電圧値からセンサ素子の抵抗値を求めるため、抵抗測
定用の電源が必要となり、センサの回路が複雑になると
いう問題点がある。更に、センサ素子の抵抗値は、セン
サの製造方法でかなり差が出てくるため、完成したセン
サ素子は個別的にキャリブレーションをする必要があ
る。また、センサの抵抗値は、初期状態にドリフトを起
こすことを防ぐため、エージング処理する必要があると
いった問題点がある。
However, in the above-mentioned prior art, since a current is applied to the sensor element and the resistance value of the sensor element is obtained from the voltage value at that time, a power source for resistance measurement is required, and the sensor There is a problem that the circuit of becomes complicated. Further, the resistance value of the sensor element varies considerably depending on the method of manufacturing the sensor, and thus the completed sensor element needs to be individually calibrated. Further, there is a problem that the resistance value of the sensor needs to be aged in order to prevent drift in the initial state.

【0004】本発明はかかる問題点に鑑みてなされたも
のであって、センサ自体が自発的に出す起電力を利用し
て炭化水素ガス濃度を測定するようにして従来のような
センサ素子抵抗を測定するための外部電源を必要とせ
ず、センサ抵抗の時間的変化に影響を受けずにガス濃度
を検出することができる炭化水素センサ及び炭化水素濃
度の測定方法を提供することを目的とする。
The present invention has been made in view of the above problems, and the resistance of the sensor element as in the prior art is measured by measuring the hydrocarbon gas concentration by utilizing the electromotive force spontaneously generated by the sensor itself. An object of the present invention is to provide a hydrocarbon sensor and a method for measuring a hydrocarbon concentration, which can detect a gas concentration without requiring an external power source for measurement and being affected by a temporal change in sensor resistance.

【0005】[0005]

【課題を解決するための手段】本発明に係る炭化水素セ
ンサは、プロトン導電性固体電解質と、この固体電解質
を挟む位置で前記固体電解質に接触する一対の多孔質電
極とを有し、前記多孔質電極のうち、一方が測定する炭
化水素ガスの燃焼に不活性な電極触媒からなり、他方が
活性な電極触媒からなることを特徴とする。
A hydrocarbon sensor according to the present invention has a proton conductive solid electrolyte and a pair of porous electrodes which are in contact with the solid electrolyte at positions sandwiching the solid electrolyte. One of the quality electrodes is composed of an electrocatalyst which is inactive in combustion of the hydrocarbon gas to be measured, and the other is composed of an active electrode catalyst.

【0006】[0006]

【作用】本願発明者等は、センサ自体が発生する起電力
を利用し、センサ抵抗の変化によらず炭化水素ガス濃度
を検出できるセンサを開発すべく、種々の実験研究を繰
り返した。その結果、プロトン導電性固体電解質を用い
ると共に、炭化水素ガスの燃焼に対する活性が異なる導
電性触媒を前記電解質に対する電極材として用いること
により、炭化水素ガスが固体電解質上で燃焼する際に両
電極上で生じる水蒸気分圧の差により発生する起電力を
利用して炭化水素ガス濃度を測定できることを見いだし
た。
The inventors of the present application repeated various experimental studies in order to develop a sensor that can detect the hydrocarbon gas concentration regardless of the change in the sensor resistance by utilizing the electromotive force generated by the sensor itself. As a result, by using a proton conductive solid electrolyte and by using a conductive catalyst having different activities for combustion of hydrocarbon gas as an electrode material for the electrolyte, when the hydrocarbon gas burns on the solid electrolyte, It was found that the hydrocarbon gas concentration can be measured by using the electromotive force generated by the difference in the partial pressure of water vapor generated in.

【0007】つまり、固体電解質の両面に接触させた導
電性触媒の活性が異なるため、活性触媒側では完全燃焼
が起こり、不活性触媒側では不完全燃焼が起こる。この
ため、両電極上で発生する水蒸気量が相互に異なるため
水蒸気分圧差が生じ、この水蒸気分圧差により両電極間
に起電力が発生する。この起電力が炭化水素ガスの濃度
に比例するため炭化水素ガス濃度を求めることができ
る。
That is, since the activities of the conductive catalysts contacting both surfaces of the solid electrolyte are different, complete combustion occurs on the active catalyst side and incomplete combustion occurs on the inert catalyst side. For this reason, since the amounts of water vapor generated on both electrodes are different from each other, a water vapor partial pressure difference occurs, and an electromotive force is generated between both electrodes due to this water vapor partial pressure difference. Since this electromotive force is proportional to the concentration of the hydrocarbon gas, the hydrocarbon gas concentration can be obtained.

【0008】[0008]

【実施例】次に、本発明の実施例について添付の図面を
参照して説明する。図1は本発明の実施例に係るセンサ
プローブを示す断面図である。ディスク状のペロブスカ
イト型プロトン導電性固体電解質1の一方の平面に活性
電極2が焼き付けにより形成され、他方の平面に不活性
電極3が同様に焼き付けにより形成されている。これら
のプロトン導電性固体電解質1は例えばCaZr0.9
0.13-αからなり、活性電極2はLa0.6Ba0.4
oO3からなり、不活性電極3はAgからなる。活性電
極2及び不活性電極3には、夫々例えばPt線からなる
リード線4が取り付けられている。
Embodiments of the present invention will now be described with reference to the accompanying drawings. FIG. 1 is a sectional view showing a sensor probe according to an embodiment of the present invention. An active electrode 2 is formed by baking on one plane of a disk-shaped perovskite-type proton conductive solid electrolyte 1, and an inactive electrode 3 is also formed by baking on the other plane. These proton-conductive solid electrolytes 1 are, for example, CaZr 0.9 I
n 0.1 O 3 -α and the active electrode 2 is La 0.6 Ba 0.4 C.
It consists oO 3, inert electrode 3 is made of Ag. A lead wire 4 made of, for example, a Pt wire is attached to each of the active electrode 2 and the inactive electrode 3.

【0009】このように構成されたセンサプローブにお
いては、固体電解質1の両面に接触させた導電性触媒電
極2,3の炭化水素ガスに対する活性が異なるため、活
性触媒電極2側では炭化水素ガスの完全燃焼が起こり、
不活性触媒電極3側では不完全燃焼が起こる。このた
め、両電極上で発生する水蒸気量が相互に異なるため、
両電極上で水蒸気分圧差が生じ、この水蒸気分圧差によ
り両電極間に起電力が発生する。この起電力が炭化水素
ガスの濃度に比例し又は両者に相関関係があるため、予
め起電力と炭化水素ガス濃度との間の関係を求めておけ
ば、この関係を校正データとして、測定された起電力に
基づいて炭化水素ガス濃度を求めることができる。
In the sensor probe constructed as described above, since the conductive catalyst electrodes 2 and 3 contacting both surfaces of the solid electrolyte 1 have different activities with respect to the hydrocarbon gas, the active catalyst electrode 2 side is not affected by the hydrocarbon gas. Complete combustion occurs,
Incomplete combustion occurs on the inert catalyst electrode 3 side. Therefore, the amount of water vapor generated on both electrodes is different from each other,
A difference in water vapor partial pressure occurs on both electrodes, and an electromotive force is generated between both electrodes due to the difference in water vapor partial pressure. Since this electromotive force is proportional to the concentration of the hydrocarbon gas or has a correlation with both of them, if the relation between the electromotive force and the hydrocarbon gas concentration is obtained in advance, this relation is measured as the calibration data. The hydrocarbon gas concentration can be calculated based on the electromotive force.

【0010】次に、本実施例の炭化水素センサの特性試
験をした結果について説明する。図1に示す構造の炭化
水素センサを製造した。先ず、その製造方法について説
明する。ペロブスカイト型のプロトン導電性固体電解質
1であるCaZr0.9In0.13-α(直径が7.8mm、厚
さが7.9mm)のディスク状試料の片面にLa0.6Ba0.4
CoO3の粉末ペーストを塗布し、空気中で1000℃に1
時間熱処理することによりこれを焼き付け、炭化水素ガ
スに対して活性な触媒としての活性電極2を形成した。
その後、Agペーストを他方の面に塗布し、これを750
℃に1時間、空気中で熱処理して焼き付け、炭化水素ガ
スに対して不活性な不活性電極3を形成した。このよう
にして製造したセンサ素子の電極2,3にリード線4と
してPt線を取付けた。その後、リード線4に図5に示
す電圧計5を接続し、常温におけるセンサの起電力を測
定した。
Next, the result of the characteristic test of the hydrocarbon sensor of this embodiment will be described. A hydrocarbon sensor having the structure shown in FIG. 1 was manufactured. First, the manufacturing method will be described. La 0.6 Ba 0.4 was formed on one side of a disk-shaped sample of CaZr 0.9 In 0.1 O 3 -α (diameter: 7.8 mm, thickness: 7.9 mm), which is a perovskite-type proton conductive solid electrolyte 1.
CoO 3 powder paste is applied and 1000 ℃ in air 1
This was heat-treated for a period of time to be baked to form an active electrode 2 as a catalyst which is active with respect to hydrocarbon gas.
After that, apply Ag paste on the other side and apply 750
It was heat-treated in air at 1 ° C. for 1 hour and baked to form an inert electrode 3 which was inert to hydrocarbon gas. A Pt wire was attached as a lead wire 4 to the electrodes 2 and 3 of the sensor element thus manufactured. Then, the voltmeter 5 shown in FIG. 5 was connected to the lead wire 4 and the electromotive force of the sensor at room temperature was measured.

【0011】次いで、このセンサ素子を770℃の電気炉
6内にセットした。この電気炉6にはアルミナ管7が挿
入されており、センサ素子をアルミナ管7内に挿入し、
電気炉6の中心に配置した。そして、ボンベ9からの炭
化水素ガス(測定ガス)を混合器8によりボンベ10か
らの空気と所定の比で混合した後、配管11を介してア
ルミナ管7内に導入し、アルミナ管7内のセンサ素子に
供給した。ボンベ9からの測定ガスは流量260ml/minで
電気炉内に導入した。そして、出口ガスの組成をガスク
ロマトグラフ(図示せず)により検量した。
Next, this sensor element was set in the electric furnace 6 at 770 ° C. An alumina tube 7 is inserted in the electric furnace 6, and the sensor element is inserted in the alumina tube 7.
It was placed in the center of the electric furnace 6. Then, after mixing the hydrocarbon gas (measurement gas) from the cylinder 9 with the air from the cylinder 10 by the mixer 8 at a predetermined ratio, it is introduced into the alumina pipe 7 through the pipe 11 and inside the alumina pipe 7. It was supplied to the sensor element. The measurement gas from the cylinder 9 was introduced into the electric furnace at a flow rate of 260 ml / min. Then, the composition of the outlet gas was calibrated by a gas chromatograph (not shown).

【0012】図3はボンベ9からの測定ガスがメタンガ
スの場合、図4はプロパンガスの場合のセンサ起電力の
測定例を示す。各図において、横軸は時間、縦軸はセン
サ起電力を示している。本実施例に係るセンサプローブ
は、炭化水素ガスの濃度変化に対して安定な起電力を示
し、再現性も良好であった。また、応答に要した時間は
2分以内で実験装置のガスの置換を考慮にいれると応答
速度はかなり迅速なものであった。
FIG. 3 shows an example of measurement of the sensor electromotive force when the measurement gas from the cylinder 9 is methane gas, and FIG. 4 shows an example of measurement of the sensor electromotive force when propane gas is used. In each figure, the horizontal axis represents time and the vertical axis represents sensor electromotive force. The sensor probe according to this example exhibited stable electromotive force with respect to changes in the concentration of hydrocarbon gas, and had good reproducibility. Also, the time required to respond is
The response speed was quite rapid when the gas replacement of the experimental equipment was taken into account within 2 minutes.

【0013】図5は横軸に炭化水素ガス(プロパン及び
メタンガス)濃度、縦軸にセンサ起電力をとって、セン
サ起電力と炭化水素ガス濃度との関係を示したものであ
る。プロパンガス及びメタンガスの濃度測定では、ガス
濃度とセンサ起電力との間には良好な一対一の対応が見
られた。
FIG. 5 shows the relationship between the sensor electromotive force and the hydrocarbon gas concentration, with the horizontal axis representing the hydrocarbon gas (propane and methane gas) concentration and the vertical axis representing the sensor electromotive force. In the concentration measurement of propane gas and methane gas, a good one-to-one correspondence was found between the gas concentration and the sensor electromotive force.

【0014】なお、センサ素子に設ける電極触媒として
は、測定する炭化水素ガスの燃焼に対する触媒活性が異
なる2種類の導電性触媒を組み合わせることによってそ
の感度を変化させることもできる。また、測定すべきガ
スの種類は触媒の種類を適切なものに設定することによ
り選択することができる。
As the electrode catalyst provided in the sensor element, the sensitivity can be changed by combining two kinds of conductive catalysts having different catalytic activities with respect to the combustion of the hydrocarbon gas to be measured. Further, the type of gas to be measured can be selected by setting the type of catalyst to an appropriate one.

【0015】[0015]

【発明の効果】以上説明したように、本発明によれば、
炭化水素ガスセンサのプローブとして、プロトン導電性
固体電解質をセンサ素子に用い、その片面に炭化水素ガ
スの燃焼に活性な電極触媒を配置し、もう片面に炭化水
素ガスの燃焼に対して不活性な電極触媒を配置すること
により、炭化水素ガスがセンサ電極上に到達して燃焼す
る際に両電極上に発生する水蒸気量の差によって生じる
起電力を利用して炭化水素濃度を測定するから、この炭
化水素濃度を連続して安定且つ簡便に測定することがで
きる。
As described above, according to the present invention,
As a probe for a hydrocarbon gas sensor, a proton conductive solid electrolyte is used for the sensor element, an electrode catalyst active for combustion of hydrocarbon gas is arranged on one side, and an electrode inert for combustion of hydrocarbon gas on the other side. By arranging the catalyst, the hydrocarbon concentration is measured by using the electromotive force generated by the difference in the amount of water vapor generated on both electrodes when the hydrocarbon gas reaches the sensor electrode and burns. The hydrogen concentration can be measured continuously and stably and easily.

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

【図1】本発明の実施例に係るセンサプローブの断面図
である。
FIG. 1 is a sectional view of a sensor probe according to an embodiment of the present invention.

【図2】本センサプローブによる測定方法を示す概略図
である。
FIG. 2 is a schematic diagram showing a measuring method using the present sensor probe.

【図3】メタンガス濃度を測定したときのセンサプロー
ブの起電力特性を示すグラフ図である。
FIG. 3 is a graph showing an electromotive force characteristic of a sensor probe when measuring a methane gas concentration.

【図4】プロパンガス濃度を測定したときのセンサプロ
ーブの起電力特性を示すグラフ図である。
FIG. 4 is a graph showing an electromotive force characteristic of a sensor probe when measuring a propane gas concentration.

【図5】同じくセンサ素子の炭化水素ガス濃度に対する
起電力特性を示すグラフ図である。
FIG. 5 is a graph showing the electromotive force characteristics of the sensor element with respect to the hydrocarbon gas concentration.

【符号の説明】[Explanation of symbols]

1;固体電解質 2;活性電極 3;不活性電極 4;白金線 5;電圧計 6;電気炉 7;アルミナ管 8;ガス混合器 9;炭化水素ガスボンベ 10;空気ボンベ 11;ガス導入管 1; Solid Electrolyte 2; Active Electrode 3; Inert Electrode 4; Platinum Wire 5; Voltmeter 6; Electric Furnace 7; Alumina Tube 8; Gas Mixer 9; Hydrocarbon Gas Cylinder 10; Air Cylinder 11; Gas Inlet Tube

フロントページの続き (72)発明者 矢嶋 保 岐阜県可児郡御嵩町御嵩2192−345Front Page Continuation (72) Inventor Ho Yashima Mitake 2192-345 Mitake Town, Kani District, Gifu Prefecture

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 プロトン導電性固体電解質と、この固体
電解質を挟む位置で前記固体電解質に接触する一対の多
孔質電極とを有し、前記多孔質電極のうち、一方が測定
する炭化水素ガスの燃焼に不活性な電極触媒からなり、
他方が活性な電極触媒からなることを特徴とする炭化水
素センサ。
1. A proton-conductive solid electrolyte, and a pair of porous electrodes that come into contact with the solid electrolyte at positions sandwiching the solid electrolyte, one of the porous electrodes being one of the hydrocarbon gas to be measured. Composed of a combustion-inert electrocatalyst,
A hydrocarbon sensor characterized in that the other is composed of an active electrode catalyst.
【請求項2】 前記活性電極触媒上で炭化水素ガスの燃
焼時に生じる水蒸気の分圧と前記不活性電極触媒上の水
蒸気分圧との差により生じるセンサ起電力を利用して炭
化水素濃度を測定することを特徴とする請求項1に記載
の炭化水素センサ。
2. The hydrocarbon concentration is measured using a sensor electromotive force generated by the difference between the partial pressure of water vapor generated when the hydrocarbon gas is burned on the active electrode catalyst and the partial pressure of water vapor on the inert electrode catalyst. The hydrocarbon sensor according to claim 1, wherein:
JP03362293A 1993-02-23 1993-02-23 Hydrocarbon sensor Expired - Fee Related JP3308624B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03362293A JP3308624B2 (en) 1993-02-23 1993-02-23 Hydrocarbon sensor

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0772042A3 (en) * 1995-11-02 1998-07-08 Matsushita Electric Industrial Co., Ltd. Hydrocarbon sensor
JPH10282054A (en) * 1997-04-03 1998-10-23 Nippon Soken Inc Hydrocarbon sensor
EP1041380A2 (en) * 1999-04-01 2000-10-04 Matsushita Electric Industrial Co., Ltd. Hydrocarbon sensor and method of producing the same
JP2002277430A (en) * 2001-03-21 2002-09-25 National Institute Of Advanced Industrial & Technology Gas sensor, method for measuring concentration of gas, hydrocarbon gas sensor and method for measuring concentration of hydrocarbon gas
JP2003083929A (en) * 2001-09-12 2003-03-19 National Institute Of Advanced Industrial & Technology Combustible gas sensor and combustible-gas-concentration measuring method
WO2009011368A1 (en) * 2007-07-19 2009-01-22 Gunze Limited Solid ion-conducting material, electrochemical device utilizing the solid ion-conducting material, and method for production of the electrochemical device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0772042A3 (en) * 1995-11-02 1998-07-08 Matsushita Electric Industrial Co., Ltd. Hydrocarbon sensor
US5935398A (en) * 1995-11-02 1999-08-10 Matsushita Electric Industrial Co., Ltd. Hydrocarbon sensor
JPH10282054A (en) * 1997-04-03 1998-10-23 Nippon Soken Inc Hydrocarbon sensor
EP1041380A2 (en) * 1999-04-01 2000-10-04 Matsushita Electric Industrial Co., Ltd. Hydrocarbon sensor and method of producing the same
JP2002277430A (en) * 2001-03-21 2002-09-25 National Institute Of Advanced Industrial & Technology Gas sensor, method for measuring concentration of gas, hydrocarbon gas sensor and method for measuring concentration of hydrocarbon gas
JP4730635B2 (en) * 2001-03-21 2011-07-20 独立行政法人産業技術総合研究所 Hydrocarbon gas sensor and hydrocarbon gas concentration measuring method
JP2003083929A (en) * 2001-09-12 2003-03-19 National Institute Of Advanced Industrial & Technology Combustible gas sensor and combustible-gas-concentration measuring method
JP4743375B2 (en) * 2001-09-12 2011-08-10 独立行政法人産業技術総合研究所 Flammable gas concentration measurement method
WO2009011368A1 (en) * 2007-07-19 2009-01-22 Gunze Limited Solid ion-conducting material, electrochemical device utilizing the solid ion-conducting material, and method for production of the electrochemical device

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