JPS6020649B2 - Required air amount control device for gaseous fuel - Google Patents
Required air amount control device for gaseous fuelInfo
- Publication number
- JPS6020649B2 JPS6020649B2 JP3880376A JP3880376A JPS6020649B2 JP S6020649 B2 JPS6020649 B2 JP S6020649B2 JP 3880376 A JP3880376 A JP 3880376A JP 3880376 A JP3880376 A JP 3880376A JP S6020649 B2 JPS6020649 B2 JP S6020649B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- combustion
- oxygen concentration
- gaseous fuel
- amount
- 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
Links
- 239000000446 fuel Substances 0.000 title claims description 49
- 239000007789 gas Substances 0.000 claims description 63
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 48
- 239000001301 oxygen Substances 0.000 claims description 48
- 229910052760 oxygen Inorganic materials 0.000 claims description 48
- 238000002485 combustion reaction Methods 0.000 claims description 43
- 239000007784 solid electrolyte Substances 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 4
- 238000005259 measurement Methods 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims 1
- 239000000203 mixture Substances 0.000 description 11
- 238000004458 analytical method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- 238000005070 sampling Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Landscapes
- Regulation And Control Of Combustion (AREA)
Description
【発明の詳細な説明】
本発明は固体電解質よりなる酸素検出器を用いた気体燃
料の必要空気量を連続的に制御測定する気体燃料の必要
空気量制御装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for controlling the amount of air required for gaseous fuel, which continuously controls and measures the amount of air required for gaseous fuel using an oxygen detector made of a solid electrolyte.
一般に、流体燃料を空気と混合し燃焼させて熱エネルギ
ーを利用する各種の燃焼装置においては、燃料を有効的
に利用するために、燃焼に先立って燃料と空気の流量と
を一定の比率に設定したのち燃焼するいわゆる空燃比制
御機構とを利用した燃焼装置と、燃焼排ガス中の酸素濃
度を測定し、この信号をフィードバックして空燃比を制
御する機構を利用した燃焼装置とが広く知られている。In general, in various combustion devices that use thermal energy by mixing fluid fuel with air and combusting it, the flow rates of fuel and air are set at a certain ratio prior to combustion in order to use the fuel effectively. Combustion devices that use a so-called air-fuel ratio control mechanism that then combusts, and combustion devices that use a mechanism that measures the oxygen concentration in the combustion exhaust gas and controls the air-fuel ratio by feeding back this signal are widely known. There is.
しかしながら前者は燃料の組成が変動する場合は、空燃
比に誤差を生じ、空気過剰になったり、反対に燃料過剰
になったりして、適正燃焼を行うことが非常にむずかし
い欠点がある。また後者はガスサンプリングの応答遅れ
が大きく、しかも組成の変化する燃料については、やは
り、前者と同じような欠点があった。これを解決するた
めに、従来気体燃料の組成たとえばCH4,C4日,o
,&,C○,等の気体燃料中の量をそれぞれ個別にガス
クロマトグラフィ一により分析し、この結果より前記気
体燃料が分析された組成により適正燃焼するために必要
な空気量を算出し、燃焼装置に供給する空気量を調整し
て適正燃焼を行う燃焼装置も知られている。しかしガス
クロマトグラフィ−での分析時間は約1時間程度と長く
かかるためこれをオンラインにフィードバックすること
は燃料組成が比較的安定している場合にしか適用できず
、組成が常に変化する気体燃料の適正燃焼については従
来ほとんど無対策のままであり、燃料消費および排ガス
対策上からも多くの問題点を含んでいた。本発明の気体
燃料の必要空気量制御装置は従来のこれらの欠点および
問題点を解決した組成の安定した気体燃料のみならず、
組成が常に変化する気体燃料の必要空気量をも迅速かつ
連続的に制御測定でき‐る装置である。However, the former has the disadvantage that if the composition of the fuel varies, an error occurs in the air-fuel ratio, resulting in excess air or, conversely, excess fuel, making it extremely difficult to perform proper combustion. In addition, the latter has the same drawbacks as the former, such as a large response delay in gas sampling and fuels whose composition changes. In order to solve this problem, conventional gaseous fuel compositions such as CH4, C4, o
, &, C○, etc. in the gaseous fuel are individually analyzed by gas chromatography, and from the results, the amount of air required for proper combustion of the gaseous fuel according to the analyzed composition is calculated, and the combustion Combustion devices that perform proper combustion by adjusting the amount of air supplied to the device are also known. However, since analysis time using gas chromatography takes a long time, approximately 1 hour, feeding this back online is only applicable when the fuel composition is relatively stable, and the analysis time is only suitable for gaseous fuels whose composition changes constantly. Until now, almost no measures have been taken regarding combustion, and there have been many problems in terms of fuel consumption and exhaust gas countermeasures. The required air amount control device for gaseous fuel of the present invention not only solves these conventional drawbacks and problems, but also produces gaseous fuel with a stable composition.
This device can quickly and continuously control and measure the amount of air required for gaseous fuel whose composition is constantly changing.
本発明は、−定流料の気体燃料と空気とを混合するガス
混合器と、該ガス混合器から排出される混合ガスを定流
量にする混合ガス定流量器と、該混合ガス定流量器にて
定流量にされた混合ガスを高温燃焼帯において燃焼する
とともに燃焼排ガス中の残酸素濃度を検出する固体電解
質からなる酸素検出器と「該酸素検出器よりの酸素濃度
に対応する起電力E,とあらかじめ設定された基準酸素
濃度に対応する基準電圧E2との差に比例した電気信号
を出す酸素濃度設定器と、該酸素濃度設定器から出され
た電気信号によって燃焼用空気を前記一定流量の空気に
制御するよう空気導入経路中に挿入された空気流量制御
器と該空気流量制御器により制御された一定流量の空気
量を測定する空気流量計とから少なくともなり、燃焼排
ガス中の残酸素濃度をあらかじめ設定した基準酸素濃度
に一致させるよう燃焼に必要な空気量を測定制御し、燃
焼装置で気体燃料を燃焼する前に気体燃料の必要空気量
を測定し、その測定結果より燃焼菱慣用空気流量制御器
を制御することを特徴とする気体燃料の必要空気量制御
装置にある。The present invention provides: - a gas mixer that mixes a constant flow rate of gaseous fuel and air; a mixed gas constant flow device that makes the mixed gas discharged from the gas mixer a constant flow rate; and the mixed gas constant flow device. An oxygen detector consisting of a solid electrolyte that detects the residual oxygen concentration in the combustion exhaust gas while burning the mixed gas at a constant flow rate in a high-temperature combustion zone, and an electromotive force E corresponding to the oxygen concentration from the oxygen detector. , and a reference voltage E2 corresponding to a preset reference oxygen concentration. It consists of at least an air flow controller inserted into the air introduction path to control the amount of air remaining in the combustion exhaust gas, and an air flow meter that measures the constant flow rate of air controlled by the air flow controller. The amount of air required for combustion is measured and controlled so that the concentration matches the standard oxygen concentration set in advance, and the amount of air required for gaseous fuel is measured before the gaseous fuel is combusted in the combustion device. A device for controlling the amount of air required for gaseous fuel is characterized by controlling an air flow rate controller.
以下、その構成を一実施例を示す図面にもとずし・て説
明する。The configuration will be explained below with reference to the drawings showing one embodiment.
第1図において気体燃料28は試料ガス入口1から入り
、試料ガス採取ポンプ2によって吸引され一定圧以上に
昇氏されて後、試料ガス定流量器3を通ることによって
一定流量一定圧となってガス混合器7に導入される。一
方、加圧空気271ま空気入口4から入り、空気流量制
御器5で流量制御されて後、空気流量計6を通ってガス
混合器れこ導入される。そして、一定量の気体燃料と空
気はガス混合器7で充分混合されたのち「 2分岐され
、一方は混合ガス定流量器8によって一定流量とされた
のち高温燃焼帯を有する円筒状固体電解質からなる酸素
検出器9中で完全燃焼されるとともに、燃焼排ガス中の
残酸素濃度に対応する起電力E,を検出し「その燃焼排
ガスはガス排出OSIを通して排出される。他方の混合
ガスは、混合ガス分流調整器10を介して、適当な燃焼
炉で燃焼して後、排出口亀1より排出する。混合ガス定
流量器8は、たとえ流量が変っても酸素検出器9がガス
流量の変動による影響を受けなくするためのものである
。そして、酸素検出器9は、第2図に示す通り「ジルコ
ェア等によりなる一体の円筒状固体電解質14を同一の
電気炉16中に挿入して「混合ガス入口16側に白金お
よび多孔質磁器よりなる触媒床17を設けた900〜1
500ooの高温帯亀8と、それに続く、燃焼排ガス中
の残酸素濃度に対応する起電力E,を電極19,2川こ
よって求める600〜900ご0の低温帯28とはそれ
ぞれ電熱線22,23で所定の温度に加熱保持されてい
る。従って混合ガス定流量器8よりの一定流量の混合ガ
スは、混合ガス入口16より酸素検出器9中に導入され
て、まず高温帯18の触媒床17で完全に燃焼され、つ
いで燃焼試料ガスは、低温帯281こおいて、円筒状固
体電解質の外側に標準ガス導入口24より導入された標
準ガスとの間において「イオン伝導によって、燃焼ガス
中の残酸素濃度に対応する起電力E,が電極19,20
1と発生し、該起電力E,‘まリード線25,26によ
って、酸素濃度設定器12に伝達される。この場合、円
筒状、固体電解質における酸素濃度と起電力の関係は0
1式で示される。E,=聖。g溝〔mV〕 …o’
ここで、E,:起電力「R:気体常数、T:絶対温度、
F:フアデ−定数、cPo2:カソード側電極の酸素濃
度〜aPo2:ア/ード側電極の酸素分圧。In FIG. 1, the gaseous fuel 28 enters from the sample gas inlet 1, is sucked in by the sample gas sampling pump 2 and raised to a constant pressure or higher, and then passes through the sample gas constant flow meter 3 to maintain a constant flow rate and constant pressure. The gas is introduced into the gas mixer 7. On the other hand, pressurized air 271 enters from the air inlet 4, is controlled in flow rate by the air flow controller 5, and is then introduced into the gas mixer through the air flow meter 6. After a certain amount of gaseous fuel and air are thoroughly mixed in a gas mixer 7, they are branched into two branches, one of which is made into a constant flow rate by a mixed gas constant flow device 8, and then separated from a cylindrical solid electrolyte having a high-temperature combustion zone. At the same time, the combustion exhaust gas is completely combusted in the oxygen detector 9, and an electromotive force E corresponding to the residual oxygen concentration in the combustion exhaust gas is detected. After being burned in a suitable combustion furnace via a gas flow divider regulator 10, it is discharged from an outlet port 1.The mixed gas constant flow meter 8 is configured so that even if the flow rate changes, the oxygen detector 9 detects fluctuations in the gas flow rate. As shown in FIG. 900-1 with a catalyst bed 17 made of platinum and porous porcelain on the mixed gas inlet 16 side
The high temperature zone 8 of 500 mm and the low temperature zone 28 of 600 to 900 mm, in which the electromotive force E corresponding to the residual oxygen concentration in the combustion exhaust gas is obtained using the electrodes 19 and 2, are the heating wires 22 and 28, respectively. It is heated and maintained at a predetermined temperature at 23. Therefore, a constant flow rate of the mixed gas from the mixed gas constant flow meter 8 is introduced into the oxygen detector 9 through the mixed gas inlet 16, and is first completely combusted in the catalyst bed 17 of the high temperature zone 18, and then the combusted sample gas is In the low temperature zone 281, an electromotive force E corresponding to the residual oxygen concentration in the combustion gas is generated between the standard gas introduced from the standard gas inlet 24 to the outside of the cylindrical solid electrolyte due to ion conduction. Electrodes 19, 20
1 is generated, and the electromotive force E,' is transmitted to the oxygen concentration setting device 12 by the lead wires 25 and 26. In this case, the relationship between oxygen concentration and electromotive force in the cylindrical solid electrolyte is 0.
It is shown in equation 1. E,=St. g groove [mV] …o'
Here, E,: electromotive force, R: gas constant, T: absolute temperature,
F: Fade constant, cPo2: oxygen concentration at the cathode side electrode ~ aPo2: oxygen partial pressure at the front side electrode.
今、ここでaPo2を一定にした場合、E,よりcPo
2が求められる。したがって、混合ガス中の酸素濃度お
よび可燃性分の酸素換算濃度を各々mPo2および×と
すると可燃性分は、高温帯で燃焼されるので、酸素検出
器9の起電力はE,:帯。Now, if we keep aPo2 constant here, E, then cPo
2 is required. Therefore, if the oxygen concentration in the mixed gas and the oxygen equivalent concentration of the combustible component are mPo2 and x, respectively, the combustible component is burned in the high temperature zone, so the electromotive force of the oxygen detector 9 is E, : zone.
g宅をX〔mV〕 .・…岬となる。G home to X [mV].・It becomes a cape.
ここで、E,は燃焼排ガス中の酸素濃度に対応する起電
力であり、基準酸素濃度に対応する基準電圧虫2と比較
されるものが得られる。そしてリード線25,26によ
って排ガス中の酸素濃度に対応する起電力E,を受ける
酸素濃度設定器12は、予め決められたある一定の酸素
濃度すなわち基準酸素濃度に対応する基準電圧E2を内
蔵しており、このE2とE,とを比較し、その差に比例
した電気信号を出すもので、該電気信号は、信号変換器
13に伝達され、ここで空気流量制御器5を駆動するの
に必要な適当な別の信号に変換し、空気流量制御器5を
制御し、同時にその空気流量は空気流量計6で測定指示
される。たとえば、ある気体燃料のその燃焼排ガス中の
残酸素濃度が1%になるような必要空気量を求める場合
は、まず、酸素濃度設定器12の基準酸素濃度に対応す
る基準電圧瓦2を、1%に対応する電圧に設定する。そ
して、組成が変化して気体燃料の可燃性分が多い場合は
当然ながら燃焼排ガス中の残酸素濃度が減少するので、
空気流量を自動的に増し、反対に気体燃料の可燃性分が
少ないときは、空気量を自動的に減らし、燃焼排ガス中
の残酸素濃度を、常に基準酸素濃度に一致させるよう燃
焼に必要な空気量が自動的に制御測定される。従って、
気体燃料の組成が変化、すなわち必要空気量が変った場
合でも、燃焼排ガス中の酸素濃度が前記基準酸素濃度に
一致するように、自動的に空気流量が制御および測定さ
れ、その気体燃料に見合った必要空気量を迅速かつ連続
的に制御測定するものである。そして測定された必要空
気量の信号により燃焼装置32のバーナ31に供給され
る燃焼用空気29の流量制御を行う燃焼装置用空気制御
器30を制御することにより安定したバーナの燃焼が確
保できるものである。Here, E is an electromotive force corresponding to the oxygen concentration in the combustion exhaust gas, and a reference voltage 2 corresponding to the reference oxygen concentration is obtained. The oxygen concentration setting device 12, which receives an electromotive force E corresponding to the oxygen concentration in the exhaust gas through the lead wires 25 and 26, has a built-in reference voltage E2 corresponding to a certain predetermined oxygen concentration, that is, a reference oxygen concentration. E2 and E are compared, and an electrical signal proportional to the difference is generated.The electrical signal is transmitted to the signal converter 13, where it is used to drive the air flow controller 5. The signal is converted into another appropriate signal to control the air flow rate controller 5, and at the same time, the air flow rate is measured and indicated by the air flow meter 6. For example, if you want to find the required amount of air so that the residual oxygen concentration in the combustion exhaust gas of a certain gaseous fuel is 1%, first, set the reference voltage tile 2 corresponding to the reference oxygen concentration of the oxygen concentration setting device 12 to 1%. Set the voltage corresponding to %. If the composition changes and the combustible content of the gaseous fuel increases, the residual oxygen concentration in the combustion exhaust gas will naturally decrease.
The air flow rate is automatically increased, and when the combustible content of the gaseous fuel is low, the air flow rate is automatically reduced to keep the residual oxygen concentration in the combustion exhaust gas consistent with the standard oxygen concentration. The air volume is automatically controlled and measured. Therefore,
Even if the composition of the gaseous fuel changes, that is, the required amount of air changes, the air flow rate is automatically controlled and measured so that the oxygen concentration in the combustion exhaust gas matches the reference oxygen concentration, and the amount of air is adjusted to match the gaseous fuel. This system quickly and continuously controls and measures the amount of air required. Then, stable combustion in the burner can be ensured by controlling the combustion device air controller 30 that controls the flow rate of the combustion air 29 supplied to the burner 31 of the combustion device 32 based on the measured required air amount signal. It is.
次に、本発明の制御装置を使用した具体例について述べ
る。Next, a specific example using the control device of the present invention will be described.
可燃性分としてCは,日2およびCOを含んだ各種の試
料ガスをそれぞれ用意し、上記の可燃性分を各々ガスク
ロマトグラフィ−により分析してその分析結果より計算
した必要空気量を(理論空気量/燃料量)理論空燃比に
換算した値と、本発明の装置を用いて測定した測定値と
の比較結果は第3図に示す通りで、両者の値がほとんど
一致しているものである。また、理論空燃比が3.4の
試料ガスを用いて本発明装置により、長時間の連続測定
をした結果は第4図の遮りで経時変化はほとんど認めら
れず安定したものであることも確認された。For the combustible component, C, prepare various sample gases containing CO and CO, analyze each of the above combustible components by gas chromatography, and calculate the required air amount from the analysis results (theoretical air amount). The comparison result between the value converted to the stoichiometric air-fuel ratio (amount/fuel amount) and the measured value measured using the device of the present invention is as shown in Figure 3, and the two values almost match. . In addition, it was confirmed that the results of long-term continuous measurements using a sample gas with a stoichiometric air-fuel ratio of 3.4 using the device of the present invention were stable with almost no change over time observed due to the blockage in Figure 4. It was done.
さらに、理論空燃比が1.5と8.0の2種類の試料ガ
スを本装置に交互に流し指示の応答時間を調べた結果は
第5図に示す通りで、指示変化があった時点からフルス
ケールの90%までの値に達する時間は約19秒程度で
あり本発明の装置は極めて早い応答性を有するものであ
ることも確認された。以上のべた通り、本発明の気体燃
料の必要空気量制御装置は、組成の変化の著しい気体燃
料についても迅速に空気量を制御測定できるものであり
、製鉄、電力、石油化学工場の気体燃料を使用する各種
の燃焼装置あるいはボイラーの燃料パイプ等に設置する
ことによって、気体燃料の最も適切な空気量を極めて迅
速に設定できるもので、熱効率の改善および燃費の節減
、さらに排出ガス対策の改善にも寄与できるものであり
、産業上極めて有用な装置である。Furthermore, two types of sample gases with stoichiometric air-fuel ratios of 1.5 and 8.0 were alternately flowed through this device, and the response time of the command was investigated. The results are shown in Figure 5, and the response time from the time when the command changed It was also confirmed that the time required to reach a value of 90% of full scale was about 19 seconds, and that the device of the present invention had extremely fast response. As described above, the device for controlling the amount of air required for gaseous fuel of the present invention can quickly control and measure the amount of air even for gaseous fuel whose composition changes significantly, and is suitable for controlling gaseous fuel in steel manufacturing, electric power, and petrochemical plants. By installing it in the fuel pipes of various combustion devices or boilers to be used, it is possible to extremely quickly set the most appropriate amount of air for gaseous fuel, improving thermal efficiency, reducing fuel consumption, and improving exhaust gas countermeasures. This is an extremely useful device industrially.
第1図は本発明の気体燃料の必要空気量制御装置の模式
的説明図、第2図は本発明の制御装置中の酸素検出器の
断面を示す説明図、第3図ないし第5図は本発明装置を
使用した具体例による測定結果の説明図である。
‐1・・・・・・試料ガス入口、2・・・・・・試料ガ
ス採取ポンプ、3…・・・試料ガス定流量器、4・・・
・・・空気入口、5空気流量制御器、6・・…・空気流
量計、7・…・・ガス混合器、8混合ガス定流量器、9
・・・・・・酸素検出器、10…・・・混合ガス分流調
整器、11・・・…ガス排出口、12・・・・・・基準
酸素濃度設定器ト13・・・・・・信号変換器、14…
・・・固体電解質円筒、15・…・・電気炉、16…・
・・混合ガス入口、17……触媒床、18・・…・高温
帯、19,20・・…・電極、21・・・・・・低温帯
、22,23・・・・・・電熱線、24・・・・・・標
準ガス導入口、25,26・・・・・・リード線、27
・・・・・・加圧空気、28・・・・・・気体燃料、2
9・…・・燃焼用空気、30…・・・燃焼装置用空気制
御器、31……バーナ〜 32…・・・燃焼装置。
第1図
第2図
第4図
第3図
第5図FIG. 1 is a schematic explanatory diagram of the required air amount control device for gaseous fuel of the present invention, FIG. 2 is an explanatory diagram showing a cross section of an oxygen detector in the control device of the present invention, and FIGS. 3 to 5 are FIG. 3 is an explanatory diagram of measurement results according to a specific example using the device of the present invention. -1...Sample gas inlet, 2...Sample gas sampling pump, 3...Sample gas constant flow meter, 4...
... Air inlet, 5 Air flow rate controller, 6... Air flow meter, 7... Gas mixer, 8 Mixed gas constant flow meter, 9
...Oxygen detector, 10...Mixed gas separation regulator, 11...Gas outlet, 12...Reference oxygen concentration setting device 13... Signal converter, 14...
・・・Solid electrolyte cylinder, 15...Electric furnace, 16...
...Mixed gas inlet, 17...Catalyst bed, 18...High temperature zone, 19,20...Electrode, 21...Low temperature zone, 22,23...Heating wire , 24... Standard gas inlet, 25, 26... Lead wire, 27
..... Pressurized air, 28 ..... Gaseous fuel, 2
9... Combustion air, 30... Combustion device air controller, 31... Burner ~ 32... Combustion device. Figure 1 Figure 2 Figure 4 Figure 3 Figure 5
Claims (1)
と、該ガス混合器から排出される混合ガスを定流量にす
る混合ガス定流量器と、該混合ガス定流量器にて定流量
にされた混合ガスを高温燃焼帯において燃焼するととも
に燃焼排ガス中の残酸濃度を検出する固体電解質からな
る酸素検出器と、該酸素検出器よりの酸素濃度に対応す
る起電力E_1とあらかじめ設定された基準酸素濃度に
対応する基準電圧E_2との差に比例した電気信号を出
す酸素濃度設定器と該酸素濃度設定器から出された電気
信号によつて燃焼用空気を前記一定流量の空気に制御す
るよう空気導入経路中に挿入された空気流量制御器と、
該空気流量制御器により制御された一定流量の空気量を
測定する空気流量計とから少なくともなり、燃焼排ガス
中の残酸素濃度をあらかじめ設定した基準酸素濃度に一
致させるよう燃焼に必要な空気量を測定制御し、燃焼装
置で気体燃料を燃焼する前に気体燃料の必要空気量を測
定し、その測定結果より燃焼装置用空気流量制御器を制
御することを特徴とする気体燃料の必要空気量制御装置
。 2 前記酸素検出器は、固体電解質円筒と、この固体電
解質円筒を包囲して入口側に高温帯を、また出口側に低
温帯を設けた電気炉と、前記電気炉の高温帯にある固体
電解質円筒内に設けられた触媒床と、前記低温帯にある
固体電解質円筒の内外に設けられた電極とより成り、定
量された混合ガスを高温燃焼帯において燃焼するととも
に、燃焼排ガス中の残酸素濃度を前記低温帯の内外に設
けた電極により検出するよう構成した特許請求の範囲第
1項記載の気体燃料の必要空気量制御装置。[Claims] 1. A gas mixer that mixes a constant flow rate of gaseous fuel and air, a mixed gas constant flow device that makes a constant flow rate of the mixed gas discharged from the gas mixer, and a constant flow rate of the mixed gas. An oxygen detector consisting of a solid electrolyte that burns a constant flow of mixed gas in a high-temperature combustion zone and detects the concentration of residual acid in the combustion exhaust gas, and an electromotive force corresponding to the oxygen concentration from the oxygen detector. Combustion air is controlled to the above-mentioned constant level by an oxygen concentration setting device that outputs an electric signal proportional to the difference between E_1 and a reference voltage E_2 corresponding to a preset reference oxygen concentration, and an electric signal output from the oxygen concentration setting device. an air flow controller inserted into the air introduction path to control the flow rate of the air;
It consists of at least an air flow meter that measures the amount of air at a constant flow rate controlled by the air flow controller, and measures the amount of air necessary for combustion so that the residual oxygen concentration in the combustion exhaust gas matches a preset reference oxygen concentration. Control of the required air amount of gaseous fuel, characterized in that the amount of air required for the gaseous fuel is measured and controlled before the gaseous fuel is combusted in the combustion device, and an air flow rate controller for the combustion device is controlled based on the measurement result. Device. 2. The oxygen detector includes a solid electrolyte cylinder, an electric furnace surrounding the solid electrolyte cylinder and having a high temperature zone on the inlet side and a low temperature zone on the outlet side, and a solid electrolyte in the high temperature zone of the electric furnace. It consists of a catalyst bed installed in a cylinder and electrodes installed inside and outside the solid electrolyte cylinder located in the low-temperature zone, and burns a fixed amount of mixed gas in the high-temperature combustion zone, and reduces the residual oxygen concentration in the combustion exhaust gas. 2. The required air amount control device for gaseous fuel according to claim 1, which is configured to detect the amount of air by means of electrodes provided inside and outside the low temperature zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3880376A JPS6020649B2 (en) | 1976-04-08 | 1976-04-08 | Required air amount control device for gaseous fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3880376A JPS6020649B2 (en) | 1976-04-08 | 1976-04-08 | Required air amount control device for gaseous fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52122937A JPS52122937A (en) | 1977-10-15 |
| JPS6020649B2 true JPS6020649B2 (en) | 1985-05-23 |
Family
ID=12535442
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3880376A Expired JPS6020649B2 (en) | 1976-04-08 | 1976-04-08 | Required air amount control device for gaseous fuel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6020649B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05257524A (en) * | 1992-03-10 | 1993-10-08 | Toyota Autom Loom Works Ltd | Remote controller |
-
1976
- 1976-04-08 JP JP3880376A patent/JPS6020649B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05257524A (en) * | 1992-03-10 | 1993-10-08 | Toyota Autom Loom Works Ltd | Remote controller |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52122937A (en) | 1977-10-15 |
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