JP4457769B2 - Temperature control method for zirconia sensor - Google Patents

Temperature control method for zirconia sensor Download PDF

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JP4457769B2
JP4457769B2 JP2004177691A JP2004177691A JP4457769B2 JP 4457769 B2 JP4457769 B2 JP 4457769B2 JP 2004177691 A JP2004177691 A JP 2004177691A JP 2004177691 A JP2004177691 A JP 2004177691A JP 4457769 B2 JP4457769 B2 JP 4457769B2
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博史 北島
行裕 関
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Yokogawa Electric Corp
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Description

本発明は、ジルコニア式酸素濃度計に関し、電源投入時から測定開始までの時間短縮を図ったジルコニア式酸素濃度計に関するものである。   The present invention relates to a zirconia oxygen analyzer, and more particularly, to a zirconia oxygen analyzer that shortens the time from power-on to the start of measurement.

ジルコニア式酸素濃度計では酸素濃度を検出するセルの表面温度を例えば750℃に制御する必要がある。温度制御はPWM機能を使用して矩形波の電力供給信号を出力しているが、温度上昇が一定となるようにそのデューティー比を制御している。   In the zirconia oxygen concentration meter, it is necessary to control the surface temperature of the cell for detecting the oxygen concentration to, for example, 750 ° C. The temperature control uses a PWM function to output a rectangular wave power supply signal, but the duty ratio is controlled so that the temperature rise is constant.

図3は本発明が適用されるジルコニア式酸素濃度計の一例を示すもので、1は酸素濃度計本体、2はジルコニア式センサ、3はジルコニア式センサ2内に組み込まれたヒーターである。この酸素濃度計本体1とジルコニア式センサ2の間はセンサ起電力信号線4、温度信号線5および電力供給線6により結線されている。7はセンサ起電力信号に基づいて演算した酸素濃度を出力する酸素濃度出力信号線、8は接点入力である。 FIG. 3 shows an example of a zirconia type oxygen concentration meter to which the present invention is applied. Reference numeral 1 denotes an oximeter main body, 2 denotes a zirconia type sensor, and 3 denotes a heater incorporated in the zirconia type sensor 2. The oxygen concentration meter main body 1 and the zirconia sensor 2 are connected by a sensor electromotive force signal line 4, a temperature signal line 5 and a power supply line 6. 7 is an oxygen concentration output signal line for outputting the oxygen concentration calculated based on the sensor electromotive force signal, and 8 is a contact input.

図4は図3の電力供給線6からPWM機能を使用して供給される矩形波信号であり、例えば、デューティー比70%とソフトウェアで指定すれば、1サイクルの中の電源ON時間70%、電源OFF時間30%のヒーター出力を実現することができる。なお700℃以降750℃まではPID制御を使用している。   FIG. 4 is a rectangular wave signal supplied from the power supply line 6 of FIG. 3 using the PWM function. For example, if the duty ratio is specified as 70% by software, the power ON time in one cycle is 70%, A heater output with a power off time of 30% can be realized. PID control is used from 700 ° C. to 750 ° C.

図5はこのような一定のデューティ比により700℃まで一定制御を用いて制御した従来の暖機例を示している。 FIG. 5 shows a conventional warm-up example in which constant control is performed up to 700 ° C. with such a constant duty ratio.

なお、このような設定値が所定の勾配の区間と定置の区間とを持つ温度などのプログラム制御を行うのに適した装置で、通常のPID制御と、外乱応答を良くするPIDパラメータおよび設定値変更時のオーバシュートを抑制するPIDパラメータの両方をもって制御する2自由度PID制御とを時間的に切り替える機能を備えたPID制御に関するものがある(特許文献1参照)。   In addition, it is an apparatus suitable for performing program control such as a temperature in which such a set value has a predetermined gradient section and a fixed section, and is used for normal PID control and PID parameters and set values for improving disturbance response. There is a PID control having a function of temporally switching between two-degree-of-freedom PID control controlled with both PID parameters for suppressing overshoot at the time of change (see Patent Document 1).

また、ヒーターを内包した加熱体を第1の設定温度を挟んで所定温度域を維持しながら加熱体との熱接触により未定着トナー像の画像定着を行う温度制御方式において、加熱体の温度Tを検出し、その検知温度Tが第1の設定温度以下で、予め設定された第2の温度の場合にその設定温度と検知温度との差分温度に基づいた設定曲線に従うように加熱温度を制御する第1の制御手段を選択し、検知温度が第2の温度を超えた場合に、第1の設定温度になるように加熱体の制御を行う第2の制御手段を選択するものがある(特許文献2参照)。 Further, the temperature control system for performing image fixing an unfixed toner image by thermal contact with the heating body while maintaining a predetermined temperature range the heating body containing therein a heater across the first set temperature, the temperature T of the heater When the detected temperature T is equal to or lower than the first set temperature and the preset second temperature, the heating temperature is controlled so as to follow a set curve based on the difference temperature between the set temperature and the detected temperature The first control means is selected, and when the detected temperature exceeds the second temperature, the second control means is selected to control the heating body so as to become the first set temperature ( Patent Document 2).

特開平6−187005号公報Japanese Patent Laid-Open No. 6-187005 特公平8−328423号公報Japanese Patent Publication No. 8-328423

ところで、従来のジルコニア式酸素濃度計においては、700℃までは一定制御を使用していた。
一定制御とは、700℃までは一定のデューティー比でヒーター出力することであり、ソフトウェアとしては、現在温度の取得と一定デューティー比の指定だけでよいので温度制御に要するソフトウェアの負荷が少ないという点で優れている。しかし、温度の低い時には温度上昇が大きく、温度が高くなるにつれて温度上昇も緩やかになってくるため、環境によっては700℃まで温度上昇できない場合があることや計測可能状態(750℃)に到達するまでの時間が予想できないことが問題となっていた。
By the way, in the conventional zirconia oximeter, constant control was used up to 700 ° C.
The constant control means that the heater is output at a constant duty ratio up to 700 ° C, and the software only needs to acquire the current temperature and specify the constant duty ratio, so the software load required for temperature control is small. Is excellent. However, when the temperature is low, the temperature rises greatly, and as the temperature rises, the temperature rises gradually. Therefore, depending on the environment, the temperature may not rise to 700 ° C., and the measurable state (750 ° C.) is reached. It was a problem that the time until could not be predicted.

従って本発明が解決しようとする課題は、温度上昇率を固定(例えば1℃/1秒)したフィードバック制御(以後、勾配制御)を実現することで、必ず700℃まで温度上昇させること、計測可能状態に到達するまでに時間も予測できるようにすること。また、温度制御に要するソフトウェアの負荷も少なく、PID制御よりも簡素なソフトウェアとすることを目的とする。   Therefore, the problem to be solved by the present invention is to realize a feedback control (hereinafter referred to as gradient control) with a fixed temperature increase rate (for example, 1 ° C./1 second), so that the temperature can always be increased to 700 ° C. and can be measured. Be able to predict the time to reach the state. It is another object of the present invention to provide software that is simpler than PID control and requires less software load for temperature control.

このような課題を解決するために、本発明のうち請求項1の発明は、
安定ジルコニアの固体電解質セラミックによって隔壁を作り、この隔壁の両側にガス透過性の多孔質白金電極を構成し、隔壁の両側に酸素分圧の異なるガスを導入して酸素濃度を検出するヒーターを有するジルコニア式センサの温度制御方法において、
ジルコニアセンサの現在温度を取得する工程と、
取得した現在温度と設定温度を比較する工程と、
取得した現在温度が設定温度未満であれば設定温度になるまで予め定めた温度上昇率に加熱開始時からの経過時間を乗じて算出した温度と実際に測定した温度との差、及び同様に演算した前回測定した温度との温度差の変化量に応じてヒーターの加熱制御量を変更し、一定の温度上昇率に固定するフィードバック制御による温度上昇率勾配制御処理を行う工程と、
取得した現在温度が設定温度に達していたらPIDによる制御を行う工程、
を含むことを特徴とするジルコニア式センサの温度制御方法。
In order to solve such a problem, the invention of claim 1 among the present invention,
A partition is made of a solid electrolyte ceramic of stable zirconia, a gas permeable porous platinum electrode is formed on both sides of the partition, and a heater for detecting oxygen concentration is introduced on both sides of the partition by introducing gases having different oxygen partial pressures. In the temperature control method of the zirconia sensor ,
Current and obtaining a temperature of the zirconia sensor,
A step of comparing the acquired current temperature with the set temperature;
If the acquired current temperature is lower than the set temperature, the difference between the temperature calculated by multiplying the predetermined rate of temperature increase by the elapsed time from the start of heating and the actually measured temperature until the set temperature is reached, and the same calculation Changing the heating control amount of the heater according to the amount of change in the temperature difference from the previously measured temperature, and performing a temperature increase rate gradient control process by feedback control that fixes to a constant temperature increase rate ; and
A process of performing control by PID if the acquired current temperature has reached the set temperature;
A temperature control method for a zirconia sensor .

請求項2においては、請求項1記載のジルコニア式センサの温度制御方法において、
前記設定温度になるまでは、一定周期で下記の式により今回の温度上昇率勾配制御量を求めることを特徴とする。

今回の温度上昇率勾配制御量=前回の温度上昇率勾配制御量+
K1×(s×t−T(t))+K2×Δ(s×t−T(t))
t:加熱開始からの経過時間
s:一定時間あたりの温度上昇率
T(t):実際に測定した温度(加熱開始からの経過時間によって変化する)
Δ(s×t−T(t)):s×t−T(t)についての今回と前回との差分
K1,K2;機器の個体差を補正する係数
In claim 2, in the temperature control method of the zirconia sensor according to claim 1,
Until the set temperature is reached, the current temperature rise rate gradient control amount is obtained by the following equation at a constant cycle.
This temperature increase rate gradient control amount = previous temperature increase rate gradient control amount +
K1 × (s × t−T (t)) + K2 × Δ (s × t−T (t))
t: Elapsed time from the start of heating s: Rate of temperature increase per fixed time T (t): Actually measured temperature (varies depending on the elapsed time from the start of heating)
Δ (s × t−T (t)): difference between the current time and the previous time regarding s × t−T (t) K1, K2; coefficients for correcting individual differences between devices

本発明によれば次のような効果がある。請求項1及び2に記載のジルコニア式センサの温度制御方法によれば、
設定温度になるまでは一定時間あたりの温度上昇率により温度勾配を制御するとともに、一定時間あたりの温度上昇率に加熱開始時からの経過時間を乗じて算出した温度と実際に測定した温度との差、及び同様に演算した前回の温度差の変化量に応じて加熱制御量を変更するようにしたので、必ず設定温度(ここでは700℃)まで温度上昇させることができるようになり、計測可能状態に到達するまでに時間も予測することができるようになる。
また、ソフトウェアの面から見ても、PID制御よりも簡素なソフトウェアとなるため、温度制御に要するソフトウェアの負荷が少ない優れたものとなる。
The present invention has the following effects. According to the temperature control method of the zirconia sensor according to claim 1 and 2,
Until the set temperature is reached, the temperature gradient is controlled by the rate of temperature rise per fixed time, and the temperature calculated by multiplying the temperature rise rate per fixed time by the elapsed time from the start of heating and the actually measured temperature Since the amount of heating control is changed according to the difference and the amount of change in the previous temperature difference calculated in the same way, the temperature can always be increased to the set temperature (700 ° C in this case) and measurement is possible. It will be possible to predict the time to reach the state.
Also, from the viewpoint of software, the software is simpler than PID control, so that the software load required for temperature control is excellent.

以下本発明を図面を用いて詳細に説明する。図1は本発明に係るジルコニア式酸素濃度計の温度制御の一例を示すフローチャートである。フローに従って説明する。
電源投入等により制御が開始されると(スタート)、ステップ1において温度信号線5を介して現在温度を取得する(図3参照)。
次にステップ2において、酸素濃度計本体1に設けられた演算手段(図示省略)により測定温度と設定温度(700℃)を比較する。
Hereinafter, the present invention will be described in detail with reference to the drawings. FIG. 1 is a flowchart showing an example of temperature control of a zirconia oximeter according to the present invention. This will be described according to the flow.
When control is started by turning on the power or the like (start), the current temperature is acquired via the temperature signal line 5 in step 1 (see FIG. 3).
Next, in step 2, the measured temperature and the set temperature (700 ° C.) are compared by a calculation means (not shown) provided in the oximeter main body 1.

比較した結果、700℃に達していればPIDによる制御を行い、700℃未満であれば勾配制御処理を実行する。即ち、設定温度と現在温度の差を演算しそれに固有の定数(1次係数)を乗じた数値を前回のヒーター制御量から加減する。 As a result of comparison, if the temperature reaches 700 ° C., control by PID is performed, and if the temperature is less than 700 ° C., gradient control processing is executed. That is, a numerical value obtained by calculating the difference between the set temperature and the current temperature and multiplying it by a specific constant (first-order coefficient) is added or subtracted from the previous heater control amount.

但し、これだけでは、温度値の応答遅れ(ヒーター制御量を変化させてから、変化した温度値読み込むまでの時間)があるため、オーバーシュートが発生してしまう。そこで、現在温度と設定温度の温度差の変化量(温度上昇率の差)を算出して、それに固有の定数(2次係数)を乗じた数値を加減する。実験では5秒ごとに現在値を取得した。これにより5秒毎の温度上昇を知ることができ、一定の温度上昇率(例えば1℃/1秒)を実現することができる。 However, this alone causes a response delay of the temperature value (the time from when the heater control amount is changed to when the changed temperature value is read), and thus overshoot occurs. Therefore, the amount of change in the temperature difference between the current temperature and the set temperature (temperature increase rate difference) is calculated, and a numerical value obtained by multiplying it by a specific constant (secondary coefficient) is added or subtracted. In the experiment, the current value was obtained every 5 seconds. As a result, the temperature increase every 5 seconds can be known, and a constant temperature increase rate (for example, 1 ° C./1 second) can be realized.

今回の勾配制御量=前回の勾配制御量+
K1×(s×t−T(t))+K2×Δ(s×t−T(t))
t:加熱開始からの経過時間
s:一定時間あたりの温度上昇率
T(t):実際に測定した温度(加熱開始からの経過時間によって変化する)
Δ(s×t−T(t)):s×t−T(t)についての今回と前回との差分
K1,K2;機器の個体差を補正する係数。
Current gradient control amount = previous gradient control amount +
K1 × (s × t−T (t)) + K2 × Δ (s × t−T (t))
t: Elapsed time from the start of heating s: Rate of temperature increase per fixed time T (t): Actually measured temperature (varies depending on the elapsed time from the start of heating)
Δ (s × t−T (t)): Difference between current time and previous time regarding s × t−T (t) K1, K2; coefficients for correcting individual differences of devices.

図2は常温Tの状態で暖機を開始し、所定の温度(700℃)までの勾配制御と700℃に達してからのPID制御に移行した状態を示す図である。
従って本発明によれば寒冷地においても確実に所定の温度まで上昇させることができ、計測可能になるまでの時間を予測することができる。
FIG. 2 is a diagram illustrating a state in which warm-up is started in a state of room temperature T, and gradient control up to a predetermined temperature (700 ° C.) and PID control after reaching 700 ° C. are performed.
Therefore, according to the present invention, the temperature can be surely increased to a predetermined temperature even in a cold region, and the time until measurement can be performed can be predicted.

なお、以上の説明は、本発明の説明および例示を目的として特定の好適な実施例を示したに過ぎない。例えば、設定温度は必ずしも700℃である必要はない。したがって本発明は、上記実施例に限定されることなく、その本質から逸脱しない範囲で更に多くの変更、変形を含むものである。   The above description merely shows a specific preferred embodiment for the purpose of explaining and illustrating the present invention. For example, the set temperature is not necessarily 700 ° C. Therefore, the present invention is not limited to the above-described embodiments, and includes many changes and modifications without departing from the essence thereof.

本発明のジルコニア式酸素濃度計の制御フローの一実施例を示す要部構成図である。It is a principal part block diagram which shows one Example of the control flow of the zirconia type oxygen concentration meter of this invention. 勾配制御とPID制御の実施例を説明する説明図である。It is explanatory drawing explaining the Example of gradient control and PID control. 本発明が実施されるジルコニア式酸素濃度計の一例を示す構成図である。It is a block diagram which shows an example of the zirconia type oxygen concentration meter by which this invention is implemented. デューティ比による制御例を示す説明図である。It is explanatory drawing which shows the example of control by a duty ratio. 従来のジルコニア式酸素濃度計の制御例を示す説明図である。It is explanatory drawing which shows the example of control of the conventional zirconia-type oxygen concentration meter.

符号の説明Explanation of symbols

1 酸素濃度計本体
2 ジルコニア式センサ
ヒーター
4 センサ起電力信号線
5 温度信号線
6 電力供給線
7 酸素濃度出力信号線
8 接点入力
1 Oxygen concentration meter body 2 Zirconia sensor 3 Heater 4 Sensor electromotive force signal line 5 Temperature signal line 6 Power supply line 7 Oxygen concentration output signal line 8 Contact input

Claims (2)

安定ジルコニアの固体電解質セラミックによって隔壁を作り、この隔壁の両側にガス透過性の多孔質白金電極を構成し、隔壁の両側に酸素分圧の異なるガスを導入して酸素濃度を検出するヒーターを有するジルコニア式センサの温度制御方法において、
1)ジルコニアセンサの現在温度を取得する工程と、
2)取得した現在温度と設定温度を比較する工程と、
3)取得した現在温度が設定温度未満であれば設定温度になるまで予め定めた温度上昇率 に加熱開始時からの経過時間を乗じて算出した温度と実際に測定した温度との差、及 び同様に演算した前回測定した温度との温度差の変化量に応じてヒーターの加熱制御 量を変更し、一定の温度上昇率に固定するフィードバック制御による温度上昇率勾配 制御処理を行う工程と、
4)取得した現在温度が設定温度に達していたらPIDによる制御を行う工程、
を含むことを特徴とするジルコニア式センサの温度制御方法。
A partition is made of a solid electrolyte ceramic of stable zirconia, a gas permeable porous platinum electrode is formed on both sides of the partition, and a heater for detecting oxygen concentration is introduced on both sides of the partition by introducing gases having different oxygen partial pressures. In the temperature control method of the zirconia sensor ,
1) a step of acquiring the current temperature of the zirconia sensor,
2) comparing the acquired current temperature with the set temperature;
3) If the acquired current temperature is less than the set temperature, the difference between the temperature calculated by multiplying the predetermined rate of temperature rise by the elapsed time from the start of heating and the actually measured temperature until the set temperature is reached, and Similarly, the process of changing the heating control amount of the heater according to the amount of change of the temperature difference from the previously measured temperature and performing the temperature increase rate gradient control process by feedback control that fixes to a constant temperature increase rate ;
4) A process of performing control by PID if the acquired current temperature has reached the set temperature,
A temperature control method for a zirconia sensor .
前記設定温度になるまでは、一定周期で下記の式により今回の温度上昇率勾配制御量を求めることを特徴とする請求項1記載のジルコニア式センサの温度制御方法。

今回の温度上昇率勾配制御量=前回の温度上昇率勾配制御量+
K1×(s×t−T(t))+K2×Δ(s×t−T(t))
t:加熱開始からの経過時間
s:一定時間あたりの温度上昇率
T(t):実際に測定した温度(加熱開始からの経過時間によって変化する)
Δ(s×t−T(t)):s×t−T(t)についての今回と前回との差分
K1,K2;機器の個体差を補正する係数
2. The temperature control method for a zirconia sensor according to claim 1, wherein the current temperature rise rate gradient control amount is obtained by the following formula at a constant period until the set temperature is reached .
This temperature increase rate gradient control amount = previous temperature increase rate gradient control amount +
K1 × (s × t−T (t)) + K2 × Δ (s × t−T (t))
t: Elapsed time from the start of heating s: Rate of temperature increase per fixed time T (t): Actually measured temperature (varies depending on the elapsed time from the start of heating)
Δ (s × t−T (t)): difference between the current time and the previous time regarding s × t−T (t) K1, K2; coefficients for correcting individual differences between devices
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