JPH0455738B2 - - Google Patents
Info
- Publication number
- JPH0455738B2 JPH0455738B2 JP6332587A JP6332587A JPH0455738B2 JP H0455738 B2 JPH0455738 B2 JP H0455738B2 JP 6332587 A JP6332587 A JP 6332587A JP 6332587 A JP6332587 A JP 6332587A JP H0455738 B2 JPH0455738 B2 JP H0455738B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- heater
- control
- cooling
- point
- 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
- 238000001816 cooling Methods 0.000 claims description 23
- 238000010438 heat treatment Methods 0.000 claims description 17
- 230000007423 decrease Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Devices For Use In Laboratory Experiments (AREA)
- Feedback Control In General (AREA)
- Control Of Temperature (AREA)
Description
【発明の詳細な説明】
(イ) 産業上の利用分野
本発明は一般に理化学機器における恒温装置の
温度制御装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention generally relates to a temperature control device for a constant temperature device in physical and chemical equipment.
(ロ) 従来の技術
従来の此種恒温装置の温度制御に関する方法は
例えば特開昭61−35856号公報に示されている。
此種恒温装置は庫内を例えば15℃〜30℃のうちの
何れかの目標値に精密に温度制御することが要求
され、そのために恒温装置内を加熱するためのヒ
ータと冷却するための圧縮機を有した冷却装置と
を備えている。(b) Prior Art A conventional method for controlling the temperature of this type of constant temperature device is disclosed in, for example, Japanese Patent Laid-Open No. 35856/1983.
This type of constant temperature device is required to precisely control the temperature inside the refrigerator to a target value of, for example, 15℃ to 30℃, which requires a heater to heat the inside of the constant temperature device and a compressor to cool it. It is equipped with a cooling device with a machine.
この場合目標値が恒温装置の周囲温度よりも高
い時はヒータの駆動は必要であるが冷却装置の駆
動は不要である。一方、周囲温度付近からそれ以
下で制御する場合はヒータと共に冷却装置による
冷却が必要とされ、又、目標値が高い場合であつ
ても、高温の試料等が収納された時はやはり冷却
が必要となる。ここで冷却装置の圧縮機はヒータ
と異なり、その機構上頻繁な駆動停止が行なえな
いため、此種精密な制御のためには圧縮機を駆動
したままでヒータの出力を制御するのが一般的で
あるが当然に電力消費が多大となるため目標値が
高い時は使用者が手動で圧縮機を停止せしめてい
た。 In this case, when the target value is higher than the ambient temperature of the constant temperature device, it is necessary to drive the heater, but it is not necessary to drive the cooling device. On the other hand, when controlling from around the ambient temperature to below it, cooling with a cooling device is required in addition to the heater.Also, even if the target value is high, cooling is still required when high temperature samples are stored. becomes. Unlike the heater, the compressor of the cooling system cannot be stopped frequently due to its mechanism, so for this type of precise control, it is common to control the heater output while the compressor is running. However, this naturally consumes a lot of power, so when the target value is high, the user has to manually stop the compressor.
この手間を省くため前記公報ではヒータと圧縮
機を交互に駆動し、この切換えは自動的に行うと
共に、ヒータは比例制御することによつて消費電
力を削減する方法を採つている。 In order to save this effort, the above-mentioned publication adopts a method in which the heater and the compressor are driven alternately, this switching is performed automatically, and the heater is proportionally controlled to reduce power consumption.
(ハ) 発明が解決しようとする問題点
前記公報ではヒータを比例制御していたが、更
に精密に制御するものとしてPI若しくはPID制御
することが考えられる。ここでPI制御とは比例
積分制御であり、PID制御とは更に微分制御が加
算される。以下にPID制御の一般式を示す。(C) Problems to be Solved by the Invention In the above-mentioned publication, the heater was proportionally controlled, but PI or PID control may be considered for more precise control. Here, PI control is proportional-integral control, and PID control further includes differential control. The general formula for PID control is shown below.
y=Kpe+Kp/Ti∫edt+KpTdde/dt ……(i)
ここでyはヒータの出力となる操作量、Kpは
比例感度、Tiは積分時間、Tdは微分時間、eは
目標値(以下(SV)とする。)と恒温装置内の温
度(以下(C)とする。)との偏差であり、式(i)中
Kpeは比例操作量を、Kp/Ti∫edtは積分操作量を、
KpTdde/dtは微分操作量を示している。 y=Kpe+Kp/Ti∫edt+KpTdde/dt...(i) Here, y is the manipulated variable that is the output of the heater, Kp is the proportional sensitivity, Ti is the integral time, Td is the differential time, and e is the target value (hereinafter referred to as (SV)) ) and the temperature in the thermostat (hereinafter referred to as (C)), and is
Kpe indicates the proportional manipulated variable, Kp/Ti∫edt indicates the integral manipulated variable, and KpTdde/dt indicates the differential manipulated variable.
比例操作量は偏差eの増加に比例し、それを減
少させる方向に作用し、積分操作量は偏差を積分
して定常的な偏差を無くする様作用し、微分操作
量は急激な温度変動を緩慢にする方向に作用する
ものである。 The proportional manipulated variable is proportional to the increase in the deviation e and acts to reduce it, the integral manipulated variable integrates the deviation and acts to eliminate steady deviations, and the differential manipulated variable acts to eliminate sudden temperature fluctuations. It acts in the direction of slowing down.
第5図に目標値(SV)を例えば+5℃としそ
の上下±0.5℃に上限値(DH)、下限値(DL)を
設定し、温度(C)が(DL)まで低下して圧縮
機を停止し、(DH)まで上昇して駆動すると共
に、圧縮機の停止中はヒータをPID制御にて発熱
させる場合の温度(C)の時間推移を示す。この
場合は圧縮機が駆動されて温度(C)が低下して
行き図中f点にて圧縮機が停止すると、その時点
で温度(C)は目標値(SV)より低いため比例
及び積分操作量はヒータの出力を増加させる方向
に、又、圧縮機が停止しても温度(C)はアンダ
ーシユートのため低下しているので微分操作量も
ヒータの出力を増加させる方向に出力を発生する
ので操作量y全体としては100%の状態となる。
そのため温度(C)は急上昇する。この時、式(i)
の積分項は図中f点からg点までの斜線範囲を出
力が増加する方向で積分し、g点からh点までの
斜線範囲を出力が減少する方向で積分している
が、アンダーシユートがあるため、f点からg点
までの積分がg点からh点までの積分を上回つて
おり、h点でヒータの出力が停止されても積分操
作量はヒータ出力を増加する方向で残存してしま
うため、これが蓄積されて行き、次回ヒータによ
る加熱が開始される際、再びヒータ出力は100%
となり、結果的に圧縮機とヒータを100%の出力
で交互に駆動するものと同じになつてしまい、温
度制御はアンダーシユート及びオーバシユートの
大きい不安定なものとなつてしまう。 In Figure 5, the target value (SV) is set to +5℃, and upper and lower limits (DH) and lower limits (DL) are set at ±0.5℃ above and below the target value (SV), and when the temperature (C) drops to (DL), the compressor is turned off. The figure shows the change in temperature (C) over time when the compressor is stopped, raised to (DH) and driven, and the heater is made to generate heat under PID control while the compressor is stopped. In this case, the compressor is driven and the temperature (C) decreases, and when the compressor stops at point f in the figure, the temperature (C) is lower than the target value (SV) at that point, so proportional and integral operations are performed. The amount will increase the output of the heater, and even if the compressor stops, the temperature (C) will decrease due to undershoot, so the differential operation amount will also increase the output of the heater. Therefore, the entire manipulated variable y is 100%.
Therefore, the temperature (C) rises rapidly. At this time, formula (i)
The integral term in the diagram integrates the shaded range from point f to point g in the direction in which the output increases, and integrates the shaded range from point g to point h in the direction in which the output decreases. Therefore, the integral from point f to point g exceeds the integral from point g to point h, and even if the heater output is stopped at point h, the integral operation amount remains in the direction of increasing the heater output. This accumulates and the next time the heater starts heating, the heater output will be 100% again.
As a result, the result is the same as driving the compressor and heater alternately at 100% output, and temperature control becomes unstable with large undershoots and overshoots.
本発明は斯かる問題点を解決するために成され
たものである。 The present invention has been made to solve these problems.
(ニ) 問題点を解決するための手段
本発明は恒温装置の温度制御装置において恒温
装置内を加熱する加熱手段と冷却する冷却手段と
をそれぞれ駆動することにより恒温装置内を目標
温度に保持するものであつて、目標温度を設定す
る手段と、恒温装置内の温度を検出する手段と、
目標温度と恒温装置内の温度に基づき加熱手段若
しくは冷却手段を交互に駆動すると共に加熱手段
をPI若しくはPID制御するための演算部を有した
制御手段とを備え、制御手段には冷却手段が停止
する時に演算部に所定の積分初期値を設定する手
段を設けたものである。(d) Means for Solving the Problems The present invention maintains the inside of the constant temperature device at a target temperature by respectively driving a heating means for heating the inside of the constant temperature device and a cooling means for cooling the inside of the constant temperature device in a temperature control device for a constant temperature device. a means for setting a target temperature, a means for detecting the temperature within the constant temperature device,
The control means has a calculation section for driving the heating means or the cooling means alternately based on the target temperature and the temperature in the constant temperature device and controlling the heating means by PI or PID, and the control means has a control means that stops the cooling means. The calculation unit is provided with means for setting a predetermined initial value of integration when performing the calculation.
(ホ) 作用
本発明によれば加熱手段と冷却手段を同時に駆
動しないので消費電力を削減できる。又、加熱手
段のPI若しくはPID制御によつて加熱手段による
安定した温度制御が可能となる。特に冷却手段の
停止後のヒータの制御が適節に行え温度変動の少
ない制御が可能となる。(E) Effect According to the present invention, power consumption can be reduced because the heating means and the cooling means are not driven simultaneously. Furthermore, stable temperature control by the heating means is possible by PI or PID control of the heating means. In particular, the heater can be controlled appropriately after the cooling means has stopped, and control with less temperature fluctuation is possible.
(ヘ) 実施例
次に図面に従つて本発明の実施例を説明する。
第1図は本発明の温度制御装置1の機能ブロツク
図を示す。2は制御手段としての周知のマイクロ
コンピユータであり、マイクロコンピユータ2は
その機能として切換え制御部3、PID演算部4、
積分初期値設定部5及びスイツチ6を有する。7
は図示しない恒温装置例えばインキユーベータの
庫内の目標温度SVを設定する温度設定部であり、
目標温度SVを切換え制御部3とPID演算部4に
出力する。8は該インキユベータの庫内温度Cを
検出する温度検出部であり、温度CをA/D変換
器9を介して切換え制御部3及びPID演算部4に
出力する。11は商用交流電源であり、その出力
には切換えスイツチ12が接続されている。13
は図示しない庫内冷却用の冷却装置の冷媒回路を
構成する圧縮機でスイツチ12のa接点に接続さ
れる。14は前記庫内を加熱する為のヒータであ
り、その発熱量はスイツチ12のb接点に接続さ
れてスイツチング素子から構成されるヒータ駆動
回路15によつて通電時間をデユーテイ比調節さ
れる。(F) Embodiments Next, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows a functional block diagram of a temperature control device 1 of the present invention. 2 is a well-known microcomputer as a control means, and the microcomputer 2 has a switching control section 3, a PID calculation section 4,
It has an integral initial value setting section 5 and a switch 6. 7
is a temperature setting unit that sets the target temperature SV inside a constant temperature device (not shown), such as an incubator;
The target temperature SV is output to the switching control section 3 and the PID calculation section 4. Reference numeral 8 denotes a temperature detection section that detects the internal temperature C of the incubator, and outputs the temperature C to the switching control section 3 and the PID calculation section 4 via the A/D converter 9. 11 is a commercial AC power source, and a changeover switch 12 is connected to its output. 13
is a compressor constituting a refrigerant circuit of a cooling device for cooling the inside of the refrigerator (not shown), and is connected to the a contact point of the switch 12. Reference numeral 14 denotes a heater for heating the interior of the refrigerator, and the amount of heat generated by the heater is controlled by the duty ratio of the energization time by a heater drive circuit 15 which is connected to the b contact of the switch 12 and is constituted by a switching element.
切換え制御部3は目標値SVの上下例えば±0.5
℃の点に上限温度DH及び下限温度DLを設定し、
温度CがDHより高い時はスイツチ12をa接点
に閉じ、その状態から低下してDLに達したらb
接点に閉じ、更にその状態から温度Cが上昇して
DHに達したらa接点に再び閉じる。又、スイツ
チ12をa接点に閉じている時はPID演算部4の
演算を休止せしめると共に、a接点からb接点に
切換える時にイツチ6を瞬時的に閉じて積分初期
値設定部5より所定の積分初期値I0をPID演算4
に入力せしめPID演算部4内に蓄積されている積
分操作量と入れ換える。PID演算部4はスイツチ
12がb接点に閉じている間、温度Cと目標値
SVとから前記式(i)に基づいてPID演算を行い、
その結果である操作量yをヒータ駆動回路15に
出力し、そのスイツチング素子を制御して操作量
yに基づいてヒータ14の発熱量を制御する。 The switching control unit 3 changes the target value SV up and down by ±0.5, for example.
Set the upper limit temperature DH and lower limit temperature DL at the point of °C,
When temperature C is higher than DH, switch 12 is closed to a contact, and when it decreases from that state and reaches DL, b
The contact closes, and the temperature C rises further from that state.
When DH is reached, the a contact is closed again. Also, when the switch 12 is closed to the a contact, the calculation of the PID calculation section 4 is stopped, and when switching from the a contact to the b contact, the switch 6 is instantaneously closed and the predetermined integral is set by the integral initial value setting section 5. PID calculation 4 for initial value I 0
, and replaces it with the integral manipulated variable stored in the PID calculation section 4. The PID calculation unit 4 calculates the temperature C and the target value while the switch 12 is closed to the b contact.
Perform PID calculation based on the above formula (i) from SV,
The resulting operation amount y is output to the heater drive circuit 15, and the switching element is controlled to control the amount of heat generated by the heater 14 based on the operation amount y.
次に第2図のマイクロコンピユータ2のソフト
ウエアを示すフローチヤートに基づき、第3図の
温度Cの時間推移を示す図を参照して動作を説明
する。電源投入からスタートしてステツプ20で
温度設定部7から目標温度SVを読み込み、ステ
ツプ21で温度検出部8から庫内温度Cを読み込
み、それに基づいて偏差eをステツプ22で算出
し、ステツプ23でそれに基づき、式(i)によつて
PID演算を実行し操作量yを決定する。次にステ
ツプ24で温度Cが上限温度DH以上か否か判別
する。 Next, the operation will be explained based on the flowchart showing the software of the microcomputer 2 shown in FIG. 2, and with reference to the diagram showing the time course of the temperature C shown in FIG. Starting from power-on, the target temperature SV is read from the temperature setting part 7 in step 20, the internal temperature C is read from the temperature detection part 8 in step 21, the deviation e is calculated in step 22 based on it, and the deviation e is calculated in step 23. Based on that, by equation (i)
Execute PID calculation and determine the manipulated variable y. Next, in step 24, it is determined whether the temperature C is higher than the upper limit temperature DH.
ここで第3図は周囲温度が例えば+20℃で目標
温度SVが+5℃である時の温度制御を示してお
り、図中i点では温度CはDHより高いからステ
ツプ26に進んでスイツチ12をa接点に閉じ、
圧縮機13を駆動してヒータ14の出力は停止さ
せる。次にステツプ27と28で同様に目標温度
SVと温度Cを読み込み、ステツプ29で温度C
がDL以下か否か判断する。第3図中i点では否
であるからステツプ26に戻る。以下ステツプ2
6から29を繰り返えしてインキユベータ内を冷
却して行き、第3図中j点おいて温度CがDLに
達するとステツプ29から30に進み、スイツチ
6を閉じてPID演算部4に積分初期値I0を入力さ
せる。PID演算部4における積分操作量の変化は
第3図中最下段に示す。即ち温度CがDLに達し
た時点で積分操作量は所定の低い値(例えば−50
%)であるI0に初期値設定される。次にステツプ
20に戻り以下ステツプ21から23まで実行
し、ステツプ24では否であるからステツプ25
に進んでスイツチ12をb接点に切換え、ヒータ
14に操作量yに基づいて給電される状態とし、
圧縮機13を停止させる。 Here, FIG. 3 shows temperature control when the ambient temperature is, for example, +20°C and the target temperature SV is +5°C. At point i in the figure, temperature C is higher than DH, so proceed to step 26 and switch 12 is turned on. Closed to A contact,
The compressor 13 is driven and the output of the heater 14 is stopped. Next, in steps 27 and 28, the target temperature is set in the same way.
Read SV and temperature C, and set temperature C in step 29.
Determine whether or not is less than DL. Since the answer at point i in FIG. 3 is negative, the process returns to step 26. Step 2 below
Repeat steps 6 to 29 to cool down the inside of the incubator, and when the temperature C reaches DL at point j in Figure 3, proceed to steps 29 to 30, close switch 6, and let PID calculation section 4 integrate. Input the initial value I 0 . Changes in the integral operation amount in the PID calculation section 4 are shown in the bottom row of FIG. That is, when the temperature C reaches DL, the integral manipulated variable is set to a predetermined low value (for example, -50
%) is initialized to I 0 . Next, return to step 20 and execute steps 21 to 23 below, and since step 24 is negative, step 25 is executed.
, the switch 12 is switched to the B contact, and the heater 14 is in a state where power is supplied based on the manipulated variable y,
The compressor 13 is stopped.
この時第3図中j点では温度Cはアンダーシユ
ートにより低下する方向であるため、ステツプ2
3によるPID演算では式(i)の比例項及び微分項は
ヒータ14の発熱を増加させる方向即ち第3図中
の操作量yを増大させる方向に増加している。し
かし乍ら積分項はステツプ30でマイナス方向の
I0に初期値設定されているので操作量y全体とし
ては第5図の如く100%とはならず例えば30%程
となつているため、その後の温度Cの上昇は緩慢
となる。以後ステツプ20から25を繰り返えし
てヒータ14をPID制御することによつて庫内を
加熱して行くが、ヒータ14の発熱開始時の出力
が低いため上限温度DH付近では操作量y即ちヒ
ータ14の出力は相当低い値となつているため温
度Cの上昇速度は緩慢となつているため、第3図
中1点でDHに達し、ステツプ24から26に進
んで圧縮機13による冷却が開始されることによ
り、温度Cは直ぐに低下し始め、これによつて第
3図中l点以降の如く温度Cのオーバーシユート
は最少限に抑えられる。又、l点までの時間が長
くなるので圧縮機13起動時の負担が少なくな
る。以後これを繰り返えし、温度CをDHとDL
の範囲内に制御して行く。特に周囲温度より目標
温度SVが低い場合は、圧縮機13が停止すれば
ヒータ14を発熱させずとも温度Cは自然に上昇
して行くものであるから、積分初期値I0を設定し
ない場合は第5図の如く温度Cが非常に不安定と
なつてしまうが、本発明の如く制御すれば第3図
の如くオーバーシユートの少ない制御が達成され
るので、本発明は斯かる状況では格別有効とな
る。 At this time, at point j in FIG. 3, the temperature C is decreasing due to undershoot, so step 2
In the PID calculation according to No. 3, the proportional term and the differential term in equation (i) increase in the direction of increasing the heat generation of the heater 14, that is, in the direction of increasing the manipulated variable y in FIG. However, the integral term is negative in step 30.
Since the initial value is set to I0 , the manipulated variable y as a whole is not 100% as shown in FIG. 5, but is, for example, about 30%, so that the temperature C increases slowly thereafter. Thereafter, steps 20 to 25 are repeated to heat the inside of the refrigerator by PID control of the heater 14, but since the output of the heater 14 when it starts generating heat is low, the manipulated variable y, that is, near the upper limit temperature DH, is Since the output of the heater 14 is quite low, the rate of increase in temperature C is slow, so DH is reached at one point in FIG. By starting, the temperature C immediately begins to decrease, thereby minimizing the overshoot of the temperature C as shown after point l in FIG. Moreover, since the time to reach point l becomes longer, the burden when starting up the compressor 13 is reduced. After that, repeat this and change the temperature C to DH and DL.
Go within the control range. In particular, when the target temperature SV is lower than the ambient temperature, the temperature C will naturally rise even if the heater 14 does not generate heat if the compressor 13 stops, so if the initial integral value I 0 is not set, As shown in FIG. 5, the temperature C becomes very unstable, but if the temperature C is controlled as shown in FIG. 5, control with little overshoot can be achieved as shown in FIG. It becomes effective.
第4図は周囲温度が+20℃で目標温度SVが例
えば+30℃である場合の制御を示す。電源投入
時、温度Cは目標温度SVよりも十分低いからス
テツプ23における操作量yは100%の状態から
開始され、ステツプ20から25を繰り返えして
温度Cはヒータ14の加熱によつて上昇して行
く。ヒータ14の出力は目標温度SVに近づくに
従つて減少して行くが、図中m点で温度DHに達
した時点でステツプ24から26に進みスイツチ
12をa接点に切換えて圧縮機13の冷却が開始
される。ステツプ26から29を繰り返えして冷
却が進行し図中n点でDLに達したらステツプ2
9から30に進んで積分初期値I0を設定してステ
ツプ20に戻り、以下同様にステツプ20から2
5を繰り返えしてヒータ14のPID制御により庫
内の温度制御を行う。この場合もヒータ14の発
熱が開始された時点で操作量yは低い値となつて
いるから、その後目標温度SVに接近する過程で
温度Cの上昇率は緩慢となつているため目標温度
SVからのオーバーシユートは少なく、その後は
ヒータ14のPID制御によつて温度Cは目標温度
SVに安定的に制御されて行く。尚、実施例では
PID制御について述べたがPI制御であつても差支
えない。 FIG. 4 shows control when the ambient temperature is +20°C and the target temperature SV is, for example, +30°C. When the power is turned on, the temperature C is sufficiently lower than the target temperature SV, so the manipulated variable y in step 23 starts from 100%, and steps 20 to 25 are repeated until the temperature C is lowered by the heating of the heater 14. going up. The output of the heater 14 decreases as it approaches the target temperature SV, but when it reaches the temperature DH at point m in the figure, the process proceeds from steps 24 to 26, where the switch 12 is switched to the a contact and the compressor 13 is cooled. is started. Steps 26 to 29 are repeated until cooling progresses and when DL is reached at point n in the figure, step 2 is started.
Proceed from step 9 to step 30, set the initial integral value I0 , return to step 20, and then proceed from step 20 to step 2 in the same manner.
By repeating step 5, the temperature inside the refrigerator is controlled by PID control of the heater 14. In this case as well, since the manipulated variable y is at a low value when the heater 14 starts generating heat, the rate of increase in temperature C becomes slow in the process of approaching the target temperature SV, so the target temperature
There is little overshoot from SV, and after that the temperature C is kept at the target temperature by PID control of the heater 14.
Stably controlled by SV. In addition, in the example
Although PID control has been described, PI control may also be used.
(ト) 発明の効果
本発明によれば加熱手段と冷却手段を同時に駆
動しないので消費電力の削減が図れると共に、そ
れらの切換えも制御装置が自動的に行うので使用
者による管理が容易となる。特に冷却が不要な場
合は加熱手段のPI若しくはPID制御によつて安定
的な温度制御が可能となると共に、冷却が必要な
状況下で冷却手段の停止時にはPI若しくはPID演
算の積分操作量を所定の初期値に設定するので加
熱過剰によるオーバーシユートを減少せしめる事
になり、安定した恒温装置の温度制御が可能とな
るものである。(G) Effects of the Invention According to the present invention, power consumption can be reduced because the heating means and the cooling means are not driven at the same time, and since the control device automatically switches between them, management by the user is facilitated. In particular, when cooling is not required, stable temperature control is possible by PI or PID control of the heating means, and when the cooling means is stopped in situations where cooling is required, the integral operation amount of PI or PID calculation is set to a predetermined value. Since it is set to the initial value of , overshoot due to excessive heating is reduced, and stable temperature control of the thermostat is possible.
第1図乃至第4図は本発明の実施例を示すもの
で、第1図は温度制御装置の機能ブロツク図、第
2図はマイクロコンピユータのソフトウエアを示
すフローチヤート、第3図及び第4図は恒温装置
内温度の時間推移を示す図であり、第5図は第3
図に相当する従来の制御装置による温度の時間推
移を示す図である。
1……温度制御装置、2……マイクロコンピユ
ータ、3……切換え制御部、4……PID演算部、
5……積分初期値設定部、7……温度設定部、8
……温度検出部、13……圧縮機、14……ヒー
タ。
1 to 4 show an embodiment of the present invention, in which FIG. 1 is a functional block diagram of a temperature control device, FIG. 2 is a flowchart showing software of a microcomputer, and FIGS. The figure shows the time course of the temperature inside the thermostat;
FIG. 2 is a diagram showing a temperature change over time according to a conventional control device corresponding to the diagram. 1...Temperature control device, 2...Microcomputer, 3...Switching control section, 4...PID calculation section,
5... Integral initial value setting section, 7... Temperature setting section, 8
...Temperature detection unit, 13...Compressor, 14...Heater.
Claims (1)
却手段とをそれぞれ駆動することにより前記恒温
装置内を目標温度に保持するものにおいて、前記
目標温度を設定する手段と、前記恒温装置内の温
度を検出する手段と、前記目標温度と前記恒温装
置内の温度に基づき前記加熱手段若しくは冷却手
段を交互に駆動すると共に前記加熱手段をPI若
しくはPID制御するための演算部を有した制御手
段とを備え、該制御手段は前記冷却手段が停止す
る時に前記演算部に所定の積分初期値を設定する
手段を具備している事を特徴とする恒温装置の温
度制御装置。1. In a device that maintains the inside of the constant temperature device at a target temperature by respectively driving a heating means for heating the inside of the constant temperature device and a cooling means for cooling the inside of the constant temperature device, a means for setting the target temperature and a means for setting the temperature inside the constant temperature device are provided. and a control means having a calculation unit for driving the heating means or the cooling means alternately based on the target temperature and the temperature in the constant temperature device and controlling the heating means by PI or PID. . A temperature control device for a constant temperature device, wherein the control means includes means for setting a predetermined integral initial value in the arithmetic unit when the cooling means is stopped.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6332587A JPS63229150A (en) | 1987-03-18 | 1987-03-18 | Temperature controlling system of thermostatic equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6332587A JPS63229150A (en) | 1987-03-18 | 1987-03-18 | Temperature controlling system of thermostatic equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63229150A JPS63229150A (en) | 1988-09-26 |
| JPH0455738B2 true JPH0455738B2 (en) | 1992-09-04 |
Family
ID=13225993
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6332587A Granted JPS63229150A (en) | 1987-03-18 | 1987-03-18 | Temperature controlling system of thermostatic equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63229150A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5320908B2 (en) * | 2008-08-29 | 2013-10-23 | 富士通株式会社 | Temperature control device for temperature chamber |
| CN102274766B (en) * | 2011-05-03 | 2014-08-13 | 宁波大学 | Chemical laboratory water saving apparatus containing heat storage link |
-
1987
- 1987-03-18 JP JP6332587A patent/JPS63229150A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63229150A (en) | 1988-09-26 |
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