JPS61821A - Temperature controller of heavy oil heater - Google Patents

Temperature controller of heavy oil heater

Info

Publication number
JPS61821A
JPS61821A JP12065584A JP12065584A JPS61821A JP S61821 A JPS61821 A JP S61821A JP 12065584 A JP12065584 A JP 12065584A JP 12065584 A JP12065584 A JP 12065584A JP S61821 A JPS61821 A JP S61821A
Authority
JP
Japan
Prior art keywords
heavy oil
oil heater
output
control
water level
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.)
Pending
Application number
JP12065584A
Other languages
Japanese (ja)
Inventor
Kazuo Komeno
米野 一夫
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12065584A priority Critical patent/JPS61821A/en
Publication of JPS61821A publication Critical patent/JPS61821A/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D23/00Control of temperature
    • G05D23/19Control of temperature characterised by the use of electric means
    • G05D23/1919Control of temperature characterised by the use of electric means characterised by the type of controller

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Automation & Control Theory (AREA)
  • Control Of Temperature (AREA)

Abstract

PURPOSE:To secure a wide control range without deteriorating the controllability by applying the control of temperature that controls only a range of low heat exchange quantity where the controllability is deteriorated according to the increase or decrease of the heat transmission area. CONSTITUTION:When the output of a deviation controller 2 is set lower than a certain level to the opening amount of a steam flow rate control valve 4, the output of a function generator 7 is outputted by changing the level set value by an amount larger than the reference water level 10. Thus a difference is produced between the output of a condensed level oscillator 6 and that of a function generator 7, and the output of a deviation controller 8 delivers a closed signal to a condensed water level control valve 9. The level 10 is raised up for condensed water by closing the valve 9, and the control of temperature is carried out within a range of low heat exchange quantity with reduction of a heat transmission area. Thus a wide control range of temperatures is secured without deteriorating the controllability.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、重油加熱器の温度制御装置において従来の制
御性を損わずに広い制御範囲を確保できるようにした制
御装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a temperature control device for a heavy oil heater that can ensure a wide control range without impairing conventional controllability.

従来の技術 従来の重油加熱器温度制御装置は、たとえば。Conventional technology Conventional heavy oil heater temperature control devices, for example.

第2図に示したように、重油加熱器出口重油温度発信器
】と、偏差調節計2と、重油加熱器出口重油温度設定器
3と、重油加熱器蒸気流量制御弁4とで構成されており
、重油加熱器出口重油温度とその設定温度との偏差より
求まる重油加熱器蒸気流量制御弁開度により蒸気流量を
変化させて熱交換量を制御している。
As shown in FIG. 2, it is composed of a heavy oil heater outlet heavy oil temperature transmitter], a deviation controller 2, a heavy oil heater outlet heavy oil temperature setting device 3, and a heavy oil heater steam flow rate control valve 4. The heat exchange amount is controlled by changing the steam flow rate based on the opening degree of the heavy oil heater steam flow rate control valve, which is determined from the deviation between the heavy oil temperature at the outlet of the heavy oil heater and its set temperature.

そのため従来の温度制御装置では、蒸気流量制御弁4の
レンジアビリティがそのまま重油加熱器の制御範囲とな
っていた。
Therefore, in the conventional temperature control device, the rangeability of the steam flow rate control valve 4 is directly within the control range of the heavy oil heater.

発明が解決しようとする問題点 本発明は、制御性の低下する低熱交換量の範囲をも制御
して従来の温度制御装置よりも、より広い制御範囲を確
保した温度制御装置を提供することを目的とする。
Problems to be Solved by the Invention The present invention aims to provide a temperature control device that can control even the range of low heat exchange amount where controllability deteriorates and secure a wider control range than conventional temperature control devices. purpose.

問題点を解決するための手段 本発明による重油加熱器温度制御装置は、重油加熱器蒸
気流量制御弁の開度を調節する調節計と、同調節計出力
が入力されて重油加熱器凝縮水レベル設定値を出力する
関数発生器と、同関数発生器出力および重油加熱器凝縮
水レベル発信器出力が入力されて重油加熱器凝縮水レベ
ル制御弁開度調節信号を出力する調節計とを具えて、制
御性の低下する低熱交換量の範囲のみを伝熱面積の増減
により行なう温度制御を加えたことにより、従来の制御
方式の制御性を損わずに広い制御範囲を確保している。
Means for Solving the Problems The heavy oil heater temperature control device according to the present invention includes a controller that adjusts the opening degree of the heavy oil heater steam flow control valve, and an output of the controller that is inputted to adjust the heavy oil heater condensate water level. The controller includes a function generator that outputs a set value, and a controller that receives the output of the function generator and the output of the heavy oil heater condensed water level transmitter and outputs a heavy oil heater condensed water level control valve opening adjustment signal. By adding temperature control that is performed by increasing or decreasing the heat transfer area only in the range of low heat exchange amount where controllability deteriorates, a wide control range is secured without impairing the controllability of the conventional control method.

実施例 以下第1図に例示した本発明の好適な実施例について詳
述する。
EXAMPLES Below, a preferred embodiment of the present invention illustrated in FIG. 1 will be described in detail.

第1図において、重油加熱器の温度制御装置は、重油加
熱器(熱交換器)11と、重油加熱器蒸気流量制御弁4
と、重油加熱器凝縮水レベル制御弁9と、ドレントラッ
プ5とより構成され、これに重油加熱器出口重油温度発
信器1と、重油加熱器出口重油温度設定器3と、その重
油温度発信器1およびその設定器3の出力信号の偏差調
節計2と。
In FIG. 1, the temperature control device for the heavy oil heater includes a heavy oil heater (heat exchanger) 11 and a heavy oil heater steam flow control valve 4.
, a heavy oil heater condensed water level control valve 9, and a drain trap 5, and a heavy oil heater outlet heavy oil temperature transmitter 1, a heavy oil heater outlet heavy oil temperature setting device 3, and the heavy oil temperature transmitter. 1 and a deviation controller 2 of the output signal of the setting device 3.

重油加熱器凝縮水レベル発信器6と、偏差調節計2の偏
差出力に対する関数発生器7と、凝縮水レベル発信器6
および関数発生器7の出力信号の偏差調節計8とが接続
されてぐる。
A heavy oil heater condensed water level transmitter 6, a function generator 7 for the deviation output of the deviation controller 2, and a condensed water level transmitter 6
and a deviation controller 8 for the output signal of the function generator 7 are connected.

作用について説明すると、重油加熱器出口重油温度発信
器1の出力と、重油加熱器出口重油温度設定器3の出力
とを入力とする偏差調節計2の出力は、重油加熱器蒸気
流量制御弁4の開度指令および関数発生器70入力とな
る。関数発生器7の出力は重油加熱器凝縮水レベルの目
標値となる。
To explain the operation, the output of the deviation controller 2 which receives the output of the heavy oil heater outlet heavy oil temperature transmitter 1 and the output of the heavy oil heater outlet heavy oil temperature setting device 3 is determined by the output of the heavy oil heater steam flow rate control valve 4. This becomes the opening command and the function generator 70 input. The output of the function generator 7 becomes the target value for the heavy oil heater condensate level.

この目標値と重油加熱器凝縮水レベル発信器6の出力と
を入力とする偏差調節計8の出力は重油加熱器凝縮水レ
ベル制御弁9への制御信号となる。
The output of the deviation controller 8, which receives this target value and the output of the heavy oil heater condensed water level transmitter 6, becomes a control signal to the heavy oil heater condensed water level control valve 9.

この制御系では、重油加熱器出口重油温度を設定温度に
制御する為に、偏差調節計2の出力により重油加熱器蒸
気流量制御弁4を操作しているが、その蒸気流量制御弁
4の開度に対して、偏差調節計2の出力があるレベル以
上であれば関数発生器7は、基準水量10以下のレベル
設定値を出力している。
In this control system, in order to control the heavy oil temperature at the outlet of the heavy oil heater to a set temperature, the heavy oil heater steam flow control valve 4 is operated by the output of the deviation controller 2. If the output of the deviation controller 2 is above a certain level with respect to the water level, the function generator 7 outputs a level setting value of the reference water amount of 10 or less.

重油加熱器凝縮水レベル発信器6の出力は、基準水量1
0以下のレベル信号を出せないので、凝縮水レベル発信
器6と関数発生器7どの出力を入力とする偏差調節計8
は凝縮水レベル制御弁9に対して全開信号を出力してい
る。この制御状態は、凝縮水レベル制御弁9が全開のた
め従来の制御と同様である。
The output of the heavy oil heater condensed water level transmitter 6 is the reference water level 1.
Since it is not possible to output a level signal below 0, a deviation controller 8 whose input is the output of the condensed water level transmitter 6 and the function generator 7 is used.
outputs a fully open signal to the condensed water level control valve 9. This control state is similar to conventional control because the condensed water level control valve 9 is fully open.

次に、蒸気流量制御弁4の開度に対して、偏差調節計2
の出力があるレベル以下になった場合、関数発生器7の
出力は、基準水量10以上にレベル設定値を変化させて
出力する。そこで、凝縮水レベル発信器6の出力と関数
発生器7の出力とに偏差が発生し、偏差調節計8の出力
は凝縮水レベル制御弁9に対して閉信号を出力する。凝
縮水レベル制御弁9が閉じることにより、凝縮水の基準
水量100レベルを上昇させて、伝熱面積を狭くし、低
熱交換量の範囲における温度制御が行なわれる。
Next, the deviation controller 2
When the output of the function generator 7 becomes less than a certain level, the output of the function generator 7 changes the level setting value to a reference water amount of 10 or more and outputs it. Therefore, a deviation occurs between the output of the condensed water level transmitter 6 and the output of the function generator 7, and the output of the deviation controller 8 outputs a close signal to the condensed water level control valve 9. By closing the condensed water level control valve 9, the standard water amount 100 level of condensed water is raised, the heat transfer area is narrowed, and temperature control is performed in the range of low heat exchange amount.

上述のように、従来制御装置では、重油加熱器出口重油
温度と設定温度との偏差より求まる重油加熱器蒸気流量
制御弁開度とにより蒸気流量を変化させて熱交換量を制
御しており、その為蒸気流量制御弁のし/シアビリティ
が重油加熱器の制御範囲となっていたのに対し、本発明
による装置では、温度制御の為の蒸気流量制御を蒸気流
量が少ない状態(蒸気流量制御弁開度が小さい時)にな
ると、重油加熱器内の凝縮水レベル制御を使用すること
により重油加熱器内の伝熱面積を凝縮水レベルの変化で
変化させ、熱交換量を制御するようにして、従来の制御
装置よりもより広い制御範囲を確保することができると
いった効果がある。
As mentioned above, in the conventional control device, the amount of heat exchange is controlled by changing the steam flow rate based on the opening degree of the heavy oil heater steam flow rate control valve, which is determined from the deviation between the heavy oil temperature at the outlet of the heavy oil heater and the set temperature. For this reason, the shearability of the steam flow control valve was limited to the control range of the heavy oil heater, whereas in the device according to the present invention, the steam flow rate control for temperature control is performed when the steam flow rate is low (steam flow rate control When the valve opening degree is small), the condensed water level control in the heavy oil heater is used to change the heat transfer area in the heavy oil heater with changes in the condensed water level and control the amount of heat exchange. This has the effect of ensuring a wider control range than conventional control devices.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明による重油加熱器温度制御装置の概要を
例示する系統図、第2図は従来の重油加熱器温度制御装
置の代表例を示す系統図である。 1・・重油温度発信器、2・・偏差調節計、3・・重油
温度設定器、4・・蒸気流量制御弁、5・・ドレントラ
ップ、6・・凝縮水レベル発信器、7・・関数発生器、
8・・偏差調節計、9・・凝縮水レベル制御弁、10・
・基準水量、11・・重油加熱器(熱交換器)。 (はか2名)
FIG. 1 is a system diagram illustrating the outline of a heavy oil heater temperature control device according to the present invention, and FIG. 2 is a system diagram showing a typical example of a conventional heavy oil heater temperature control device. 1. Heavy oil temperature transmitter, 2. Deviation controller, 3. Heavy oil temperature setting device, 4. Steam flow control valve, 5. Drain trap, 6. Condensed water level transmitter, 7. Function generator,
8. Deviation controller, 9. Condensed water level control valve, 10.
- Standard water volume, 11... Heavy oil heater (heat exchanger). (2 people)

Claims (1)

【特許請求の範囲】[Claims] 重油加熱器蒸気流量制御弁の開度を調節する調節計と、
同調節計出力が入力されて重油加熱器凝縮水レベル設定
値を出力する関数発生器と、同関数発生器出力および重
油加熱器凝縮水レベル発信器出力が入力されて重油加熱
器凝縮水レベル制御弁開度調節信号を出力する調節計と
を具えてなる重油加熱器温度制御装置。
a controller that adjusts the opening degree of the heavy oil heater steam flow control valve;
A function generator receives the controller output and outputs the heavy oil heater condensate level set value, and a function generator receives the same function generator output and the heavy oil heater condensate water level transmitter output to control the heavy oil heater condensate water level. A heavy oil heater temperature control device comprising a controller that outputs a valve opening adjustment signal.
JP12065584A 1984-06-14 1984-06-14 Temperature controller of heavy oil heater Pending JPS61821A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12065584A JPS61821A (en) 1984-06-14 1984-06-14 Temperature controller of heavy oil heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12065584A JPS61821A (en) 1984-06-14 1984-06-14 Temperature controller of heavy oil heater

Publications (1)

Publication Number Publication Date
JPS61821A true JPS61821A (en) 1986-01-06

Family

ID=14791605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12065584A Pending JPS61821A (en) 1984-06-14 1984-06-14 Temperature controller of heavy oil heater

Country Status (1)

Country Link
JP (1) JPS61821A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008126134A (en) * 2006-11-20 2008-06-05 Chubu Electric Power Co Inc Halogen-containing gas dry processing apparatus and dry processing method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008126134A (en) * 2006-11-20 2008-06-05 Chubu Electric Power Co Inc Halogen-containing gas dry processing apparatus and dry processing method

Similar Documents

Publication Publication Date Title
KR840001677A (en) Bypass device for steam turbine
JPS61821A (en) Temperature controller of heavy oil heater
JP2558700B2 (en) Plant warming controller
DE59406398D1 (en) Control device
KR900002153A (en) Quantity controller of water heater
SU1645757A2 (en) Method of level control in steam turbine regenerative heater
JPH01118034A (en) Mixer for hot water and water
JP2600915B2 (en) Water heater
JPS608437B2 (en) Condenser vacuum control device
JPH0452454A (en) Water temperature controller for instantaneous water heater
JPH0339227B2 (en)
JPH0330755Y2 (en)
JPS6354553A (en) Control device of hot water supplier
JPS6222382B2 (en)
JPH0123072Y2 (en)
JP2831502B2 (en) Shower equipment
JPS6238131Y2 (en)
RU1802261C (en) Method of level control in regenerative heater of steam turbine
JPS6190701A (en) Control device for multiple-effect evaporator
SU1092284A2 (en) System for controlling a heat and power steam turbine unit
JPH04720Y2 (en)
JPS5989924A (en) Fluidized bed boiler inlet air pressure control device
JPS6373055A (en) Refrigeration equipment
JPS61284576A (en) Method for controlling vacuum evaporating apparatus
JPS6226414A (en) Flow control valve control device