JP3154039B2 - Temperature control device and temperature control method for water heater - Google Patents

Temperature control device and temperature control method for water heater

Info

Publication number
JP3154039B2
JP3154039B2 JP06545895A JP6545895A JP3154039B2 JP 3154039 B2 JP3154039 B2 JP 3154039B2 JP 06545895 A JP06545895 A JP 06545895A JP 6545895 A JP6545895 A JP 6545895A JP 3154039 B2 JP3154039 B2 JP 3154039B2
Authority
JP
Japan
Prior art keywords
temperature
heating
hot water
cold
heater
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 - Fee Related
Application number
JP06545895A
Other languages
Japanese (ja)
Other versions
JPH08261590A (en
Inventor
雅巳 仁藤
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.)
Yazaki Corp
Original Assignee
Yazaki Corp
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Filing date
Publication date
Application filed by Yazaki Corp filed Critical Yazaki Corp
Priority to JP06545895A priority Critical patent/JP3154039B2/en
Publication of JPH08261590A publication Critical patent/JPH08261590A/en
Application granted granted Critical
Publication of JP3154039B2 publication Critical patent/JP3154039B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

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、冷温水機の温度制御装
置及び温度制御方法に係り、特に、熱を発生させる加熱
手段の加熱を受ける熱媒体の異常温度及び圧力から冷温
水機の機器を保護し、且つ冷温水の制御を可能にする冷
温水機の温度制御装置及び温度制御方法に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a temperature control device and a temperature control method for a chiller / heater, and more particularly to an apparatus for a chiller / heater based on abnormal temperature and pressure of a heat medium which is heated by a heating means for generating heat. The present invention relates to a temperature control device and a temperature control method for a water heater and a water heater that protects the water and controls the cold and hot water.

【0002】[0002]

【従来の技術】図8は、従来技術に係る吸収式冷温水機
の系統図である。吸収式冷温水機2は、冷房時には、稀
溶液32bを加熱する加熱源14を有する高温再生器1
5と、高温再生器15で加熱された稀溶液32aを冷媒
蒸気33aと中間濃度溶液34aとに分離する分離器1
8と、分離器18からの中間濃度溶液34aと高温再生
器15に流入する稀溶液32cとを熱交換させる高温溶
液熱交換器19と、分離器18から導かれた冷媒蒸気3
3aにより中間濃度溶液34bを加熱し冷媒蒸気33b
と濃溶液35aとに分離する低温再生器20と、低温再
生器20からの冷媒蒸気33a、33bを凝縮させる凝
縮器21とを有している。
2. Description of the Related Art FIG. 8 is a system diagram of an absorption type chiller / heater according to the prior art. The absorption chiller / heater 2 has a high-temperature regenerator 1 having a heating source 14 for heating the dilute solution 32b during cooling.
5 and a separator 1 for separating the dilute solution 32a heated by the high temperature regenerator 15 into a refrigerant vapor 33a and an intermediate concentration solution 34a.
8, a high-temperature solution heat exchanger 19 for exchanging heat between the intermediate concentration solution 34a from the separator 18 and the dilute solution 32c flowing into the high-temperature regenerator 15, and a refrigerant vapor 3 guided from the separator 18.
3a heats the intermediate-concentration solution 34b so that the refrigerant vapor 33b
A low-temperature regenerator 20 that separates the refrigerant vapor into a concentrated solution 35a; and a condenser 21 that condenses the refrigerant vapors 33a and 33b from the low-temperature regenerator 20.

【0003】更に、凝縮器21により濃縮した液冷媒3
1を散布して蒸発させ冷温水27を冷却する低圧の蒸発
器16と、低温再生器20から流入した濃溶液35aを
高温溶液熱交換器19に流入する稀溶液32cと熱交換
させ冷却する低温溶液熱交換器22と、低温溶液熱交換
器22からの濃溶液35bを散布し蒸発器16から流入
した冷媒蒸気を吸収させて稀溶液32dとする吸収器1
7と、吸収器17で生じた稀溶液32dを低温溶液熱交
換器22及び高温溶液熱交換器19を介して高温再生器
15に圧送する溶液循環ポンプ23とを有する。
Further, the liquid refrigerant 3 concentrated by the condenser 21
1 is sprayed and evaporated to cool the cold and hot water 27. The solution heat exchanger 22 and the absorber 1 which sprays the concentrated solution 35b from the low-temperature solution heat exchanger 22 and absorbs the refrigerant vapor flowing from the evaporator 16 into a diluted solution 32d.
7 and a solution circulation pump 23 for pumping the dilute solution 32 d generated in the absorber 17 to the high temperature regenerator 15 via the low temperature solution heat exchanger 22 and the high temperature solution heat exchanger 19.

【0004】尚、参照番号26aは、吸収器17での吸
収熱を取り去る冷却水熱交換器、参照番号26bは、凝
縮器21での凝縮熱を取り去る冷却水熱交換器、参照番
号30は、熱媒体である吸収溶液である。又、加熱源1
4で発生した排ガス36は煙突から排出される。
Reference numeral 26a denotes a cooling water heat exchanger for removing heat of absorption in the absorber 17, reference numeral 26b denotes a cooling water heat exchanger for removing heat of condensation in the condenser 21, and reference numeral 30 denotes It is an absorbing solution that is a heating medium. Heating source 1
The exhaust gas 36 generated in 4 is discharged from the chimney.

【0005】暖房時には、冷暖房切換弁25を開放す
る。従って、分離器18からの高温吸収溶液30aは、
吸収器17及び蒸発器16に入り、冷温水入口28から
流入した冷温水27は加熱されて温水となり冷温水出口
29から流出する。熱交換した稀溶液32dは、溶液循
環ポンプ23により低温溶液熱交換器22、高温溶液熱
交換器19を経て高温再生器15に圧送される。
At the time of heating, the cooling / heating switching valve 25 is opened. Therefore, the high-temperature absorbing solution 30a from the separator 18 is
The cold / hot water 27 that enters the absorber 17 and the evaporator 16 and flows in from the cold / hot water inlet 28 is heated to become hot water and flows out from the cold / hot water outlet 29. The heat-exchanged dilute solution 32 d is pumped to the high-temperature regenerator 15 via the low-temperature solution heat exchanger 22 and the high-temperature solution heat exchanger 19 by the solution circulation pump 23.

【0006】このような吸収式冷温水機2において、冷
温水27の温度による加熱源14の燃焼出力の多位置制
御を行なう場合、従来では、例えば冷房運転の場合、図
9に示すように、冷温水27である冷水の冷水温度と燃
焼出力の関係が矩形状乃至階段状になるような設定温度
Toで燃焼操作がなされていた。この冷房運転での冷水
の温度制御を例とするならば、最終的に制御される冷水
温度は次のようになる。冷房負荷が軽く冷水温度が6℃
以下になると燃焼が停止する。冷水温度が上昇して10
℃になると燃焼出力は100%となり、更に、冷水温度
が6℃になると、燃焼が停止するという繰り返しとな
り、結果として6℃から10℃の間で燃焼が操作される
ことになる。
In such an absorption type chiller / heater 2, when performing multi-position control of the combustion output of the heating source 14 based on the temperature of the chill / hot water 27, conventionally, for example, in a cooling operation, as shown in FIG. The combustion operation has been performed at the set temperature To such that the relationship between the chilled water temperature of the chilled water 27 as the chilled water 27 and the combustion output becomes rectangular or stepwise. If the temperature control of the chilled water in the cooling operation is taken as an example, the finally controlled chilled water temperature is as follows. Light cooling load and cold water temperature of 6 ℃
The combustion stops when the temperature falls below. Cold water temperature rises to 10
When the temperature reaches 0 ° C, the combustion output becomes 100%, and when the chilled water temperature reaches 6 ° C, the combustion is repeatedly stopped. As a result, the combustion is operated between 6 ° C and 10 ° C.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、このよ
うな吸収式冷温水機2において、冷温水の温度制御を行
なう場合、その燃焼出力の操作は、比例動作の場合は冷
温水出口29の温度によるPID動作で、2位置(燃焼
停止、100%燃焼)又は3位置(燃焼停止、50%燃
焼、100%燃焼)以上の多位置動作による燃焼の場合
は、上記図9のようなヒステリシスをもつ温度設定での
制御をとることが一般的である。
However, in such an absorption type chiller / heater 2, when controlling the temperature of chilled / hot water, the operation of the combustion output depends on the temperature of the chilled / hot water outlet 29 in the case of proportional operation. In the PID operation, when the combustion is performed by multi-position operation at two positions (combustion stop, 100% combustion) or three positions (combustion stop, 50% combustion, 100% combustion) or more, the temperature having hysteresis as shown in FIG. It is common to take control by setting.

【0008】この場合、従来では高温再生器15の吸収
溶液30の温度及び圧力が異常に上昇した場合に、例え
ば図10に示したように、本体保護として予め定められ
た設定温度である180℃になると、燃焼を強制的に停
止するといった操作や、冷温水出口29の温度とは無関
係に直接燃焼出力を減らすという操作がとられていた。
このような従来の冷温水制御では、高温再生器の吸収溶
液30の温度が高くなった場合に、冷温水出口29の温
度での制御を停止するという制御になるため、機器保護
という面では良いが、冷温水温度の確保という面では問
題であった。
In this case, when the temperature and the pressure of the absorbing solution 30 of the high-temperature regenerator 15 are abnormally increased, as shown in FIG. , The operation of forcibly stopping the combustion and the operation of directly reducing the combustion output irrespective of the temperature of the cold / hot water outlet 29 have been taken.
In such conventional cold / hot water control, when the temperature of the absorbing solution 30 of the high temperature regenerator becomes high, the control at the temperature of the cold / hot water outlet 29 is stopped, which is good in terms of equipment protection. However, there was a problem in securing the temperature of cold and hot water.

【0009】本発明の目的は、冷温水機の熱媒体の温度
及び圧力の異常上昇を防止して冷温水機の機器を保護す
ると共に、冷温水の温度制御が可能な冷温水機の温度制
御装置及び温度制御方法を提供することである。
SUMMARY OF THE INVENTION It is an object of the present invention to protect the equipment of a chiller / heater by preventing abnormal rises in temperature and pressure of a heat medium of the chiller / heater, and to control the temperature of a chiller / heater capable of controlling the temperature of the chiller and heater. It is to provide an apparatus and a temperature control method.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するため
本発明は、熱を発生させる加熱手段と、該加熱手段の加
熱を受けて熱媒体を加熱する被加熱手段と、前記熱媒体
を利用して冷温水を加熱し又は冷却する加熱冷却手段と
を有する冷温水機であって、前記加熱手段を操作して前
記冷温水の温度を制御する冷温水機の温度制御装置にお
いて、前記被加熱手段の熱媒体の温度を検出する温度検
出手段と、該温度検出手段で検出した熱媒体の検出温度
に対応して予め定められた前記冷温水の温度補正量を算
出し、該温度補正量を予め設定された前記冷温水の設定
温度に加算して新たな設定温度を算出し、該新たな設定
温度に基づいて前記加熱手段を操作する操作信号を送る
制御部とを備えたものである。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides a heating means for generating heat, a heated means for heating a heating medium in response to the heating of the heating means, and a heating medium utilizing the heating medium. A heating and cooling means for heating or cooling the cold and hot water by heating and cooling the hot and cold water, wherein the temperature control device of the cold and hot water machine for controlling the temperature of the cold and hot water by operating the heating means. Temperature detecting means for detecting the temperature of the heat medium of the means, and calculating a predetermined temperature correction amount of the cold and hot water corresponding to the detected temperature of the heat medium detected by the temperature detection means, and calculating the temperature correction amount. A control unit for calculating a new set temperature by adding to the preset set temperature of the cold / hot water, and transmitting an operation signal for operating the heating means based on the new set temperature.

【0011】更に、上記発明において、前記温度検出手
段は、前記被加熱手段の熱媒体の出口側近傍の温度を検
出するものである。
Further, in the above invention, the temperature detecting means detects a temperature in the vicinity of the heat medium outlet side of the heated means.

【0012】そして、上記いずれかの発明において、前
記冷温水機の温度制御装置は、燃料の燃焼熱を発生させ
る前記加熱手段と、吸収剤に冷媒が溶解した吸収溶液を
前記熱媒体として加熱する前記被加熱手段と、前記吸収
溶液を利用して冷温水を加熱し又は冷却する前記加熱冷
却手段とを有する吸収式冷温水機に設けられたものであ
る。
[0012] In any one of the above inventions, the temperature control device of the chiller / heater is configured to heat the heating means for generating heat of combustion of fuel and an absorbing solution in which a refrigerant is dissolved in an absorbent as the heating medium. It is provided in an absorption-type hot and cold water machine having the means to be heated and the heating and cooling means for heating or cooling cold and hot water using the absorbing solution.

【0013】又、熱を発生させる加熱手段で熱媒体を加
熱し、該熱媒体を利用して冷温水を加熱し又は冷却する
冷温水機の温度制御方法において、前記加熱手段で加熱
された前記熱媒体の温度を検出し、該検出した熱媒体の
検出温度に対応して予め定められた前記冷温水の温度補
正量を算出し、該温度補正量を予め設定された前記冷温
水の設定温度に加算して新たな設定温度を算出し、該新
たな設定温度に基づいて前記加熱手段を操作して前記冷
温水の温度を制御することである。
Further, in a temperature control method for a chiller / heater in which a heating medium is heated by heating means for generating heat and chilled or heated water is heated or cooled by using the heating medium, the heating medium is heated by the heating means. Detecting the temperature of the heat medium, calculating a predetermined temperature correction amount of the cold / hot water corresponding to the detected temperature of the heat medium, and setting the temperature correction amount to a preset temperature of the cold / hot water To calculate a new set temperature, and control the temperature of the cold and hot water by operating the heating means based on the new set temperature.

【0014】[0014]

【作用】本発明の冷温水機の温度制御装置によれば、被
加熱手段の熱媒体の温度を検出する温度検出手段と、こ
の熱媒体の検出温度に対応して予め定められた冷温水の
温度補正量を算出し、この温度補正量を予め設定された
冷温水の設定温度に加算して新たな設定温度を算出し、
この新たな設定温度に基づいて加熱手段を操作する操作
信号を送る制御部とを備えたものであるので、被加熱手
段の熱媒体の温度が上昇した場合には、この温度を検出
し、この検出温度に対応した予め定められた冷温水の温
度補正量を予め設定された冷温水の設定温度に加算し
て、新たな設定温度を目標に温度制御がなされるので、
冷温水機の負荷を実質的に小さくしたことと同じになり
加熱手段の発生熱量を抑えることが出来、これによっ
て、被加熱手段の熱媒体の温度を下げることが出来る。
従って、冷温水機の熱媒体の温度及び圧力の異常上昇を
防止して冷温水機の機器を保護すると共に、冷温水の温
度制御が可能になる。
According to the temperature control device of the chiller / heater of the present invention, a temperature detector for detecting the temperature of the heat medium of the means to be heated, and a chilled / hot water predetermined in correspondence with the detected temperature of the heat medium. Calculate the temperature correction amount, add this temperature correction amount to the preset temperature of cold and hot water to calculate a new set temperature,
And a control unit for sending an operation signal for operating the heating means based on the new set temperature, so that when the temperature of the heat medium of the heated means rises, this temperature is detected, and By adding a predetermined temperature correction amount of the cold / hot water corresponding to the detected temperature to the preset temperature of the cold / hot water, and the temperature is controlled with the target of the new set temperature,
This is the same as substantially reducing the load of the water heater, and the amount of heat generated by the heating means can be reduced, thereby reducing the temperature of the heat medium of the heated means.
Therefore, the temperature and pressure of the heat medium of the chiller / heater can be prevented from abnormally rising to protect the chiller / heater, and the temperature of the chiller / heater can be controlled.

【0015】更に、上記発明において、温度検出手段
は、被加熱手段の熱媒体の出口側近傍の温度を検出する
ものであるので、上記発明の作用に加え、被加熱手段の
熱媒体の温度異常を確実に検出することが出来、冷温水
発生機の温度制御装置の制御性と信頼性が向上する。
Further, in the above invention, the temperature detecting means detects the temperature in the vicinity of the outlet of the heating medium of the heated means. And the controllability and reliability of the temperature control device of the cold / hot water generator are improved.

【0016】そして、上記いずれかの発明において、冷
温水機の温度制御装置は、吸収式冷温水機に設けられた
ものであるので、上記いずれかの発明の作用に加え、吸
収式冷温水機において、冷温水機の熱媒体の温度及び圧
力の異常上昇を防止して冷温水機の機器を保護すると共
に、冷温水の温度制御が可能になる。
In any one of the above inventions, the temperature control device of the chiller / heater is provided in the absorption chiller / heater. In this case, the temperature and pressure of the heat medium of the chiller / heater can be prevented from being abnormally increased, thereby protecting the chiller / heater and controlling the temperature of the chiller / heater.

【0017】又、本発明の冷温水機の温度制御方法によ
れば、加熱手段で加熱された熱媒体の温度を検出し、こ
の検出した熱媒体の検出温度に対応して予め定められた
冷温水の温度補正量を算出し、この温度補正量を予め設
定された冷温水の設定温度に加算して新たな設定温度を
算出し、この新たな設定温度に基づいて加熱手段を操作
して冷温水の温度を制御することであるので、熱媒体の
温度が上昇した場合には、この温度を検出し、この検出
温度に対応した予め定められた冷温水の温度補正量を予
め設定された冷温水の設定温度に加算して、新たなより
高い設定温度を目標に温度制御を行なうので、冷温水機
の負荷を実質的に小さくしたことと同じになり加熱手段
の発生熱量を抑えることが出来、これによって、熱媒体
の温度を下げることが出来る。従って、熱媒体の温度及
び圧力の異常上昇を防止すると共に、冷温水の温度制御
が可能になる。
Further, according to the temperature control method for a water heater of the present invention, the temperature of the heating medium heated by the heating means is detected, and a predetermined cooling temperature corresponding to the detected temperature of the heating medium is detected. The temperature correction amount of the water is calculated, the temperature correction amount is added to the preset temperature of the cold and hot water to calculate a new set temperature, and the heating means is operated based on the new set temperature to control the cold temperature. Since the temperature of the water is controlled, when the temperature of the heat medium rises, this temperature is detected, and the temperature correction amount of the predetermined cold / hot water corresponding to the detected temperature is set to the predetermined cold / hot temperature. Since the temperature is controlled with the target of a new higher set temperature added to the set temperature of water, the load on the chiller / heater is reduced substantially, and the amount of heat generated by the heating means can be reduced. This reduces the temperature of the heating medium. It can be. Therefore, it is possible to prevent abnormal rises in the temperature and pressure of the heat medium and to control the temperature of the cold and hot water.

【0018】[0018]

【実施例】以下、本発明に係る冷温水機の温度制御装置
及び温度制御方法の実施例を図面に基づいて詳細に説明
する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of a temperature control device and a temperature control method for a chiller / heater according to the present invention will be described below in detail with reference to the drawings.

【0019】図2は、本実施例の温度制御装置を適用し
た吸収式冷温水機の系統図である。本実施例の温度制御
装置3は、燃料の燃焼熱を発生させる加熱手段である加
熱源14と、この加熱源14の加熱を受けて熱媒体であ
る吸収剤に冷媒が溶解した吸収溶液30を加熱する被加
熱手段である高温再生器15と、吸収溶液30を利用し
て冷温水27を加熱し又は冷却する加熱冷却手段である
蒸発器16及び吸収器17とを有するものである。
FIG. 2 is a system diagram of an absorption chiller / heater to which the temperature control device of the present embodiment is applied. The temperature control device 3 according to the present embodiment includes a heating source 14 that is a heating unit that generates combustion heat of fuel, and an absorption solution 30 in which a refrigerant is dissolved in an absorbent that is a heating medium by receiving heat from the heating source 14. It has a high-temperature regenerator 15 as heating means to be heated, and an evaporator 16 and an absorber 17 as heating and cooling means to heat or cool the cold / hot water 27 using the absorbing solution 30.

【0020】更に、冷温水機の温度制御装置3は、高温
再生器15の吸収溶液30の出口側近傍の温度を検出す
る温度検出手段である再生器温度検出器4と、再生器温
度検出器4で検出した吸収溶液30の検出温度に対応し
て予め定められた冷温水27の温度補正量Hを算出し、
この温度補正量Hを予め設定された冷温水27の設定温
度に加算して新たな設定温度を算出し、この新たな設定
温度に基づいて加熱源14を操作する操作信号を送る制
御部6とを備えたものである。吸収式冷温水機1は、温
度制御装置3を除いて、従来技術の説明で示した図8の
吸収式冷温水機2と同一のものである。図2において図
8と同一構造、作用部分には同一の参照番号を付けてそ
の説明を省略する。
Further, the temperature control device 3 of the chiller / heater includes a regenerator temperature detector 4 as temperature detecting means for detecting a temperature near the outlet side of the absorbing solution 30 of the high temperature regenerator 15, and a regenerator temperature detector. Calculating a predetermined temperature correction amount H of the cold / hot water 27 corresponding to the detected temperature of the absorption solution 30 detected in 4;
The controller 6 adds the temperature correction amount H to a preset set temperature of the cold / hot water 27 to calculate a new set temperature, and sends an operation signal for operating the heating source 14 based on the new set temperature. It is provided with. The absorption chiller / heater 1 is the same as the absorption chiller / heater 2 shown in FIG. In FIG. 2, the same structure and operation as those in FIG. 8 are denoted by the same reference numerals, and description thereof will be omitted.

【0021】図3は、図2に示した温度制御装置3の制
御部6の系統図である。制御部6は、冷温水出口温度検
出器13が検出する冷温水出口29の温度信号を変換し
て中央演算処理部10へ出力する冷温水温度検出回路9
と、同様に、高温再生器15の吸収溶液30の出口側近
傍温度15aの温度信号を変換して中央演算処理部10
へ出力する再生器温度検出回路11とを有する。
FIG. 3 is a system diagram of the control unit 6 of the temperature control device 3 shown in FIG. The control unit 6 converts a temperature signal of the cold / hot water outlet 29 detected by the cold / hot water outlet temperature detector 13 and outputs the signal to the central processing unit 10.
Similarly, the temperature signal of the temperature 15a near the outlet side of the absorbing solution 30 of the high-temperature regenerator 15 is converted and the central processing unit 10
And a regenerator temperature detection circuit 11 for outputting to the regenerator.

【0022】更に、破線で示すように制御部6内の各回
路の操作用及び制御用電力を供給する電源回路7と、各
種バルブ、真空ポンプ、溶液循環ポンプ、圧縮機等の圧
力、流量等の検出信号を変換して中央演算処理部10へ
出力し、逆に中央演算処理部10からの制御信号を受け
て前記各種バルブ、真空ポンプ、溶液循環ポンプ、圧縮
機等に操作信号を送る周辺入出力回路8と、中央演算処
理部10からの制御信号を受けて加熱源14の燃焼用バ
ルブ、ファン等に操作信号6aを送り、又風圧スイッ
チ、安全装置等の検出信号を変換し中央演算処理部10
に出力する燃焼制御回路12とを有するものである。
Further, as indicated by broken lines, a power supply circuit 7 for supplying power for operating and controlling each circuit in the control section 6 and pressure, flow rate, etc. of various valves, vacuum pumps, solution circulation pumps, compressors and the like. And outputs the detected signal to the central processing unit 10, and conversely, receives the control signal from the central processing unit 10 and sends operation signals to the various valves, vacuum pumps, solution circulation pumps, compressors, etc. In response to a control signal from the input / output circuit 8 and the central processing unit 10, an operation signal 6a is sent to a combustion valve, a fan, and the like of the heating source 14, and a detection signal from a wind pressure switch, a safety device, and the like is converted and the central processing is performed. Processing unit 10
And a combustion control circuit 12 for output to

【0023】以上のような冷温水機の温度制御装置3の
作用について、図1〜7に基づいて説明する。図1は、
本発明に係る冷温水機の温度制御装置の一実施例の制御
フローチャートであるが、先ず再生器温度検出器4によ
って高温再生器15の吸収溶液30の温度Tgを検出す
る。燃焼制御回路12は、再生器温度検出器4が検出し
た吸収溶液30の温度Tgの温度信号を変換して中央演
算処理部10に出力する。この変換信号を受けて中央演
算処理部10は、図4に示すように、予め定められた高
温再生器の吸収溶液温度と冷温水出口の温度補正量Hと
の関係により冷温水出口の温度補正量Hを算出する。
The operation of the temperature control device 3 of the water heater will be described with reference to FIGS. FIG.
1 is a control flowchart of an embodiment of a temperature control device for a water heater according to the present invention. First, a regenerator temperature detector 4 detects a temperature Tg of an absorption solution 30 of a high temperature regenerator 15. The combustion control circuit 12 converts the temperature signal of the temperature Tg of the absorption solution 30 detected by the regenerator temperature detector 4 and outputs the converted signal to the central processing unit 10. Upon receiving this conversion signal, the central processing unit 10 corrects the temperature of the cold / hot water outlet based on the predetermined relationship between the temperature of the absorbing solution of the high-temperature regenerator and the temperature correction amount H of the cold / hot water outlet, as shown in FIG. The quantity H is calculated.

【0024】次に、図7に示すように、予め設定された
冷温水である冷水温度と燃焼出力との関係の冷水の設定
温度Toに上記温度補正量Hを加算して新たに冷水の設
定温度Tsを算出する。新たな冷水の設定温度Tsは、
図7では縦の破線で示され、縦の実線を補正量Hだけ右
に移動した破線である。新たな設定温度Tsによると、
例えば7〜11℃間で、燃焼出力0%と100%の間で
加熱源14の燃焼が切り替わるような操作となる。ここ
でもし、負荷が大きく冷水温度が上昇するならば、11
℃で100%燃焼となり、冷水温度が下がって冷水温度
が7℃になると0%燃焼に切り替わる。
Next, as shown in FIG. 7, the temperature correction amount H is added to a preset cold water temperature To which is a relationship between the cold water temperature, which is the cold water temperature, and the combustion output to newly set the cold water. Calculate the temperature Ts. The set temperature Ts of the new cold water is
In FIG. 7, a vertical dashed line is a dashed line obtained by moving the vertical solid line to the right by the correction amount H. According to the new set temperature Ts,
For example, the operation is such that the combustion of the heating source 14 is switched between 0% and 100% between 7 and 11 ° C. Here, if the load is large and the chilled water temperature rises, 11
When the temperature of the cold water drops to 7 ° C., the combustion switches to 0% combustion.

【0025】高温再生器15の吸収溶液温度Tgと冷温
水出口の温度補正量Hとの関係は、必ずしも図4のよう
に、略140℃から、冷房時は右上がりの直線、暖房時
は右下がりの直線になる設定にする必要はなく、例え
ば、図5或いは6の高温再生器の吸収溶液温度Tgと冷
温水出口の温度補正量Hとの関係図に示したように、冷
房時、暖房時共に曲線的に変化させた場合も考えられ
る。
As shown in FIG. 4, the relationship between the absorption solution temperature Tg of the high-temperature regenerator 15 and the temperature correction amount H at the outlet of the cold / hot water is necessarily from approximately 140 ° C. It is not necessary to make the setting such that it becomes a downward straight line. For example, as shown in the relationship diagram of the absorption solution temperature Tg of the high-temperature regenerator and the temperature correction amount H at the cold / hot water outlet in FIG. It is also conceivable to change the curve with time.

【0026】上記実施例は、冷温水機の冷房時の場合に
ついて説明したが、暖房時の温水制御の場合でも、更に
2位置制御だけでなく、3位置制御以上での多段階制御
或いは比例(P)動作、積分(I)動作或いはPID動
作等の制御動作でも、その設定温度自体に補正をかける
ことにより同様の制御が可能である。
Although the above embodiment has been described with respect to the case of cooling of the chiller / heater, in the case of hot water control during heating, not only two-position control but also multi-step control or three-position control or proportional ( In the control operation such as the P) operation, the integration (I) operation or the PID operation, similar control can be performed by correcting the set temperature itself.

【0027】次に、本実施例の冷温水機の温度制御方法
は、熱を発生させる加熱手段である加熱源において、熱
媒体である吸収溶液を加熱し、この吸収溶液を利用して
冷温水を加熱し又は冷却するものであって、加熱源で加
熱された吸収溶液の温度を検出し、この検出した吸収溶
液の検出温度に対応して予め定められた冷温水の温度補
正量を算出し、この温度補正量を予め設定された冷温水
の設定温度に加算して新たな設定温度を算出し、この新
たな設定温度に基づいて加熱源を操作して冷温水の温度
を制御することである。
Next, according to the temperature control method of the chiller / heater of the present embodiment, a heating source, which is a heating means for generating heat, heats an absorbing solution as a heat medium, and uses the absorbing solution to cool and cool the water. Heating or cooling, detecting the temperature of the absorbing solution heated by the heating source, and calculating a predetermined temperature correction amount of cold and hot water corresponding to the detected temperature of the detected absorbing solution. By adding this temperature correction amount to a preset set temperature of cold and hot water to calculate a new set temperature, and operating the heating source based on the new set temperature to control the temperature of the cold and hot water. is there.

【0028】従って、吸収溶液の温度が上昇した場合に
は、この温度を検出し、この検出温度に対応した予め定
められた冷温水の温度補正量を予め設定された冷温水の
設定温度に加算して、新たなより高い設定温度を目標に
温度制御を行なうので、冷温水機の負荷を実質的に小さ
くしたことと同じになり加熱源の発生熱量を抑えること
が出来、これによって、吸収溶液の温度を下げることが
出来る。従って、吸収溶液の温度及び圧力の異常上昇を
防止すると共に、冷温水の温度制御が可能になる。
Therefore, when the temperature of the absorbing solution rises, this temperature is detected, and a predetermined temperature correction amount of the cold / hot water corresponding to the detected temperature is added to the preset temperature of the cold / hot water. Then, since the temperature is controlled with the target of a new higher set temperature, the load on the water heater is substantially reduced, and the amount of heat generated by the heating source can be suppressed. Can be lowered. Accordingly, it is possible to prevent abnormal rises in the temperature and pressure of the absorbing solution and to control the temperature of the cold and hot water.

【0029】以上説明したように、高温再生器の吸収溶
液温度を検出することによって冷温水出口の設定温度を
自動的に補正することで、機器の保護機能を働かせなが
らも、要求温度に近い冷温水出口温度の制御が可能にな
るため、高温再生器の温度、圧力の異常状態に近い状況
においても、冷温水出口の温度制御が可能になる。
As described above, by automatically correcting the set temperature of the cold / hot water outlet by detecting the temperature of the absorbing solution of the high-temperature regenerator, the cold temperature close to the required temperature can be maintained while the protection function of the device is operated. Since the water outlet temperature can be controlled, it is possible to control the temperature of the cold / hot water outlet even in a situation close to an abnormal state of the temperature and pressure of the high-temperature regenerator.

【0030】[0030]

【発明の効果】本発明の冷温水機の温度制御装置によれ
ば、冷温水の設定温度に補正量を加算することにより、
冷温水機の負荷を実質的に小さくすることになり、従っ
て、冷温水機の熱媒体の温度及び圧力の異常上昇を防止
して冷温水機の機器を保護すると共に、冷温水の温度制
御が可能になる。
According to the temperature control apparatus for a water heater of the present invention, the correction amount is added to the set temperature of the water heater,
This substantially reduces the load on the chiller / heater, thereby preventing the temperature and pressure of the heating medium of the chiller / heater from being abnormally increased to protect the chiller / heater equipment and controlling the temperature of the chiller / heater. Will be possible.

【0031】更に、上記発明において、温度検出手段
は、被加熱手段の熱媒体の出口側近傍の温度を検出する
ものであるので、上記発明の効果に加え、被加熱手段の
熱媒体の温度の異常を確実に検出することが出来、冷温
水機の温度制御装置の制御性と信頼性が向上する。
Further, in the above invention, the temperature detecting means detects the temperature in the vicinity of the outlet of the heating medium of the heated means. An abnormality can be reliably detected, and the controllability and reliability of the temperature control device of the chiller / heater are improved.

【0032】そして、上記いずれかの発明において、冷
温水機の温度制御装置は、吸収式冷温水機に設けられた
ものであるので、上記いずれかの発明の効果に加え、吸
収式冷温水機において、冷温水機の熱媒体の温度及び圧
力の異常上昇を防止して冷温水機の機器を保護すると共
に、冷温水の温度制御が可能になる。
In any one of the above inventions, the temperature control device for the chiller / heater is provided in the absorption chiller / heater. In this case, the temperature and pressure of the heat medium of the chiller / heater can be prevented from being abnormally increased, thereby protecting the chiller / heater and controlling the temperature of the chiller / heater.

【0033】又、本発明の冷温水機の温度制御方法によ
れば、冷温水の設定温度に補正量を加算することによ
り、冷温水の冷却又は加熱の負荷を実質的に小さくする
ことになり、従って、冷温水を冷却又は加熱する熱媒体
の温度及び圧力の異常上昇を防止すると共に、冷温水の
温度制御が可能になる。
According to the method of controlling the temperature of the water heater of the present invention, the load of cooling or heating of the water is substantially reduced by adding the correction amount to the set temperature of the water. Therefore, it is possible to prevent the temperature and pressure of the heat medium for cooling or heating the cold and hot water from being abnormally increased, and to control the temperature of the cold and hot water.

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

【図1】本発明に係る冷温水機の温度制御装置の一実施
例の制御フローチャートである。
FIG. 1 is a control flowchart of an embodiment of a temperature control device for a water heater according to the present invention.

【図2】本実施例の温度制御装置を適用した吸収式冷温
水機の系統図である。
FIG. 2 is a system diagram of an absorption chiller / heater to which the temperature control device of the present embodiment is applied.

【図3】図2に示した温度制御装置の制御部の系統図で
ある。
FIG. 3 is a system diagram of a control unit of the temperature control device shown in FIG. 2;

【図4】本実施例の高温再生器の吸収溶液温度と冷温水
出口の温度補正量との関係図である。
FIG. 4 is a relationship diagram between the temperature of the absorbing solution of the high-temperature regenerator and the temperature correction amount at the outlet of the cold / hot water in the present embodiment.

【図5】高温再生器の吸収溶液温度と冷温水出口の温度
補正量との別の関係図である。
FIG. 5 is another relationship diagram between the absorption solution temperature of the high-temperature regenerator and the temperature correction amount of the cold / hot water outlet.

【図6】高温再生器の吸収溶液温度と冷温水出口の温度
補正量との更に別の関係図である。
FIG. 6 is a diagram showing still another relationship between the temperature of the absorbing solution of the high-temperature regenerator and the temperature correction amount at the outlet of the cold / hot water.

【図7】本実施例の冷水温度と燃焼出力との関係図であ
る。
FIG. 7 is a diagram showing the relationship between the chilled water temperature and the combustion output according to the present embodiment.

【図8】従来技術に係る吸収式冷温水機の系統図であ
る。
FIG. 8 is a system diagram of an absorption chiller / heater according to the related art.

【図9】図8に示した吸収式冷温水機の冷水温度と燃焼
出力の関係図である。
9 is a diagram showing a relationship between a chilled water temperature and a combustion output of the absorption chiller / heater shown in FIG.

【図10】図9に示した高温再生器の吸収溶液温度と燃
焼状態との関係図である。
FIG. 10 is a diagram showing the relationship between the temperature of the absorbing solution and the combustion state of the high-temperature regenerator shown in FIG.

【符号の説明】[Explanation of symbols]

1 吸収式冷温水機(冷温水機) 3 温度制御装置 4 再生器温度検出器(温度検出手段) 6 制御部 14 加熱源(加熱手段) 15 高温再生器(被加熱手段) 16 蒸発器(加熱冷却手段) 17 吸収器(加熱冷却手段) 27 冷温水 30 吸収溶液(熱媒体) DESCRIPTION OF SYMBOLS 1 Absorption chiller / heater (cooler / heater) 3 Temperature controller 4 Regenerator temperature detector (temperature detection means) 6 Control part 14 Heat source (heating means) 15 High temperature regenerator (heated means) 16 Evaporator (heating) Cooling means) 17 absorber (heating and cooling means) 27 cold and hot water 30 absorbing solution (heat medium)

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 熱を発生させる加熱手段と、該加熱手段
の加熱を受けて熱媒体を加熱する被加熱手段と、前記熱
媒体を利用して冷温水を加熱し又は冷却する加熱冷却手
段とを有する冷温水機であって、前記加熱手段を操作し
て前記冷温水の温度を制御する冷温水機の温度制御装置
において、前記被加熱手段の熱媒体の温度を検出する温
度検出手段と、該温度検出手段で検出した熱媒体の検出
温度に対応して予め定められた前記冷温水の温度補正量
を算出し、該温度補正量を予め設定された前記冷温水の
設定温度に加算して新たな設定温度を算出し、該新たな
設定温度に基づいて前記加熱手段を操作する操作信号を
送る制御部とを備えたものであることを特徴とする冷温
水機の温度制御装置。
1. A heating means for generating heat, a heated means for heating a heating medium by receiving heat from the heating means, and a heating and cooling means for heating or cooling cold and hot water using the heating medium. A chilled / hot water machine having a temperature control device for controlling the temperature of the chilled / hot water by operating the heating means, wherein a temperature detecting means for detecting a temperature of a heat medium of the heated means, Calculate a predetermined temperature correction amount of the cold / hot water corresponding to the detected temperature of the heat medium detected by the temperature detection means, and add the temperature correction amount to a preset temperature of the cold / hot water. A controller for calculating a new set temperature and sending an operation signal for operating the heating means based on the new set temperature.
【請求項2】 請求項1において、前記温度検出手段
は、前記被加熱手段の熱媒体の出口側近傍の温度を検出
するものであることを特徴とする冷温水機の温度制御装
置。
2. The temperature control device for a water heater according to claim 1, wherein the temperature detecting means detects a temperature near an outlet side of the heating medium of the heating means.
【請求項3】 請求項1又は2において、前記冷温水機
の温度制御装置は、燃料の燃焼熱を発生させる前記加熱
手段と、吸収剤に冷媒が溶解した吸収溶液を前記熱媒体
として加熱する前記被加熱手段と、前記吸収溶液を利用
して冷温水を加熱し又は冷却する前記加熱冷却手段とを
有する吸収式冷温水機に設けられたものであることを特
徴とする冷温水機の温度制御装置。
3. The temperature control device of the chiller / heater according to claim 1, wherein the heating means for generating heat of combustion of the fuel and an absorbing solution in which a refrigerant is dissolved in an absorbent are heated as the heating medium. The temperature of the chilled / hot water machine characterized by being provided in an absorption type chilled / hot water machine having the heated means and the heating / cooling means for heating or cooling the chilled / hot water using the absorbing solution. Control device.
【請求項4】 熱を発生させる加熱手段で熱媒体を加熱
し、該熱媒体を利用して冷温水を加熱し又は冷却する冷
温水機の温度制御方法において、前記加熱手段で加熱さ
れた前記熱媒体の温度を検出し、該検出した熱媒体の検
出温度に対応して予め定められた前記冷温水の温度補正
量を算出し、該温度補正量を予め設定された前記冷温水
の設定温度に加算して新たな設定温度を算出し、該新た
な設定温度に基づいて前記加熱手段を操作して前記冷温
水の温度を制御することを特徴とする冷温水機の温度制
御方法。
4. A method for controlling the temperature of a chiller / heater in which a heating medium is heated by heating means for generating heat, and the chilled or heated water is heated or cooled by using the heating medium. Detecting the temperature of the heat medium, calculating a predetermined temperature correction amount of the cold / hot water corresponding to the detected temperature of the heat medium, and setting the temperature correction amount to a preset temperature of the cold / hot water And calculating a new set temperature, and operating the heating means to control the temperature of the cold and hot water based on the new set temperature.
JP06545895A 1995-03-24 1995-03-24 Temperature control device and temperature control method for water heater Expired - Fee Related JP3154039B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06545895A JP3154039B2 (en) 1995-03-24 1995-03-24 Temperature control device and temperature control method for water heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06545895A JP3154039B2 (en) 1995-03-24 1995-03-24 Temperature control device and temperature control method for water heater

Publications (2)

Publication Number Publication Date
JPH08261590A JPH08261590A (en) 1996-10-11
JP3154039B2 true JP3154039B2 (en) 2001-04-09

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Country Link
JP (1) JP3154039B2 (en)

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Publication number Priority date Publication date Assignee Title
JP5551857B2 (en) * 2008-07-09 2014-07-16 大阪瓦斯株式会社 Burner combustion furnace

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