JPS5841423B2 - Absorption refrigeration equipment that uses waste heat - Google Patents

Absorption refrigeration equipment that uses waste heat

Info

Publication number
JPS5841423B2
JPS5841423B2 JP53156187A JP15618778A JPS5841423B2 JP S5841423 B2 JPS5841423 B2 JP S5841423B2 JP 53156187 A JP53156187 A JP 53156187A JP 15618778 A JP15618778 A JP 15618778A JP S5841423 B2 JPS5841423 B2 JP S5841423B2
Authority
JP
Japan
Prior art keywords
heat
amount
generator
control valve
load
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
Application number
JP53156187A
Other languages
Japanese (ja)
Other versions
JPS5582271A (en
Inventor
彬宏 高田
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.)
Daikin Industries Ltd
Original Assignee
Daikin Kogyo Co 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 Daikin Kogyo Co Ltd filed Critical Daikin Kogyo Co Ltd
Priority to JP53156187A priority Critical patent/JPS5841423B2/en
Publication of JPS5582271A publication Critical patent/JPS5582271A/en
Publication of JPS5841423B2 publication Critical patent/JPS5841423B2/en
Expired legal-status Critical Current

Links

Classifications

    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 本発明は、排熱利用の吸収式冷凍装置に関する。[Detailed description of the invention] TECHNICAL FIELD The present invention relates to an absorption refrigerating device that utilizes waste heat.

更に詳記すると、工場等にふ・いて大気に排棄される主
として燃焼排ガスやその他蒸気又は温水などの排熱を利
用し、冷水と温水との少くとも一方を供給できるように
した吸収式冷凍装置に関する。
More specifically, absorption refrigeration is a type of absorption refrigeration that is capable of supplying at least one of cold water and hot water by using exhaust heat from combustion exhaust gas, other steam, or hot water that is discharged into the atmosphere from factories, etc. Regarding equipment.

一般に蒸発器で製造する冷水と、発生器に接続した温水
熱交換器で製造する温水との少くとも一方、詳しくは前
記冷水と温水との両方、又は切換えにより前記冷水と温
水との内いずれか一方、又は冷水のみ(以下これらを総
合して供給水という)を供給できるようにした吸収式冷
凍装置に釦いては、発生器に入熱する熱量と、前記供給
水の供給側負荷とが互いに変動すると、発生器の圧力が
異常に上昇したり、又能力不足を起こして所期の前記供
給水が得られなかったり、溶液が結晶したりするなどし
て正常な運転を行なえなくなるので、前記供給水の供給
側負荷により前記発生器に入熱する熱量を制御している
。
In general, at least one of cold water produced by an evaporator and hot water produced by a hot water heat exchanger connected to a generator; specifically, both the cold water and hot water, or either the cold water or the hot water by switching. On the other hand, in the case of absorption refrigerating equipment that can supply only cold water (hereinafter collectively referred to as supply water), the amount of heat entering the generator and the supply side load of the supply water are mutually exclusive. If the pressure fluctuates, the pressure of the generator may rise abnormally, the capacity may become insufficient and the desired supply water may not be obtained, or the solution may crystallize, making normal operation impossible. The amount of heat input to the generator is controlled by the load on the supply side of the supply water.

所が発生器に入熱する熱量を、前記冷凍装置のために設
ける専用の加熱源から得る場合には、前記入熱熱量の制
御で、前記供給水の供給側負荷が変化しても、所期の前
記供給水を取出すことができるのであるが、専用加熱源
を設けることなく排熱を利用する場合には、入熱熱量を
、例えば排ガスの流量を絞ったり、分流させたりして制
御すれば、排熱系統の作動状態が変化し、工場に赴ける
本機に影響を与えることがある。
When the amount of heat input to the generator is obtained from a dedicated heat source provided for the refrigeration equipment, the amount of heat input can be controlled to ensure that the amount of heat input to the generator changes even if the load on the supply side of the supply water changes. However, when using waste heat without installing a dedicated heating source, the amount of heat input must be controlled by, for example, restricting the flow rate of the waste gas or dividing the flow. For example, the operating status of the heat exhaust system may change, which may affect the machine that can go to the factory.

例えば燃焼脱臭を行なう脱臭装置の排ガス熱を利用する
場合、排ガスの排出経路に絞り弁やバイパス弁を設けて
、発生器への入熱量を制御すると、脱臭装置に釦ける内
圧が変化し、脱臭機能を阻害することになるのである。
For example, when using exhaust gas heat from a deodorizing device that performs combustion deodorization, if a throttle valve or bypass valve is installed in the exhaust gas exhaust path to control the amount of heat input to the generator, the internal pressure at the button of the deodorizing device will change, and the deodorizing device will be deodorized. This will impede its functionality.

そこで本発明は、前記した排ガスなどの排熱を利用しな
がら、排熱熱源側に悪影響を及ぼすことなく、しかも前
記排熱量の大きさ如何に拘わらず前記供給水の供給側負
荷に応じた熱量で運転できるようにしたものであって、
前記排熱熱源側からの排熱を規制することなく、その1
1発生器に導入するごとく威し、かつ発生器に放熱器を
設けると共に発生器の圧力を検出する圧力検出器を設け
て、発生器への最少入熱量に対し入熱量が増加するとき
の圧力増加を検出して過剰に入熱する排熱を放熱するご
とく制御し、この制御により前記供給水の供給側負荷及
び発生器への入熱量が変動しても常に能力の過不足なく
前記供給水が取り出されるようにしたのである。
Therefore, the present invention utilizes waste heat such as the above-mentioned exhaust gas, does not adversely affect the waste heat heat source side, and, regardless of the size of the waste heat amount, the amount of heat is determined according to the load on the supply side of the supply water. It is designed so that it can be driven with
Part 1: Without regulating the exhaust heat from the exhaust heat heat source side
1.The generator is equipped with a radiator and a pressure detector to detect the pressure of the generator, and the pressure when the amount of heat input increases relative to the minimum amount of heat input to the generator The increase is detected and the excess heat input is controlled so as to be radiated. Through this control, even if the supply side load of the supply water and the amount of heat input to the generator fluctuate, the supply water is always maintained at its capacity without excess or deficiency. was made so that it could be taken out.

しかして本発明の特徴は、特許請求の範囲に記載した通
りであって、特許請求の範囲第1項に記載した第1番目
の発明は、発生器に排熱熱源を接続し、蒸発器に冷水負
荷を接続し前記排熱を利用して冷水を供給できるように
した吸収式冷凍装置であって、前記発生器に、該発生器
に入熱する排熱の放熱器を接続して、たの接続回路にモ
ジュトロールモータにより動作する放熱量制御弁を介装
すると共に、前記冷水負荷を検出し、該負荷に応じた制
御信号を発信するごとくした負荷検出器を設ける一方、
発生器に入熱する最少入熱量に対し入熱量が増加すると
きの圧力増加を検出する圧力検出器を設けて、圧力増加
に応じた制御信号を発信するごとく威し、前記放熱量制
御弁のモジュトロールモータに、前記発生器への最少入
熱量と入熱量の増加分とを加算した制御信号から、前記
負荷検出器に訃ける負荷に応じた制御信号を減算した出
力信号を与え、前記放熱量制御弁の弁開度を制御するご
とくしたことを特徴とするものである。
Therefore, the features of the present invention are as described in the claims, and the first invention described in claim 1 is characterized in that a waste heat heat source is connected to the generator and the evaporator is connected to the exhaust heat source. An absorption refrigeration system that connects a chilled water load and can supply chilled water using the exhaust heat, wherein the generator is connected to a radiator for the exhaust heat that is input to the generator. A heat radiation amount control valve operated by a Modutrol motor is interposed in the connection circuit, and a load detector is provided for detecting the chilled water load and transmitting a control signal according to the load,
A pressure detector is provided to detect an increase in pressure when the amount of heat input increases with respect to the minimum amount of heat input into the generator, and a pressure detector is provided to detect the increase in pressure when the amount of heat input increases with respect to the minimum amount of heat input into the generator. An output signal obtained by subtracting a control signal corresponding to the load applied to the load detector from a control signal obtained by adding the minimum amount of heat input to the generator and an increase in the amount of heat input is given to the Modutrol motor. This is characterized in that the opening degree of the heat quantity control valve is controlled.

また特許請求の範囲第2項に記載した第2番目の発明は
前記第1番目の発明に釦いて、蒸発器に冷水負荷を、捷
た発生器に接続する温水熱交換器に温水負荷をそれぞれ
接続して冷房と暖房とを切換運転可能としたものであっ
て、前記温水熱交換器で作る温水の加温能力制御弁を設
けて、モジュトロールモータにより動作させ弁開度に応
じた制御信号を発信するごとく威す一方、冷水負荷を検
出し、負荷に応じた制御信号を発信する冷水負荷検出器
を設けると共に、前記放熱量制御弁のモジュトロールモ
ータに、前記発生器への最少入熱量と入熱量の増加分と
を加算した制御信号から、前記能力制御弁と冷水負荷検
出器との一方から発信する制御信号を減算した出力信号
を与え、前記放熱量制御弁の弁開度を制御するごとくし
たものである。
Further, the second invention described in claim 2 is based on the first invention, and provides a cold water load to the evaporator and a hot water load to the hot water heat exchanger connected to the shunted generator. The device is connected to enable switching operation between cooling and heating, and is equipped with a heating capacity control valve for hot water produced by the hot water heat exchanger, which is operated by a modutrol motor and receives a control signal according to the valve opening degree. At the same time, a chilled water load detector is provided to detect the chilled water load and issue a control signal according to the load. An output signal is provided by subtracting a control signal transmitted from one of the capacity control valve and the chilled water load detector from a control signal obtained by adding the amount of heat input and the increase in heat input amount, and the valve opening degree of the heat release amount control valve is controlled. It was a great accomplishment.

また特許請求の範囲第3項及び第4項に記載した第3番
目及び第4番目の発明は、いずれも第1番目の発明に釦
いて、蒸発器に冷水負荷を、また発生器に接続する温水
熱交換器に温水負荷をそれぞれ接続して、冷房と暖房と
を同時運転可能とした吸収式冷凍装置であって、先ず第
3番目の発明は、温水熱交換器で作る温水の加温能力制
御弁を設けてモジュトロールモータにより動作させ、弁
開度に応じた制御信号を発信するごとく威すと共に、冷
水負荷を検出し、負荷に応じた制御信号を発信する冷水
負荷検出器を設けて、前記放熱量制御弁のモジュトロー
ルモータに、前記発生器への最少入熱量と入熱量の増加
分とを加算した制御信号から、前記能力制御弁の弁開度
に応じた制御信号と、冷水負荷検出器からの制御信号と
の加算合計を減算した出力信号を与え、前記放熱量制御
弁の弁開度を制御するごとくしたものである。
In addition, the third and fourth inventions described in claims 3 and 4 are based on the first invention, and connect a chilled water load to the evaporator and a generator. The third invention is an absorption refrigeration system that connects each hot water load to a hot water heat exchanger to enable simultaneous operation of cooling and heating. A control valve is provided and operated by a modutrol motor to send out a control signal according to the valve opening degree, and a chilled water load detector is installed to detect the chilled water load and send out a control signal according to the load. , a control signal corresponding to the valve opening degree of the capacity control valve is generated from a control signal obtained by adding the minimum amount of heat input to the generator and an increase in the amount of heat input to the modutrol motor of the heat release amount control valve, and a control signal corresponding to the opening degree of the capacity control valve, and a cold water An output signal obtained by subtracting the sum from the control signal from the load detector is provided to control the valve opening degree of the heat radiation amount control valve.

そして第4番目の発明は、第3番目の発明にかいて蒸発
器で作る冷水の冷却能力を制御する冷却能力制御弁を設
け、この制御弁を温水の加温能力制御弁と同様にモジュ
トロールモータにより動作させ弁開度に応じた制御信号
を発信するごとく成したものである。
The fourth invention is to provide a cooling capacity control valve for controlling the cooling capacity of the cold water produced by the evaporator according to the third invention, and to control this control valve with a module control valve in the same way as the hot water heating capacity control valve. It is operated by a motor and sends a control signal according to the valve opening degree.

先ず本発明にふ−げる前記放熱量制御弁の弁開度制御方
式について説明する。
First, a method for controlling the opening degree of the heat radiation amount control valve according to the present invention will be explained.

この制御方式は、冷水及び温水の少なくとも一方の供給
側負荷を検出し、この負荷に応じた制御信号を発信する
ごとく威すと共に、発生器に入熱する最少入熱量に対し
入熱量が増加したときの圧力増加に応じた制御信号を発
信するごとく威し、これら制御信号により制御するもの
で、第1図に基づいて説明する。
This control method detects the load on the supply side of at least one of cold water and hot water, sends a control signal according to this load, and increases the amount of heat input relative to the minimum amount of heat input to the generator. The system is designed to transmit control signals corresponding to the increase in pressure at a given time, and to control based on these control signals, which will be explained based on FIG.

第1図に示したものは、冷水の冷却能力を制御する冷却
能力制御弁Aと、温水の加温能力制御弁Bと、発生器に
入熱する最少入熱量に対し入熱量が増加したときの圧力
増加を検出する圧力検出器Cとを設け、これら能力制御
弁A、B及び圧力検出器Cの作動状態に見合う制御信号
により制御するごとくしたものである。
What is shown in Figure 1 is the cooling capacity control valve A that controls the cooling capacity of cold water, the heating capacity control valve B of hot water, and when the amount of heat input increases relative to the minimum amount of heat input to the generator. A pressure detector C for detecting an increase in pressure is provided, and control is performed using control signals appropriate to the operating states of these capacity control valves A, B and pressure detector C.

尚第1図では冷水の冷却能力制御弁Aを設けたが、この
制御弁Aを設けないで、冷水負荷に応じた制御信号を発
信可能とした冷水負荷検出器を用いるごとくしてもよい
。
Although the chilled water cooling capacity control valve A is provided in FIG. 1, the control valve A may not be provided and a chilled water load detector capable of transmitting a control signal according to the chilled water load may be used.

即ち前記能力制御弁A、Bを動作させるモジュトロール
モータの補助ポテンショメータD 1 * D 2と、
前記圧力検出器Cの圧力を抵抗に変換した抵抗器C1と
、放熱量制御弁Eを動作させるモジュトロールモータの
フィードバックポテンショメータFとを組合わせてブリ
ッジ回路Gを形成し、前記能力制御弁A、Bの弁開度に
より与えられる出力信号及び発生器への最少入熱量と入
熱量の増加分とを、前記ブリッジ回路Gで加減算し、前
記放熱量制御弁Eを、排熱の全入熱量に見合う弁開度で
、かつ前記能力制御弁A、Bの弁開度合計に対し所定関
係の弁開度になるごとくするものである。
That is, auxiliary potentiometers D 1 * D 2 of the Modutrol motor that operate the capacity control valves A and B;
A bridge circuit G is formed by combining a resistor C1 that converts the pressure of the pressure detector C into resistance and a feedback potentiometer F of a modutrol motor that operates a heat radiation amount control valve E, and the capacity control valve A, The bridge circuit G adds and subtracts the output signal given by the valve opening degree of B, the minimum amount of heat input to the generator, and the increase in the amount of heat input, and the amount of heat radiation control valve E is adjusted to the total amount of heat input of exhaust heat. The valve opening is made to be appropriate and in a predetermined relationship with respect to the total valve opening of the capacity control valves A and B.

前記補助ポアンショメータD1.D2は、端子B2.W
2間及びB3.W3間にそれぞれ所定抵抗の抵抗体が接
続され、ワイパーaの駆動により、該ワイパーaに連通
する端子R2,R3と端子W21W3との間の抵抗r3
. r4が零から最大値1で変動するようになっている
。
The auxiliary pointiometer D1. D2 is the terminal B2. W
2 and B3. Resistors each having a predetermined resistance are connected between W3, and when the wiper a is driven, the resistance r3 between the terminals R2 and R3 communicating with the wiper a and the terminal W21W3 is increased.
.. r4 varies from zero to a maximum value of one.

そしてこれらワイパーaは能力制御弁A、Bを動作させ
るモジュトロールモータにより連動するようになってい
るのであって、能力制御弁A、Bの弁開度が零の時前記
抵抗r3m r4は最小の零となり、また弁開度がt
ookの時前記抵抗r3s r4は最大値となり、また
弁開度が中間状態の時各抵抗r3. r4は弁開度の増
加に応じて増加する値となるのである。
These wipers a are interlocked by a modtrol motor that operates the capacity control valves A and B, and when the opening degrees of the capacity control valves A and B are zero, the resistances r3m and r4 are at their minimum. becomes zero, and the valve opening becomes t.
When the valve opening is in the intermediate state, the resistances r3s and r4 are at their maximum values. The value r4 increases as the valve opening increases.

そして前記圧力検出器Cは、例えば第3図のごとく発生
器圧力Pを受圧したベローズから成る検出体2の変位量
を抵抗器C1のワイパーaに伝えるごとくして検出体C
1が検出する発生器内の圧力に応じて抵抗器C1のワイ
パーaが駆動し、該ワイパーaに連通する端子R1と端
子W1間の抵抗r1 が検出圧力に見合う抵抗値として
出力するようにしたものであって、該抵抗値は前記検出
圧力が所定の最低値、例えば700mmH?の時零とな
り、所定の最大値例えば750rurtHfの時最大抵
抗となり、そして中間圧力の時検出圧力の増加に応じて
増加する抵抗値となるようにするのである。
As shown in FIG. 3, the pressure detector C transmits the displacement of the detector 2, which is a bellows that receives the generator pressure P, to the wiper a of the resistor C1.
The wiper a of the resistor C1 is driven in accordance with the pressure inside the generator detected by the wiper a, and the resistance r1 between the terminal R1 and the terminal W1 communicating with the wiper a is output as a resistance value commensurate with the detected pressure. The resistance value is determined when the detected pressure is a predetermined minimum value, for example, 700 mmH? The resistance is zero at a predetermined maximum value, for example, 750rurtHf, and the resistance increases at an intermediate pressure as the detected pressure increases.

渣たこの圧力検出器Cは第4図のとと〈形成することも
できる。
The pressure detector C of the residue can also be formed as shown in FIG.

即ち第4図の圧力検出器Cは、発生器圧力Pの変化に応
じて上下方向に変位するごとくした検出体C2と、該検
出体C2の変位量を電流出力lに変換する変換器C3と
、該変換器C2から入力する電流値を抵抗値に変換する
変換器C4とから成り、前記変換器C3における高周波
電圧を印加したピンクアンプコイルL1i L2の印加
電圧比を、前記検出体C2により上下動するコアC5の
変位により変化させ、この変化を圧力Pの変化に比例し
た電流に変換して取出し、更に変換器C4により抵抗信
号を得るごとくしたものである。
That is, the pressure detector C in FIG. 4 includes a detecting body C2 that is vertically displaced in response to changes in the generator pressure P, and a converter C3 that converts the amount of displacement of the detecting body C2 into a current output l. , and a converter C4 that converts the current value input from the converter C2 into a resistance value, and the applied voltage ratio of the pink amplifier coil L1i L2 to which the high frequency voltage is applied in the converter C3 is adjusted up and down by the detecting body C2. This change is caused by the displacement of the moving core C5, and this change is converted into a current proportional to the change in pressure P and extracted, and a resistance signal is obtained by a converter C4.

また前記フィードバックポテンショメータFは、前記放
熱量制御弁Eを動作させるモジュトロールモータMを制
御するもので、該モータMに内蔵された端子B’、W’
間に所定抵抗の抵抗体が接続され、ワイパーaの駆動に
より該ワイパーaに連通ずる端子R′と端子W′との間
の抵抗r4が零から最大値1で変動するようになってい
る。
The feedback potentiometer F controls a modutrol motor M that operates the heat radiation amount control valve E, and has terminals B' and W' built into the motor M.
A resistor having a predetermined resistance is connected between them, and as the wiper a is driven, the resistance r4 between the terminal R' and the terminal W' communicating with the wiper a varies from zero to a maximum value of one.

そしてこのワイパーaは放熱量制御弁Eを動作させるモ
ジュトロールモータMにより連動するようになっている
のであって、放熱量制御弁Eの弁開度が零の時、前記抵
抗r4は最小の零となり、筐た弁開度が100%の時抵
抗r4は最大値となり、また弁開度が中間状態の時抵抗
r4は弁開度の増加に応じて増加する値となるのである
。
This wiper a is operated in conjunction with a modtrol motor M that operates a heat radiation amount control valve E, and when the valve opening degree of the heat radiation amount control valve E is zero, the resistance r4 is the minimum value of zero. Therefore, when the valve opening degree is 100%, the resistance r4 has a maximum value, and when the valve opening degree is in an intermediate state, the resistance r4 has a value that increases as the valve opening degree increases.

尚Hは冷水測温体、■は温水測温体、J、にはこれら測
温体により検出する冷水、温水の各負荷に対し前記能力
制御弁A、Bのモジュトロールモータを制御するコント
ローラー、C2は圧力検出体である。
In addition, H is a cold water temperature measuring device, ■ is a hot water temperature measuring device, and J is a controller that controls the modtrol motor of the capacity control valves A and B for each load of cold water and hot water detected by these temperature measuring devices. C2 is a pressure sensor.

尚冷水のみを供給するとき、並びに切換えにより冷水捷
たは温水のいずれか一方を供給できるようにするときは
、他方の能力制御弁A又はBの弁開度を零にすべく成す
ことにより行なえるが;この場合については後に第5図
に基づいて説明する。
Furthermore, when supplying only cold water, or when switching to supply either cold water or hot water, this can be done by setting the valve opening of the other capacity control valve A or B to zero. However, this case will be explained later based on FIG.

以下冷水及び温水を同時に供給する場合(但し供給量が
常置の場合を含む)について更に詳記する。
The case where cold water and hot water are supplied at the same time (including the case where the supply amount is constant) will be described in more detail below.

即ち前記発生器には排熱供給側から排熱を規制すること
なくその1x導入するごとく威し、斯く導入する排熱の
最少入熱量を基準とし、これを100とすれば発生器に
はこの100の最少入熱量と、該最少入熱量に対しP%
の入熱量の増加分とを入熱するごとくするものと考え、
前記最少入熱量100を基準としこれに対して放熱器で
の放熱量をz係とし、吸収器及び凝縮器での放熱量をQ
%、温水器での放熱量(温水加温能力)をY%、蒸発器
での入熱量(冷水冷却能力)をX%とすると、冷水と温
水とを同時(但しいずれか一方が零の場合を含む)に供
給する運転時の熱収支は出熱量と入熱量とが等しいから Z+Q+Y=X+100+P (但しZ、Q、Y。
In other words, if the exhaust heat is introduced into the generator from the exhaust heat supply side as if 1x without regulation, and if the minimum amount of heat input of the exhaust heat thus introduced is taken as a standard and this is set as 100, then the generator has this amount. 100 minimum heat input and P% for the minimum heat input
Assuming that the increase in heat input is the same as heat input,
Based on the above minimum heat input of 100, the amount of heat released by the radiator is set as the factor z, and the amount of heat released by the absorber and condenser is given as the factor Q.
%, the amount of heat dissipated in the water heater (hot water heating capacity) is Y%, and the amount of heat input in the evaporator (chilled water cooling capacity) is X%, then cold water and hot water are used simultaneously (however, if one of them is zero) Since the amount of heat output and the amount of heat input are equal, Z+Q+Y=X+100+P (however, Z, Q, Y).

x、pはいずれも≧0) となり、放熱器による放熱量2は、 Z = 100 +P+X −Y−Q となる。x and p are both ≧0) Therefore, the amount of heat radiated by the radiator 2 is Z = 100 +P+X -Y-Q becomes.

そして二重効用吸収式冷凍機にかける冷凍サイクルの効
率ははヒ1.0で、所定の冷水冷却能力を発揮させるた
めの発生画人熱量と冷水冷却能力(冷凍能力)とは等し
く、従って所定の冷水冷却能力Xを発揮しているときの
冷凍サイクルに釦ける吸収器及び凝縮器での放熱量Qは
冷水冷却能力を発揮させるための発生画人熱量と冷水冷
却能力Xとの合計即ち2Xとなるから、 Z=100+P+X−Y−2Xとなり Z=(1oO+p−(x+y)) となる。
The efficiency of the refrigeration cycle applied to the dual-effect absorption refrigerator is 1.0, and the amount of heat generated to exert the specified chilled water cooling capacity is equal to the chilled water cooling capacity (refrigeration capacity), so the specified chilled water cooling capacity (refrigeration capacity) is equal. The amount of heat dissipated by the absorber and condenser in the refrigeration cycle when the chilled water cooling capacity X is exerted is the sum of the amount of heat generated to exert the chilled water cooling capacity and the chilled water cooling capacity X, that is, 2X Therefore, Z=100+P+X-Y-2X and Z=(1oO+p-(x+y)).

このことから放熱器での放熱量は第1図に示した実施例
では冷水負荷と温水負荷との加算合計を、発生器に入熱
する排熱(100+P)から減算した値で制御すればよ
いことになる。
From this, in the example shown in Figure 1, the amount of heat radiated by the radiator can be controlled by the value obtained by subtracting the sum of the cold water load and hot water load from the waste heat (100+P) input to the generator. It turns out.

しかして第1図に示した前記ブリッジ回路Gを、前記第
2図のごとく以上の関係式を満足できるように形成する
のである。
Therefore, the bridge circuit G shown in FIG. 1 is formed so as to satisfy the above relational expression as shown in FIG. 2.

即ち前記冷却能力制御弁Aの補助ポテンショメータD1
の一方側と前記圧力検出器Cの抵抗器C1と前記フィー
ドバックポテンショメータFの一方側とを直列に接続す
ると共に、前記補助ポテンショメータD1の他方側と前
記加温能力制御弁Bの補助ポテンショメータD2と前記
フィードバックポテンショメータFの他方側とを直列に
接続してブリッジ回路Gを形成し、かつ前記補助ポテン
ショメータD11、及びフィードバックポテンショメー
タFの抵抗を、前記補助ポテンショメータD2及び抵抗
器c1の抵抗の1/2としたのである。
That is, the auxiliary potentiometer D1 of the cooling capacity control valve A
One side of the resistor C1 of the pressure detector C and one side of the feedback potentiometer F are connected in series, and the other side of the auxiliary potentiometer D1 and the auxiliary potentiometer D2 of the heating capacity control valve B are connected in series. A bridge circuit G is formed by connecting the other side of the feedback potentiometer F in series, and the resistance of the auxiliary potentiometer D11 and the feedback potentiometer F is set to 1/2 of the resistance of the auxiliary potentiometer D2 and the resistor c1. It is.

前記ブリッジ回路Gは第2図により明らかな通り、抵抗
器C1の端子R1をフィードバックポテンショメータF
の開側端子B′に接続し、抵抗器C1の低圧側端子W1
を補助ポテンショメータD1の開側端子B2 に接続
すると共に、この補助ポテンショメータD1の閉側端子
W2を補助ポテンショメータD2の端子R3に接続し、
この補助ポテンショメータD2の閉側端子W3をフィー
ドバックポテンショメータFの閉側端子W′に接続し、
かつ補助ポテンショメータD1 の端子R2ヲフィード
バックポテンショメータFの端子R′に電源りの直列回
路を介して接続して形成するのである。
As is clear from FIG. 2, the bridge circuit G connects the terminal R1 of the resistor C1 to the feedback potentiometer F.
connected to the open side terminal B' of the resistor C1 and the low voltage side terminal W1 of the resistor C1.
is connected to the open side terminal B2 of the auxiliary potentiometer D1, and the closed side terminal W2 of this auxiliary potentiometer D1 is connected to the terminal R3 of the auxiliary potentiometer D2,
Connect the closed side terminal W3 of this auxiliary potentiometer D2 to the closed side terminal W' of the feedback potentiometer F,
The terminal R2 of the auxiliary potentiometer D1 is connected to the terminal R' of the feedback potentiometer F via a series circuit connected to the power supply.

尚第2図に釦いてMl、N2は電磁石、N1.N2は回
転コイル、01,02はリレー接点、T1.T2は端子
で、この端子T1.T2間に前記交流電源りを介装して
いる。
In addition, in Fig. 2, the buttons Ml and N2 are electromagnets, and N1. N2 is a rotating coil, 01 and 02 are relay contacts, T1. T2 is a terminal, and this terminal T1. The AC power source is interposed between T2.

しかして以上のブリッジ回路に釦いて、前記能力制御弁
A、Bの弁開度力税閉制御されると補助ポテンショメー
タD1.D2のワイパーaが開または閉方向に動作し、
また前記圧力検出器Cが検出する発生器の歪力が変動す
ると、該圧力の変動に応じて抵抗器C1のワイパーaが
高圧側または低圧側に動作スるのであって、このワイパ
ーaの動作により、端子R1−Wl s B2 # R
2s R2# W2s R3゜R3間の抵抗が増減して
前記ブリッジ回路Gが不平衡となり、前記放熱量制御弁
EのモジュトロールモータMに釦げる電磁石M1.M2
の電磁力に差が生じて、リレー接点C1,O2の一方が
閉じ、時計方向又は反時計方向に電流が流れて前記モー
タMを回転させ、前記制御弁Eの弁開度を制御するので
あり、発生器への入熱量が一定で、冷水、温水の負荷が
増大し前記能力制御弁A、Bが開方向に動作するとき、
前記放熱量制御弁Eは閉方向に制御されて放熱器での放
熱量を少なくするのである。
When the above-mentioned bridge circuit is pressed and the openings of the capacity control valves A and B are controlled to close, the auxiliary potentiometer D1. Wiper a of D2 operates in the open or close direction,
Further, when the strain force of the generator detected by the pressure detector C fluctuates, the wiper a of the resistor C1 operates to the high pressure side or the low pressure side in accordance with the pressure fluctuation. Accordingly, the terminal R1-Wl s B2 # R
2s R2 # W2s R3 ° The resistance between R3 increases and decreases, and the bridge circuit G becomes unbalanced, and the electromagnet M1. M2
A difference occurs in the electromagnetic force between the relay contacts C1 and O2, which causes a current to flow clockwise or counterclockwise to rotate the motor M and control the opening of the control valve E. , when the amount of heat input to the generator is constant and the load of cold water and hot water increases and the capacity control valves A and B operate in the opening direction,
The heat radiation amount control valve E is controlled in the closing direction to reduce the amount of heat radiation from the radiator.

また冷水、温水の負荷が一定で、発生器への入熱量が増
大し抵抗器c1のワイパーaが高圧側に動作するとき、
前記放熱量制御弁Eは開方向に制御され放熱器での放熱
量を大きくするのである。
Also, when the load of cold water and hot water is constant and the amount of heat input to the generator increases and wiper a of resistor c1 operates to the high pressure side,
The heat radiation amount control valve E is controlled in the opening direction to increase the amount of heat radiation from the radiator.

今前記端子B2.W2.B′、W′間の抵抗を100、
tた端子B1. Wl、 B3. R3間の抵抗を20
0とし、冷却能力制御弁Aの弁開度をX%。
Now said terminal B2. W2. The resistance between B' and W' is 100,
Terminal B1. Wl, B3. The resistance between R3 is 20
0, and the valve opening of cooling capacity control valve A is set to X%.

加温能力制御弁Bの弁開度をYaI)、最少入熱量に対
し、入熱量が増加するとき圧力検出器Cが検出する圧力
増加の割合をP%、放熱量制御弁Eの弁開度をZ%とす
ると、抵抗器C1の端子R1,R1間の抵抗r1、補助
ポテンショメータD1.D2の端子B2. R2間の抵
抗r3、端子R2,R2間の抵抗r4、フィードバック
ポテンショメータFの端子B/ 、 R7間の抵抗r5
、端子R’、W’の抵抗r6は次の通りとなる。
The valve opening degree of the heating capacity control valve B is YaI), the ratio of pressure increase detected by the pressure detector C when the heat input increases with respect to the minimum heat input amount is P%, and the valve opening degree of the heat release amount control valve E is Z%, the resistance r1 between the terminals R1 and R1 of the resistor C1, the auxiliary potentiometer D1. Terminal B2 of D2. Resistance r3 between R2, resistance r4 between terminals R2 and R2, resistance r5 between terminals B/ and R7 of feedback potentiometer F
, the resistance r6 of the terminals R' and W' is as follows.

ここで前記ブリッジ回路Gが平衡状態を保つのは、前記
ブリッジ回路Gにおける端子R2から端子B2゜Wl、
R1,B 、B’を経てR′に至る間の合成抵抗r2+
r1+r5と、端子R2から端子W2.B3゜R3,R
3,W、W’を経てR′に至る間の合成抵抗r3+r4
+r6とが等しいことである。
Here, the bridge circuit G maintains a balanced state from the terminal R2 to the terminal B2°Wl in the bridge circuit G.
Combined resistance r2+ through R1, B, and B' to R'
r1+r5, and from terminal R2 to terminal W2. B3゜R3,R
3. Combined resistance r3+r4 through W and W' to R'
+r6 is equal.

従って、で平衡することになり、放熱量制御弁の弁開度
は発生器に入熱する全排熱量(100+P)%から、冷
水負荷及び温水負荷により設定される前記冷却能力制御
弁Aの弁開度X%と前記加温能力制御弁Bの弁開度Y%
との合計を引いた開度に制御されることになる。
Therefore, the valve opening degree of the heat release amount control valve is determined from the total amount of waste heat input to the generator (100+P)%, and the valve opening degree of the cooling capacity control valve A is set based on the chilled water load and the hot water load. Opening degree X% and valve opening degree Y% of the heating capacity control valve B
The opening degree will be controlled by subtracting the sum of .

以上の説明は、冷水及び温水を同時に供給するものであ
るが、切換えにより冷水または温水のいずれか一方を供
給できるようにするものを第5図及び第6図に基づいて
説明する。
In the above description, cold water and hot water are supplied simultaneously, but a system that can supply either cold water or hot water by switching will be explained based on FIGS. 5 and 6.

即ち前記放熱量制御弁の弁開度制御方式は、第5図のご
とく冷水測温体H及び温水測温体Iの各出力側を冷暖房
切換スイッチSW1の冷房及び暖房用接点に接続すると
共に、切換スイッチSW1の供通接点を、前記測温体H
またはIにより検出する冷水または温水の各負荷に対し
前記能力制御弁またはBのモジュトロールモータを制御
するコントローラNを介して、前記切換スイッチSw1
と連動する切換スイッチSW1の共通接点に接続する。
That is, the valve opening degree control method of the heat release amount control valve is as shown in FIG. The current contact of the changeover switch SW1 is connected to the temperature measuring element H.
or the changeover switch Sw1 via the controller N that controls the capacity control valve or the modutrol motor B for each load of cold water or hot water detected by I.
Connect to the common contact of the changeover switch SW1 that is linked to the switch SW1.

そしてこの切換スイッチSW1の冷房及び暖房用接点を
前記能力制御弁A及びBに接続し、これら能力制御弁A
またはBを動作させるモジュトロールモータの補助ポテ
ンショメータD1及びD2を、前記切換スイッチSW1
.SW2と連通する切換スイッチSW3の冷房及び暖房
用接点に接続して、前記各切換スイッチSW1.SW2
.SW3の切換えにより、切換側の前記補助ポテンショ
メータD1またはD2と、抵抗器C1と、放熱量制御弁
Eを動作させるモジュトロールモータのフィードバック
ポテンショメータFとを組合せてブリッジ回路T1を形
威し、前記放熱量制御弁Eを、前記入熱量の増加分に見
合う弁開度で、かつ前記能力制御弁AまたはBの弁開度
に対し所定関係の弁開度になるごとくするのである。
Then, the cooling and heating contacts of this changeover switch SW1 are connected to the capacity control valves A and B, and these capacity control valves A and B are connected to each other.
Alternatively, the auxiliary potentiometers D1 and D2 of the modutrol motor that operates B are connected to the changeover switch SW1.
.. The cooling and heating contacts of the changeover switch SW3 communicating with SW2 are connected to the respective changeover switches SW1. SW2
.. By switching SW3, a bridge circuit T1 is formed by combining the auxiliary potentiometer D1 or D2 on the switching side, the resistor C1, and the feedback potentiometer F of the Modutrol motor that operates the heat radiation amount control valve E. The amount of heat control valve E is set to have a valve opening that corresponds to the increase in the amount of heat input and has a predetermined relationship with the valve opening of the capacity control valve A or B.

即ち前記切換スイッチSW1.SW2.SW3を冷房用
側に切換えて冷水のみを供給するようにした場合の熱収
支は出熱量と入熱量とが等しいから、Z+Q=100+
P となり、放熱器による放熱量2は、Q=2Xの関係があ
るので、 Z= (100+P )−X となる。
That is, the changeover switch SW1. SW2. The heat balance when SW3 is switched to the cooling side and only cold water is supplied is that the heat output and heat input are equal, so Z+Q=100+
P, and the heat radiation amount 2 by the radiator has the relationship Q=2X, so Z=(100+P)-X.

即ち放熱器での放熱量は冷水負荷を発生器に入熱する排
熱(100+P)から減算した値で制御すればよいこと
になる。
That is, the amount of heat radiated by the radiator can be controlled by the value obtained by subtracting the cold water load from the exhaust heat (100+P) input to the generator.

また前記切換スイッチSW1.SW2.SW3を暖房側
に切換えて温水のみを供給するようにした場合の熱収支
は、 Z+Y= 100+P となり、Z= (100+P )−Yとなる。
Further, the changeover switch SW1. SW2. The heat balance when SW3 is switched to the heating side to supply only hot water is Z+Y=100+P, and Z=(100+P)-Y.

即ち放熱器での放熱量は温水負荷を発生器に入熱する排
熱(100+P)から減算した値で制御すればよいこと
になる。
That is, the amount of heat radiated by the radiator can be controlled by the value obtained by subtracting the hot water load from the exhaust heat (100+P) input to the generator.

しかして第5図に示した前記ブリッジ回路G1を第6図
のごとく以上の関係式を満足できるように形成するので
ある。
Therefore, the bridge circuit G1 shown in FIG. 5 is formed so as to satisfy the above relational expression as shown in FIG.

即ち、各切換スイッチSW1.SW2.SW3の切換え
により冷水を供給する時補助ポテンショメータD1がブ
リッジ回路G1を構成することとなるのであって、補助
ポテンショ、メータD1のワイパーaに連通する端子R
4と34間の抵抗r3と、抵抗器C1の端子R1,W1
間の抵抗r1 とフィードバックポテンンヨメータFの
端子B/ 、 R7間の抵抗r、とを直列に接続すると
共に、補助ポテンショメータD0の端子R4,W4間の
抵抗r7とフィードバックポテンショメータFの端子R
’、W’間の抵抗r8とを直列に接続し、前記端子R4
゜R′間に電源りを接続するごとくするのである。
That is, each changeover switch SW1. SW2. When supplying cold water by switching SW3, the auxiliary potentiometer D1 forms a bridge circuit G1, and the auxiliary potentiometer is connected to the terminal R connected to the wiper a of the meter D1.
Resistor r3 between 4 and 34 and terminals R1, W1 of resistor C1
The resistance r1 between terminals B/ and R7 of feedback potentiometer F are connected in series, and the resistance r7 between terminals R4 and W4 of auxiliary potentiometer D0 and terminal R of feedback potentiometer F are connected in series.
', W' are connected in series with the resistor r8, and the terminal R4
It is as if a power supply is connected between ゜R'.

そして補助ポテンショメータD1 の端子B4゜W4及
びフィードバックポテンショメータFの端子B′、W′
間の抵抗を100.fた抵抗器C1の端子B1.W1間
の抵抗を200とし、冷却能力制御弁Bの弁開度をX%
、圧力検出器Cが検出する圧力増加の割合をP%、放熱
量制御弁Eの弁開度を1とすると、前記抵抗r1h r
5* r6* r7mr8はそれぞれ次の通りとなる。
Terminal B4゜W4 of auxiliary potentiometer D1 and terminals B' and W' of feedback potentiometer F.
The resistance between 100. terminal B1 of resistor C1. The resistance between W1 is 200, and the opening degree of cooling capacity control valve B is X%.
, the rate of pressure increase detected by the pressure detector C is P%, and the valve opening degree of the heat release control valve E is 1, then the resistance r1h r
5*r6*r7mr8 are respectively as follows.

ここで前記ブリッジ回路Gが平衡状態を保つのであるの
で、 (100−X)+(2P)+(100−Z)=(X)+
(Z )即ち、 Z= (100+P ) −X の関係が成立することであり、放熱量制御弁Eの弁開度
は発生器に入熱する全排熱量(100+P)係から、冷
水負荷により設定される前記冷却能力制御弁Aの弁開度
Yqbを引いた開度に制御されることになる。
Here, since the bridge circuit G maintains a balanced state, (100-X)+(2P)+(100-Z)=(X)+
(Z) That is, the relationship Z = (100+P) -X is established, and the valve opening degree of the heat release control valve E is set based on the total amount of waste heat (100+P) entering the generator, and the chilled water load. The opening of the cooling capacity control valve A is subtracted by the opening Yqb of the cooling capacity control valve A.

又各切換スイッチSW1.SW2.SW3の切換により
温水を供給する時補助ポテンショメータD2力やブリッ
ジ回路G1 を構成することとなるのであって、冷水を
供給する場合と相違する点は、冷却能力制御弁Aの弁開
度X%の代りに加温能力制御弁Bの開度Y%を用いるご
とくするものである。
In addition, each changeover switch SW1. SW2. When supplying hot water by switching SW3, the auxiliary potentiometer D2 force and the bridge circuit G1 are configured.The difference from when supplying cold water is that the valve opening X% of the cooling capacity control valve A is Instead, the opening degree Y% of the heating capacity control valve B is used.

即ち の関係が取立することであり、放熱量制御弁の弁開度は
発生器に入熱する全排熱量(100+P)係から温水負
荷により設定される前記加温能力制御弁Bの弁開度Y%
を引いた開度に制御されることになる。
That is, the relationship is established, and the valve opening degree of the heat radiation amount control valve is the valve opening degree of the heating capacity control valve B set by the hot water load from the total amount of exhaust heat input to the generator (100+P). Y%
The opening will be controlled by subtracting the opening.

また冷水のみを供給する場合には、第5図にかいて切換
えスイッチSW1.SW2.SW3、温水測温体■及び
加温能力制御弁Bを取り除けば良いのであって、前記ブ
リッジ回路は第6図と同じに構成すれば良いのである。
In addition, when only cold water is supplied, selector switch SW1. SW2. It is sufficient to remove SW3, hot water temperature measuring element (3), and heating capacity control valve B, and the bridge circuit may be constructed in the same manner as shown in FIG. 6.

以上説明したものは、何れも冷却能力制御弁Aを用いた
ものであるが、この冷却能力制御弁Aは必らずしも必要
でない。
Although the systems described above all use the cooling capacity control valve A, this cooling capacity control valve A is not necessarily required.

冷却能力制御弁Aを設けない場合は、冷水負荷を検出す
る冷水負荷検出器を形成するのであって、この負荷検出
器は補助ポテンショメータD1 を備えたモジュトロー
ルモータにより形成するのであり、前記ブリッジ回路G
、G1は冷却能力制御弁Aを用いる場合と同様である。
If the cooling capacity control valve A is not provided, a chilled water load detector for detecting the chilled water load is formed, and this load detector is formed by a modutrol motor equipped with an auxiliary potentiometer D1, and the bridge circuit G
, G1 are the same as when using the cooling capacity control valve A.

次に本発明吸収式冷凍装置の冷水と温水を同時に供給で
きるものの実施例を第7図に基づいて説明する。
Next, an embodiment of the absorption refrigerating apparatus of the present invention capable of simultaneously supplying cold water and hot water will be described with reference to FIG.

第7図に示した冷凍装置は、二重効用吸収式冷凍装置で
あって、高温発生器1に排ガス等の排熱熱源に連なる排
熱管2を接続し、排熱熱源からの排熱を規制することな
くその1\入熱するごとく威すと共に、この高温発生器
1には、前記排熱が冷温水負荷に対し過剰のとき放熱す
るための放熱器3を接続すると共に、前記高温発生器1
に入熱する最少入熱量に対し、入熱量が増加するときの
圧力増加を検出する前記圧力検出器Cを設けるのである
。
The refrigeration system shown in Fig. 7 is a double-effect absorption refrigeration system, in which a high-temperature generator 1 is connected to a heat exhaust pipe 2 connected to a waste heat heat source such as exhaust gas, and the waste heat from the waste heat heat source is regulated. At the same time, a radiator 3 is connected to the high temperature generator 1 for dissipating heat when the waste heat is excessive with respect to the cold/hot water load. 1
The pressure detector C is provided to detect an increase in pressure when the amount of heat input increases with respect to the minimum amount of heat input.

前記放熱器3には、冷却水管12と連通ずる熱交換チュ
ーブを配設していて、高温発生器1からの高温の冷媒蒸
気と熱交換するごとくなって釦り、前記放熱器3と高温
発生器1とを結ぶドレン管4に、放熱量を制御する前記
放熱量制御弁Eを設けるのである。
The radiator 3 is provided with a heat exchange tube that communicates with the cooling water pipe 12, and the heat exchanger tube exchanges heat with the high-temperature refrigerant vapor from the high-temperature generator 1. The drain pipe 4 connecting to the container 1 is provided with the heat radiation amount control valve E for controlling the amount of heat radiation.

この制御弁Eは、前記放熱器3に釦ける排熱の放熱量を
調節して前記発生器1の圧力が所定値を越えないように
制御するもので、前記制御弁Eを閉じることにより、放
熱器3内にドレンを貯溜し、とのドレンにより前記熱交
換チューブを埋没させて、放熱面積を小さくするもので
、この制御弁Eの弁開度を調節することにより放熱量を
制御できる。
This control valve E controls the pressure of the generator 1 so as not to exceed a predetermined value by adjusting the amount of heat released from the heat radiator 3. By closing the control valve E, Drain is stored in the radiator 3, and the heat exchange tube is buried by the drain to reduce the heat radiation area.By adjusting the opening degree of the control valve E, the amount of heat radiation can be controlled.

又冷水の冷却能力を制御する冷却能力制御弁Aは溶液管
、第7図に示した実施例では吸収器5と前記高温発生器
1とを結ぶ溶液管6から分岐し、吸収器5に側路するバ
イパス管6′に介装し、溶液循環量を調節するのであり
、また温水の加温能力を制御する加温能力制御弁Bは、
前記高温発生器1に接続する温水熱交換器7のドレン管
8に介装するのである。
The cooling capacity control valve A that controls the cooling capacity of the cold water is branched from a solution pipe, in the embodiment shown in FIG. 7, a solution pipe 6 connecting the absorber 5 and the high temperature generator 1, The heating capacity control valve B, which is installed in the bypass pipe 6' passing through the water, adjusts the amount of solution circulation, and also controls the heating capacity of hot water.
It is installed in the drain pipe 8 of the hot water heat exchanger 7 connected to the high temperature generator 1.

尚前記冷却能力制御弁Aは、低温発生器9から凝縮器1
0に至る冷媒配管11の途中に介装し、凝縮器10に流
れる冷媒量を調節するごとく威してもよい。
Note that the cooling capacity control valve A is connected from the low temperature generator 9 to the condenser 1.
The refrigerant pipe 11 may be interposed in the middle of the refrigerant pipe 11 leading to zero, and the amount of refrigerant flowing into the condenser 10 may be adjusted.

また前記放熱量制御弁E及び加温能力制御弁Bは、三方
弁を用いてもよい。
Furthermore, the heat release amount control valve E and the heating capacity control valve B may be three-way valves.

この場合には第7図のごとく前記冷却水管12の入口側
と出口側との間にバイパス管13を、捷た前記温水熱交
換器7に連結する温水管14の入口側と出口側との間に
バイパス管15を設けて、これらバイパス管13゜13
の前記冷却水管12及び温水管14との合流点に三方弁
から戒る前記放熱量制御弁E及び加温能力制御弁Bを介
装するのである。
In this case, as shown in FIG. 7, a bypass pipe 13 is provided between the inlet side and the outlet side of the cooling water pipe 12, and a bypass pipe 13 is provided between the inlet side and the outlet side of the hot water pipe 14 connected to the disconnected hot water heat exchanger 7. A bypass pipe 15 is provided between these bypass pipes 13゜13.
The heat radiation amount control valve E and the heating capacity control valve B, which are controlled from the three-way valve, are interposed at the junction of the cooling water pipe 12 and the hot water pipe 14.

又第7図に釦いて16は蒸発器で、該蒸発器16には冷
水管17が配管されてかり、前記凝縮器10で液化した
冷媒を、冷媒ポンプ18で圧送し、散布ノズル16aか
ら前記冷水管17に散布し、管内を流れる被冷却水から
蒸発潜熱を奪って冷却し、冷水を形成するのである。
Further, in FIG. 7, 16 is an evaporator, and a cold water pipe 17 is connected to the evaporator 16. The refrigerant liquefied in the condenser 10 is pumped by a refrigerant pump 18, and is discharged from the spray nozzle 16a. It is sprayed on the cold water pipe 17, and the latent heat of vaporization is taken away from the water to be cooled flowing inside the pipe to cool it and form cold water.

又19は溶液ポンプ、20は低温熱交換器、21は高温
熱交換器である。
Further, 19 is a solution pump, 20 is a low temperature heat exchanger, and 21 is a high temperature heat exchanger.

しかして以上の構成にかいて、冷媒は吸収器5で溶液に
吸収され、溶液ポンプ19の駆動により溶液管6を介し
、前記低温熱交換器20、高温熱交換器21を経て高温
発生器1に入り、此処で前記排熱により加熱され、冷媒
蒸気となって溶液から分離し、前記冷媒配管11を流れ
、低温発生器9で分離された冷媒と共に凝縮器10に入
り、冷却水管12の冷却水と熱交換して凝縮し、そして
凝縮した液冷媒は蒸発器16に入り、冷水管17を流れ
る被冷却水から熱を奪って蒸発し、再び吸収器5で溶液
に吸収される冷凍サイクルを繰返すのである。
According to the above configuration, the refrigerant is absorbed into the solution in the absorber 5, and is driven by the solution pump 19 to pass through the solution pipe 6, the low temperature heat exchanger 20, the high temperature heat exchanger 21, and the high temperature generator 1. Here, it is heated by the exhaust heat, becomes refrigerant vapor, separates from the solution, flows through the refrigerant pipe 11, enters the condenser 10 together with the refrigerant separated by the low temperature generator 9, and cools the cooling water pipe 12. The liquid refrigerant exchanges heat with water, condenses, enters the evaporator 16, takes heat from the cooled water flowing through the cold water pipe 17, evaporates, and is absorbed into the solution again in the absorber 5, starting the refrigeration cycle. Repeat.

しかして以上の如きサイクルに釦ける前記蒸発器16で
の冷媒の蒸発により冷水を作り、前記高温発生器1で発
生した高温の冷媒蒸気を温水熱交換器7に導き、温水管
14を流れる被加温水を加熱して温水を作るのである。
In the cycle described above, cold water is produced by evaporating the refrigerant in the evaporator 16, and the high temperature refrigerant vapor generated in the high temperature generator 1 is led to the hot water heat exchanger 7, and the hot water flowing through the hot water pipe 14 is heated. It heats warm water to make hot water.

そして以上の運転に釦いて、高温発生器1に入熱する排
熱量が変動し、高温発生器1内の圧力が変動すると、こ
れを検出する圧力検出器Cを介して前記変動に応じて放
熱量制御弁Eが操作され、放熱器3の放熱能力を自動的
に調節するのである。
When the above operation is pressed, the amount of waste heat input to the high temperature generator 1 fluctuates, and the pressure inside the high temperature generator 1 fluctuates. The heat quantity control valve E is operated to automatically adjust the heat dissipation capacity of the radiator 3.

また冷水負荷が変動すると、これを検出する測温体H、
コントローラーJを介して前記変動に応じて冷却能力制
御弁Aが操作され、冷却能力を自動的に調整するのであ
り温水負荷が変動すれば、これを検出する測温体重、コ
ントローラーKを介して、前記変動に応じて加温能力制
御弁Bが操作され、加温能力を自動的に調節するのであ
る。
In addition, when the cold water load fluctuates, a temperature measuring element H detects this.
The cooling capacity control valve A is operated according to the fluctuations via the controller J, and the cooling capacity is automatically adjusted. The heating capacity control valve B is operated in accordance with the fluctuation, and the heating capacity is automatically adjusted.

そして高温発生器1に入熱する排熱量あるいは各負荷の
変動により、以上の如く圧力検出器Cの抵抗値が調節さ
れると共に能力制御弁A、Bの弁開度が調節されると、
前記したブリッジ回路Gが不平衡となり圧力検出器Cの
抵抗値及びこれら能力制御弁A、Bの弁開度に見合う一
定割合の弁開度で、前記放熱量制御弁Eが制御され、発
生器1の圧力を所定の安全値に保持できて、前記冷水及
び温水を、前記発生器1への入熱量及び前記負荷の変動
に拘わらず、一定温度に維持できるのである。
Then, when the resistance value of the pressure detector C is adjusted as described above and the valve opening degrees of the capacity control valves A and B are adjusted according to the amount of exhaust heat input to the high temperature generator 1 or fluctuations in each load, as described above,
When the bridge circuit G described above becomes unbalanced, the heat radiation amount control valve E is controlled at a valve opening degree of a certain proportion corresponding to the resistance value of the pressure detector C and the valve opening degrees of these capacity control valves A and B, and the generator 1 can be maintained at a predetermined safe value, and the cold water and hot water can be maintained at a constant temperature regardless of the amount of heat input to the generator 1 and fluctuations in the load.

即ち前記発生器1への入熱量が多くなって発生器1内の
圧力が上昇し、前記圧力検出器Cの抵抗出力が犬きくな
れば、前記放熱量制御弁Eの弁開度は大きくなるのであ
って、その弁開度は前記能力制御弁A、Bの弁開度合計
を、発生器1に入熱する全排熱量から減算した値に制御
される。
That is, if the amount of heat input to the generator 1 increases, the pressure inside the generator 1 increases, and the resistance output of the pressure detector C becomes sharper, the opening degree of the heat release amount control valve E increases. The valve opening degree is controlled to a value obtained by subtracting the total valve opening degree of the capacity control valves A and B from the total amount of exhaust heat input to the generator 1.

つ1り入熱量の増加により放熱量を増加し、入熱量の減
少により放熱量を減少するのである。
The amount of heat dissipated increases as the amount of heat input increases, and the amount of heat dissipated decreases as the amount of heat input decreases.

又前記発生器1への入熱量が一定で、負荷が多くなり前
記能力制御弁A、Bの弁開度が犬きくなれば、前記放熱
量制御弁Eの弁開度は小さくなるのであって、その弁開
度は前記能力制御弁A、 Bの弁開度合計を、発生器1
に入熱する全排熱量から減算した値に制御される。
Further, if the amount of heat input to the generator 1 is constant, and the load increases and the opening degrees of the capacity control valves A and B become sharper, the opening degree of the heat release amount control valve E becomes smaller. , the valve opening is the sum of the valve openings of the capacity control valves A and B, and the generator 1
Controlled to a value subtracted from the total amount of waste heat input.

つ1り負荷の増加ににより放熱量を減少し、最大負荷で
放熱量を零とするものであり、負荷の減少により放熱量
を増加し、最小負荷が最大即ち100%放熱とするもの
である。
The amount of heat dissipated is reduced as the load increases, and the amount of heat dissipated becomes zero at the maximum load.The amount of heat dissipated is increased as the load decreases, and the amount of heat dissipated is the maximum at the minimum load, that is, 100% heat dissipation. .

尚前記コントローラーJ、 Kは、前記冷水管17、温
水管14の出口側に測温体H,Iを設げて、冷水及び温
水出口温度を検出して作動するごとく威したものについ
て説明したが、その他蒸発器16内の温度や温水熱交換
器7内の温度などを検出してもよいのであって、要する
に負荷の変動を検知して作動するごとく威すのである。
It should be noted that the controllers J and K were explained as having temperature measuring elements H and I installed on the outlet sides of the cold water pipe 17 and the hot water pipe 14 to detect the cold water and hot water outlet temperatures and operate. , the temperature inside the evaporator 16, the temperature inside the hot water heat exchanger 7, etc. may also be detected, in other words, the change in load is detected and activated.

筐た冷水または温水を切換えにより供給できるようにす
るには、前記第5図の制御方式を用い、第9図のごとく
構成して放熱量制御弁Eの制御を行なうととくするので
ある。
In order to be able to supply cold water or hot water by switching, the control system shown in FIG. 5 is used, and the heat radiation amount control valve E is controlled by constructing the system as shown in FIG. 9.

即ち前記切換スイッチSW1.SW2.SW3を冷房側
に切換えて冷水のみを供給するごとくしている時、冷水
負荷が変動すると、これを検出する測温体H、コントロ
ーラーNを介して前記変動に応じて冷却能力制御弁Aが
操作されて弁開度が前記X%となり、冷却能力を自動的
に調整するのであり、冷水温度を一定値に維持できるの
である。
That is, the changeover switch SW1. SW2. When SW3 is switched to the cooling side to supply only chilled water, if the chilled water load fluctuates, the cooling capacity control valve A is operated according to the fluctuation via the temperature sensor H and controller N that detects this. As a result, the valve opening becomes the above-mentioned X%, and the cooling capacity is automatically adjusted, making it possible to maintain the cold water temperature at a constant value.

そしてこの運転時、高温発生器1に入熱する排熱量が変
動し、高温発生器1内の圧力が前記P%変動すると、こ
のP%の変動を検出する圧力検出器Cを介して前記変動
に応じて放熱量制御弁Eが操作されて弁開度Zが(1o
O+P)−X%となり放熱器3の放熱能力を自動的に調
節するのである。
During this operation, when the amount of waste heat input to the high temperature generator 1 fluctuates and the pressure inside the high temperature generator 1 fluctuates by the above P%, the fluctuation is detected via the pressure detector C which detects the fluctuation of this P%. The heat release amount control valve E is operated in accordance with
O+P)-X%, and the heat radiation capacity of the heat sink 3 is automatically adjusted.

又前記切換スイッチSW工、sw2.sw3を暖房側に
切換えて温水のみを供給するごとくしている時、温水負
荷が変動すると、これを検出する測温体■、コントロー
ラーNを介して前記変動に応じて加温能力制御弁Bが操
作されて弁開度が前記Y%となり、加温能力を自動的に
調整するのであり、温水温度を一定値に維持できるので
ある。
Moreover, the said changeover switch SW work, sw2. When sw3 is switched to the heating side to supply only hot water, if the hot water load fluctuates, the heating capacity control valve B is activated in response to the fluctuation via the temperature sensing element ■, which detects this, and the controller N. When operated, the valve opening becomes Y%, and the heating capacity is automatically adjusted, making it possible to maintain the hot water temperature at a constant value.

そしてこの運転時、高温発生器1に入熱する排熱量が変
動し、高温発生器1内の圧力が前記P%変動すると、こ
のP%の変動を検出する圧力検出器Cを介して前記変動
に応じて放熱量制御弁Eが操作されて弁開度2が(’1
00+P )−Y%となり、放熱器3の放熱能力を自動
的に調節するのである。
During this operation, when the amount of waste heat input to the high temperature generator 1 fluctuates and the pressure inside the high temperature generator 1 fluctuates by the above P%, the fluctuation is detected via the pressure detector C which detects the fluctuation of this P%. The heat radiation amount control valve E is operated in accordance with
00+P)-Y%, and the heat dissipation capacity of the radiator 3 is automatically adjusted.

また冷水のみを供給するように構成するには、第9図の
実施例に釦いて、温水熱交換器7、加温能力制御弁B、
切換スイッチSW1.SW2.Sw3及び温水測温体■
を取り除けば良いのである。
In addition, in order to configure the system to supply only cold water, click the embodiment shown in FIG.
Selector switch SW1. SW2. Sw3 and hot water thermometer ■
All you have to do is remove it.

また第7図、第9図の実施例では、冷却能力制御弁Aを
設けたが、冷却能力は該冷却能力を発揮させるための発
生器入熱量が放熱量制御弁Eにより制御されるため、前
記冷却能力制御弁Aは必ずしも必要ではない。
In addition, in the embodiments shown in FIGS. 7 and 9, a cooling capacity control valve A is provided, but since the amount of heat input to the generator for exerting the cooling capacity is controlled by the heat radiation amount control valve E, The cooling capacity control valve A is not necessarily required.

この場合は、冷水負荷を検出する冷水負荷検出器を形成
するのであって、この負荷検出器は、前述した如く、補
助ポテンショメータD1を備えたモジュトロールモータ
により形成するのである。
In this case, a chilled water load detector for detecting the chilled water load is formed, and this load detector is formed by a modutrol motor equipped with an auxiliary potentiometer D1, as described above.

以上の如く本発明によれば、排熱熱源側からの排熱を規
制することなくその1\発生器に導入し、過剰分は放熱
器で放熱するので、排熱熱源側に悪影響を及ぼすことは
全くないのであり、しかも前記過剰分は圧力検出器によ
り発生器への最少入熱量に対し入熱量が増加するときの
圧力増加を検出することにより常に確実に検出できて、
放熱器から放熱できるので、発生器の圧力を常に正常値
に保持できると共に、溶液の異常濃縮が全くなく安全な
運転を行なえるのである。
As described above, according to the present invention, waste heat from the waste heat heat source is introduced into the generator without being regulated, and excess heat is radiated by the radiator, so that there is no adverse effect on the waste heat heat source. Moreover, the excess amount can always be detected reliably by using a pressure detector to detect the pressure increase when the amount of heat input increases relative to the minimum amount of heat input to the generator.
Since heat can be radiated from the radiator, the pressure in the generator can always be maintained at a normal value, and there is no abnormal concentration of the solution, allowing safe operation.

即ち発生器への排熱の入熱量如何を問わず、冷水と温水
との少くとも一方、詳しくは前記冷水と温水との両方又
は切換えにより前記冷水と温水とのいずれか一方、又は
冷水のみのそれぞれの各供給水をいずれの場合でも、常
に過不足なく供給するごとくできるのである。
That is, regardless of the amount of heat input of waste heat to the generator, at least one of cold water and hot water, more specifically, both the cold water and hot water, or one of the cold water and hot water by switching, or only cold water. In any case, it is possible to always supply just enough water.

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

第1図は本発明装置の運転制御方式の一例を示す説明図
、第2図はブリッジ回路図、第3図及び第4図は圧力検
出器の実施例を示す説明図、第5図は本発明装置の運転
制御方式の他の一例を示す説明図、第6図はそのブリッ
ジ回路図、第7図は本発明装置の一実施例を示す冷凍サ
イクル図、第8図は別の実施例を示す一部分の冷凍サイ
クル図、第9図は本発明装置の他の実施例を示す冷凍サ
イクル図である。 1・・・発生器、E・・・放熱量制御弁、3・・・放熱
器、A・・・冷却能力制御弁、B・・・加温能力制御弁
、C・・・圧力検出器。
Fig. 1 is an explanatory diagram showing an example of the operation control system of the device of the present invention, Fig. 2 is a bridge circuit diagram, Figs. 3 and 4 are explanatory diagrams showing an embodiment of the pressure detector, and Fig. An explanatory diagram showing another example of the operation control system of the inventive device, FIG. 6 is a bridge circuit diagram thereof, FIG. 7 is a refrigeration cycle diagram showing one embodiment of the inventive device, and FIG. 8 is a diagram showing another embodiment. A partial refrigeration cycle diagram shown in FIG. 9 is a refrigeration cycle diagram showing another embodiment of the apparatus of the present invention. DESCRIPTION OF SYMBOLS 1... Generator, E... Heat radiation amount control valve, 3... Heat radiator, A... Cooling capacity control valve, B... Heating capacity control valve, C... Pressure detector.

Claims (1)

【特許請求の範囲】 1 発生器に排熱熱源を接続し、蒸発器に冷水負荷を接
続し、前記排熱を利用して冷水を供給できるようにした
吸収式冷凍装置であって、前記発生器に、該発生器に入
熱する排熱の放熱器を接続して、この接続回路にモジュ
トロールモータにより動作する放熱量制御弁を介装する
と共に、前記冷水負荷を検出し、該負荷に応じた制御信
号を発信するととくした負荷検出器を設ける一方、発生
器に入熱する最少入熱量に対し入熱量が増加するときの
圧力増加を検出する圧力検出器を設けて、圧力増加に応
じた制御信号を発信するごとく威し、前記放熱量制御弁
のモジュトロールモータに、前記発生器への最少入熱量
と入熱量の増加分とを加算した制御信号から、前記負荷
検出器に釦ける負荷に応じた制御信号を減算した出力信
号を与え、前記放熱量制御弁の弁開度を制御するごとく
したことを特徴とする排熱利用の吸収式冷凍装置。 2 発生器に排熱熱源を接続し、蒸発器に冷水負荷を、
また前記発生器に接続する温水熱交換器に温水負荷をそ
れぞれ接続して、冷房と暖房とを切換運転可能とした吸
収式冷凍装置であって、前記発生器に、該発生器に入熱
する排熱の放熱器を接続して、この接続回路にモジュト
ロールモータにより動作する放熱量制御弁を介装すると
共に、前記温水熱交換器で作る温水の加温能力制御弁を
設けて、該能力制御弁を補助ポテンショメータを備エタ
モジュトロールモータにより動作させ弁開度に応じた制
御信号を発信するごとく威す一方、冷水負荷を検出し負
荷に応じた制御信号を発信する冷水負荷検出器を設ける
と共に、前記発生器に入熱する最少入熱量に対し入熱量
が増加したときの圧力増加を検出する圧力検出器を設け
て、圧力増加に応じた制御信号を発信するごとく威し、
前記放熱量制御弁のモジュトロールモータに前記発信器
への最少入熱量と入熱量の増加分とを加算した制御信号
から、前記能力制御弁と、冷水負荷検出器との一方から
発信する制御信号を減算した出力信号を与え、前記放熱
量制御弁の弁開度を制御するごとくしたことを特徴とす
る排熱利用の吸収式3 発生器に排熱熱源を接続し、蒸
発器に冷水負荷を、また前記発生器に接続する温水熱交
換器に温水負荷をそれぞれ接続して、冷房と暖房とを同
時運転可能とした吸収式冷凍装置であって、前記発生器
に、該発生器に入熱する排熱の放熱器を接続して、この
接続回路にモジュトロールモータにより動作する放熱量
制御弁を介装すると共に、前記温水熱交換器で作る温水
の加温能力制御弁を設けて、能力制御弁を補助ポテンシ
ョメータを備えたモジュトロールモータにより動作させ
、弁Mliに応じた制御信号を発信するごとく威す一方
、冷水負荷を検出し、負荷に応じた制御信号を発信する
冷水負荷検出器と、前記発生器に入熱する最少入熱量に
対し入熱量が増加したときの圧力増加を検出し、圧力増
加に応じた制御信号を発信する圧力検出器とを、それぞ
れ設けて、前記放熱量制御弁のモジュトロールモータに
、前記発生器への最少入熱量と入熱量の増加分とを加算
した制御信号から前記能力制御弁の弁開度に応じた制御
信号と、冷水負荷検出器からの制御信号との加算合計を
減算した出力信号を与え前記放熱量制御弁の弁開度を制
御するごとくしたことを特徴とする排熱利用の吸収式冷
凍装置。 4 発生器に排熱熱源を接続し、蒸発器に冷水負荷を、
また前記発生器に接続する温水熱交換器に温水負荷をそ
れぞれ接続して、冷房と暖房とを同時運転可能とした吸
収式冷凍装置であって、前記発生器に、該発生器に入熱
する排熱の放熱器を接続して、この接続回路にモジュト
ロールモータにより動作する放熱量制御弁を介装すると
共に、前記蒸発器で作る冷水の冷却能力を制御する冷却
能力制御弁と、前記温水熱交換器で作る温水の加温能力
制御弁とを設けて、これら能力制御弁をそれぞれ補助ポ
テンショメータを備えたモジュトロールモータにより動
作させ弁開度に応じた制御信号を発信するごとく威す一
方、前記発生器に入熱する最少入熱量に対し入熱量が増
加したときの圧力増加を検出する圧力検出器を設けて、
圧力増加に応じた制御信号を発信するごとく戒し、前記
放熱量制御弁のモジュトロールモータに、前記発生器へ
の最少入熱量と入熱量の増加分とを加算した制御信号か
ら、前記冷却能力制御弁と加温能力制御弁との弁開度に
応じた制御信号の加算合計を減算した出力信号を与え、
前記放熱量制御弁の弁開度を制御するごとくしたことを
特徴とする排熱利用の吸収式冷凍装置。
[Scope of Claims] 1. An absorption refrigeration system in which a waste heat heat source is connected to a generator, a chilled water load is connected to an evaporator, and chilled water can be supplied using the waste heat, which A radiator for waste heat that enters the generator is connected to the generator, and a heat radiation amount control valve operated by a Modutrol motor is inserted in this connection circuit, and the chilled water load is detected and the load is A load detector is installed to send a control signal according to the increase in pressure, while a pressure detector is installed to detect the increase in pressure when the amount of heat input increases relative to the minimum amount of heat input into the generator. The module control motor of the heat radiation amount control valve is activated to send a control signal to the load detector based on a control signal that is the sum of the minimum amount of heat input to the generator and the increase in the amount of heat input. An absorption refrigeration system using exhaust heat, characterized in that an output signal obtained by subtracting a control signal according to the load is provided to control the valve opening degree of the heat radiation amount control valve. 2 Connect the exhaust heat heat source to the generator, apply cold water load to the evaporator,
Further, the absorption refrigeration apparatus is capable of switching operation between cooling and heating by connecting hot water loads to hot water heat exchangers connected to the generator, respectively, wherein heat is input to the generator. A heat radiator for waste heat is connected, a heat radiation amount control valve operated by a Modutrol motor is interposed in this connection circuit, and a heating capacity control valve for hot water produced by the hot water heat exchanger is provided to control the heating capacity. The control valve is operated by a motor equipped with an auxiliary potentiometer to send a control signal according to the valve opening degree, and a chilled water load detector is installed to detect the chilled water load and send a control signal according to the load. At the same time, a pressure detector is provided to detect an increase in pressure when the amount of heat input increases with respect to the minimum amount of heat input into the generator, and is configured to transmit a control signal in accordance with the increase in pressure,
A control signal transmitted from one of the capacity control valve and the chilled water load detector based on a control signal obtained by adding the minimum amount of heat input to the transmitter and the increase in the amount of heat input to the modutrol motor of the heat radiation amount control valve. Absorption type 3 for waste heat utilization, characterized in that an output signal obtained by subtracting the amount of heat is given to control the opening degree of the heat release control valve. , and an absorption refrigeration system capable of simultaneously operating cooling and heating by connecting a hot water load to a hot water heat exchanger connected to the generator, wherein heat is input to the generator. A heat radiator for waste heat is connected, and a heat radiation amount control valve operated by a Modutrol motor is interposed in this connection circuit, and a heating capacity control valve for hot water produced by the hot water heat exchanger is provided to increase the capacity. The control valve is actuated by a modutrol motor equipped with an auxiliary potentiometer to transmit a control signal according to the valve Mli, and a chilled water load detector detects the chilled water load and transmits a control signal according to the load. and a pressure detector that detects an increase in pressure when the amount of heat input increases with respect to the minimum amount of heat input into the generator, and transmits a control signal in accordance with the pressure increase, and controls the amount of heat released. A control signal corresponding to the opening degree of the capacity control valve is generated from a control signal obtained by adding the minimum amount of heat input to the generator and an increase in the amount of heat input to the modutrol motor of the valve, and a control signal from the chilled water load detector. An absorption refrigeration system using exhaust heat, characterized in that an output signal obtained by subtracting the sum of additions from a signal is given to control the valve opening degree of the heat radiation amount control valve. 4 Connect the exhaust heat heat source to the generator, apply cold water load to the evaporator,
Further, the absorption refrigeration apparatus is capable of simultaneous operation of cooling and heating by connecting hot water loads to hot water heat exchangers connected to the generator, respectively, wherein heat is input to the generator. A heat radiator for exhaust heat is connected, and a heat radiation amount control valve operated by a Modutrol motor is interposed in this connection circuit, and a cooling capacity control valve for controlling the cooling capacity of the cold water produced by the evaporator; A heating capacity control valve for hot water produced by a heat exchanger is provided, and each of these capacity control valves is operated by a modutrol motor equipped with an auxiliary potentiometer to transmit a control signal according to the valve opening degree, while Providing a pressure detector that detects an increase in pressure when the amount of heat input increases with respect to the minimum amount of heat input into the generator,
A control signal corresponding to the increase in pressure is transmitted, and the cooling capacity is determined by the modutrol motor of the heat radiation amount control valve from a control signal that is the sum of the minimum amount of heat input to the generator and the increase in the amount of heat input. Provides an output signal obtained by subtracting the sum of control signals according to the valve opening degrees of the control valve and the heating capacity control valve,
An absorption refrigeration system using exhaust heat, characterized in that the opening degree of the heat radiation amount control valve is controlled.
JP53156187A 1978-12-14 1978-12-14 Absorption refrigeration equipment that uses waste heat Expired JPS5841423B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53156187A JPS5841423B2 (en) 1978-12-14 1978-12-14 Absorption refrigeration equipment that uses waste heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53156187A JPS5841423B2 (en) 1978-12-14 1978-12-14 Absorption refrigeration equipment that uses waste heat

Publications (2)

Publication Number Publication Date
JPS5582271A JPS5582271A (en) 1980-06-20
JPS5841423B2 true JPS5841423B2 (en) 1983-09-12

Family

ID=15622261

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53156187A Expired JPS5841423B2 (en) 1978-12-14 1978-12-14 Absorption refrigeration equipment that uses waste heat

Country Status (1)

Country Link
JP (1) JPS5841423B2 (en)

Also Published As

Publication number Publication date
JPS5582271A (en) 1980-06-20

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