JPH0754209B2 - Absorption cold / hot water device and its operating method - Google Patents
Absorption cold / hot water device and its operating methodInfo
- Publication number
- JPH0754209B2 JPH0754209B2 JP33023790A JP33023790A JPH0754209B2 JP H0754209 B2 JPH0754209 B2 JP H0754209B2 JP 33023790 A JP33023790 A JP 33023790A JP 33023790 A JP33023790 A JP 33023790A JP H0754209 B2 JPH0754209 B2 JP H0754209B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- heat source
- hot water
- absorber
- cooling water
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 44
- 238000010521 absorption reaction Methods 0.000 title claims description 26
- 238000011017 operating method Methods 0.000 title description 3
- 238000001816 cooling Methods 0.000 claims description 50
- 239000000498 cooling water Substances 0.000 claims description 45
- 238000010438 heat treatment Methods 0.000 claims description 32
- 239000003507 refrigerant Substances 0.000 claims description 28
- 239000006096 absorbing agent Substances 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims 1
- 238000004378 air conditioning Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、吸収冷温水装置に係り、特に排熱などを熱源
として運転する吸収冷温水装置とその運転方法に関す
る。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption cold / hot water apparatus, and more particularly to an absorption cold / hot water apparatus that operates using exhaust heat as a heat source and an operating method thereof.
通常、吸収冷凍機では、冷房運転時は、吸収器、凝縮器
に冷却水を通水し、発生器に熱源となる温水(エンジン
の排出熱など)を通し、蒸発器から、冷房用の冷水を取
り出す。冷房サイクルは通常の吸収冷凍サイクルで運転
される。Normally, in an absorption chiller, during cooling operation, cooling water is passed through the absorber and condenser, hot water (heat discharged from the engine, etc.) that serves as a heat source is passed through the generator, and the evaporator is used to cool the cooling water. Take out. The cooling cycle operates as a normal absorption refrigeration cycle.
一方、暖房の場合は、熱源となる温水と、暖房用温水と
を直接、熱交換させてもよいのであるが、空調用流体
(冷水、温水)の経路が、冷房と暖房とで異なり、切替
弁が必要になる。すなわち、冷水は蒸発器から、温水は
熱源温水と暖房温水との熱交換器から得ることになる。On the other hand, in the case of heating, the hot water serving as a heat source and the hot water for heating may be directly heat-exchanged, but the route of the air conditioning fluid (cool water, hot water) is different between cooling and heating. I need a valve. That is, cold water is obtained from the evaporator, and hot water is obtained from the heat exchanger between the heat source hot water and the heating hot water.
ところで、通常、空調機は一つのコイルを持ち冷房時に
冷水を、暖房時に温水を通す。従って、冷温水機側では
同一の機器(ここでは蒸発器)から冷水、温水を取り出
すのが好ましい。By the way, normally, an air conditioner has one coil and passes cold water during cooling and hot water during heating. Therefore, it is preferable to take out cold water and hot water from the same device (here, the evaporator) on the cold / hot water machine side.
そこで、本発明は、同一の機器から冷水、温水を取り出
すことができ、しかも、冷房運転、暖房運転、冷却塔単
独運転等の運転モードの変換がスムーズにできる吸収冷
温水装置とその運転方法を提供することを目的とする。Therefore, the present invention provides an absorption cold / hot water device and its operating method capable of extracting cold water and hot water from the same device, and capable of smoothly converting operation modes such as cooling operation, heating operation, and independent operation of a cooling tower. The purpose is to provide.
上記目的を達成するために、本発明では、発生器、凝縮
器、吸収器、蒸発器、溶液熱交換器を主要構成機器と
し、これらを溶液配管、冷媒配管で結んでサイクルを構
成する吸収冷温水装置において、発生器への熱源供給通
路に熱源冷却器を設け、また、該熱源冷却器、吸収器及
び凝縮器を冷却するための冷却水を冷却する冷却塔を設
けると共に、該冷却塔と吸収器及び凝縮器に至る冷却水
配管中及び該冷却塔と熱源冷却器に至る冷却水配管中に
それぞれ自動制御弁を設けたことを特徴とする吸収冷温
水装置としたものであり、そして、上記の吸収冷温水装
置において、発生器への熱源供給通路には、熱源過剰度
検出器を設けるのがよい。In order to achieve the above object, in the present invention, a generator, a condenser, an absorber, an evaporator, a solution heat exchanger as a main component device, these are connected by a solution pipe, a refrigerant pipe absorption cold temperature constituting a cycle In the water device, a heat source cooler is provided in the heat source supply passage to the generator, and a cooling tower for cooling the cooling water for cooling the heat source cooler, the absorber and the condenser is provided, and the cooling tower and An absorption cold / hot water device characterized in that an automatic control valve is provided in each of a cooling water pipe leading to an absorber and a condenser and in a cooling water pipe leading to the cooling tower and a heat source cooler, and In the above absorption chilled / hot water apparatus, a heat source excess degree detector may be provided in the heat source supply passage to the generator.
また、上記の他の目的を達成するために、本発明では、
上記の吸収冷温水装置の運転において、冷房サイクルで
は、冷却塔と吸収器及び凝縮器に至る冷却水配管中の自
動制御弁を開として冷却水を吸収器及び凝縮器に通水
し、一方暖房サイクルでは、前記自動制御弁を閉とし
て、吸収器及び凝縮器に通水せずに運転し、また、冷房
運転又は暖房運転において、熱源過剰の場合は冷却塔と
熱源冷却器に至る冷却水配管中の自動制御弁を開として
熱源を冷却水に放出する運転をすることを特徴とする吸
収冷温水装置の運転方法としたものである。In addition, in order to achieve the above-mentioned other objects, in the present invention,
In the above operation of the absorption chilled water heater, in the cooling cycle, the automatic control valve in the cooling water pipe leading to the cooling tower and the absorber and the condenser is opened to pass the cooling water to the absorber and the condenser, while heating In the cycle, the automatic control valve is closed to operate without passing water to the absorber and the condenser, and in the cooling operation or the heating operation, when the heat source is excessive, a cooling water pipe leading to the cooling tower and the heat source cooler. This is a method for operating an absorption chilled / hot water device, which is characterized in that an automatic control valve therein is opened to release a heat source to cooling water.
エンジンの排出熱などを熱源として運転する吸収冷温水
装置では、吸収冷温水装置の役目として冷温水を製造す
る以外に、熱源を冷却する役目もあるが、本発明では、
冷房運転モード、暖房運転モード、冷却塔単独運転モー
ドの間をスムーズにモード変換がてきる。また、本発明
では、冷房運転モードあるいは、暖房運転モードであっ
ても、熱源過剰の場合(熱源が温水の場合、温水温度で
検出し、熱源が蒸気の場合、蒸気圧で検出)、自動制御
弁Vwを制御して、熱源を冷却水に放出することも容易に
できる。In the absorption cold / hot water device that operates by using the exhaust heat of the engine as a heat source, in addition to producing cold / hot water as a function of the absorption cold / hot water device, it also has a role of cooling the heat source, but in the present invention,
The mode can be smoothly changed between the cooling operation mode, the heating operation mode, and the cooling tower single operation mode. Further, in the present invention, even in the cooling operation mode or the heating operation mode, when the heat source is excessive (when the heat source is hot water, it is detected by the hot water temperature, and when the heat source is steam, it is detected by the steam pressure), automatic control It is also possible to easily release the heat source to the cooling water by controlling the valve Vw.
冷却塔の運転、冷却器への冷却水流量制御動作は、冷温
水機の運転制御と深く関わり、各モードの制御は、冷温
水機制御盤で行うのが、好ましい。The operation of the cooling tower and the operation of controlling the flow rate of the cooling water to the cooler are closely related to the operation control of the chiller-heater, and the control of each mode is preferably performed by the chiller-heater control panel.
各モードの制御は次のようになる。The control of each mode is as follows.
冷房運転モード:自動制御弁Vrを開として、冷却水を冷
温水機に通水し、吸収冷温水機は冷房サイクルをする。Cooling operation mode: The automatic control valve Vr is opened, cooling water is passed through the cooling / heating machine, and the absorption cooling / heating machine performs a cooling cycle.
熱源過剰の場合、自動制御弁Vwを制御して、熱源を冷却
水に放出する。When the heat source is excessive, the automatic control valve Vw is controlled to release the heat source to the cooling water.
暖房運転モード:自動制御弁Vrを開として、冷温水機に
は冷却水を通水せず、吸収冷温水機は暖房サイクルをす
る。Heating operation mode: The automatic control valve Vr is opened, the cooling water is not passed through the chiller-heater, and the absorption chiller-heater performs a heating cycle.
熱源過剰の場合、自動制御弁Vwを制御して、熱源を冷却
水に放出する。When the heat source is excessive, the automatic control valve Vw is controlled to release the heat source to the cooling water.
また吸収冷温水機内の冷却水の有無は、冷却水有で、起
動すると起動の時間がかかる。しかし、冷房に切り替え
る際は、すぐに冷房に入っていける。これは無では、吸
収器、凝縮器の満水に時間がかかるためである。自動弁
Vrと吸収器の間を始点とし、冷却塔を終点として、自動
弁を有する冷却水ブロー配管を設けてもよい。この自動
弁の制御は、冷暖房の切替が頻繁に予想される場合は、
閉として、ブローせず、暖房が続く場合は、開として、
ブローしてもよい。予想としては、季節を根拠にしても
よい。たとえば、冬期の暖房時は開とし、中間期には閉
とする。In addition, the presence or absence of cooling water in the absorption chiller / heater has cooling water, and it takes time to start up. However, when switching to air conditioning, you can immediately enter air conditioning. This is because it takes a long time to fill the absorber and condenser with nothing. Automatic valve
A cooling water blow pipe having an automatic valve may be provided with the start point between the Vr and the absorber and the end point at the cooling tower. This automatic valve control can be used when switching between air conditioning and heating is expected frequently.
If it is closed and does not blow, and heating continues, open it,
You can blow it. The forecast may be based on the season. For example, open during heating in winter and close during intermediate periods.
冷却塔単独運転モード:吸収冷温水機のサイクル運転は
停止とし、自動制御弁Vwを制御して、熱源を冷却水に放
出させる運転をする。Cooling tower single operation mode: The cycle operation of the absorption chiller-heater is stopped, and the automatic control valve Vw is controlled to discharge the heat source to the cooling water.
熱源過剰の場合、自動制御弁Vwを制御して熱源を冷却水
に放出する形態をとっているが、長期間冷却水が流れな
いと、熱源冷却器内の冷却水は、熱源温度と同程度まで
高まる。ここで、流れ出すと、冷却塔を痛める(冷却塔
の許容温度は50〜60℃程度:充填材がプラスチック
製)。この対策として熱源冷却器に対して、冷却水がバ
イパスするラインを設け、冷却器を通る冷却水とバイパ
スする冷却水とを混合し、許容温度以下としている。バ
イパスラインの流量制限は、オリフィスあるいは弁を用
いる。When the heat source is excessive, the automatic control valve Vw is controlled to release the heat source to the cooling water.However, if the cooling water does not flow for a long period of time, the cooling water in the heat source cooler has the same temperature as the heat source temperature. Increase to. Here, if it flows out, it damages the cooling tower (the allowable temperature of the cooling tower is about 50 to 60 ° C: the filler is made of plastic). As a countermeasure against this, a line for bypassing the cooling water is provided for the heat source cooler, and the cooling water passing through the cooler and the cooling water bypassing are mixed to keep the temperature below the allowable temperature. An orifice or valve is used to limit the flow rate of the bypass line.
以下、本発明を実施例により具体的に説明するが、本発
明はこれに限定されるものではない。Hereinafter, the present invention will be specifically described with reference to examples, but the present invention is not limited thereto.
実施例1 第1図に本発明の吸収冷温水装置のフロー構成図を示
す。第1図において、Gは発生器、Aは吸収器、Eは蒸
発器、Cは凝縮器、Hは溶液熱交換器、Vr,Vwは自動制
御弁、9は冷媒蒸気弁、10は冷媒液弁、11,12はポン
プ、15は熱源冷却器、16は熱源温度検出器、17は冷却
塔、20はポンプ、管1〜4は溶液通路、管5〜8は冷媒
通路、管21〜25は冷却水通路を示す。Example 1 FIG. 1 shows a flow configuration diagram of an absorption cold / hot water device of the present invention. In FIG. 1, G is a generator, A is an absorber, E is an evaporator, C is a condenser, H is a solution heat exchanger, Vr and Vw are automatic control valves, 9 is a refrigerant vapor valve, and 10 is a refrigerant liquid. Valves, 11 and 12 are pumps, 15 is a heat source cooler, 16 is a heat source temperature detector, 17 is a cooling tower, 20 is a pump, pipes 1 to 4 are solution passages, pipes 5 to 8 are refrigerant passages, and pipes 21 to 25. Indicates a cooling water passage.
そして、冷房運転モードでは、自動制御弁Vrを開とし
て、冷却水を吸収器A及び凝縮器Cに通水することによ
り運転を開始する。Then, in the cooling operation mode, the automatic control valve Vr is opened and the cooling water is passed through the absorber A and the condenser C to start the operation.
冷房運転モードにおける冷房サイクルを説明すると、ま
ず、冷媒を吸収した希溶液は吸収器Aから管1を通り、
ポンプ11により熱交換器の被加熱側に送られ、熱交換に
より加温された希溶液は管2を通り発生器Gに導入され
る。発生器Gでは、管14からのエンジンのジャケット温
水等の熱源により加熱されて、吸収した冷媒蒸気を蒸発
して濃縮される。濃縮された濃溶液は管3から熱交換器
Hの加熱側を通って、管4から吸収器Aに導入され再び
冷媒を吸収して希溶液となって管1から循環される。To explain the cooling cycle in the cooling operation mode, first, the diluted solution that has absorbed the refrigerant passes from the absorber A through the pipe 1,
The dilute solution sent to the heated side of the heat exchanger by the pump 11 and heated by the heat exchange is introduced into the generator G through the pipe 2. In the generator G, the refrigerant vapor that is heated by a heat source such as the jacket hot water of the engine from the pipe 14 is evaporated and concentrated. The concentrated concentrated solution passes from the pipe 3 through the heating side of the heat exchanger H, is introduced from the pipe 4 to the absorber A, absorbs the refrigerant again, and becomes a dilute solution, which is circulated from the pipe 1.
一方、発生器Gで発生した冷媒蒸気は凝縮器Cに至り、
凝縮器C中の冷却水によって冷却されて凝縮し、管5か
ら蒸発器Eに導入される。蒸発器Eでは、冷媒は冷水か
ら熱を奪い、冷凍効果を発揮して蒸発する。蒸発した冷
媒蒸気は吸収器Aで溶液に吸収される。吸収の際の吸収
熱は吸収器を流れる管24からの冷却水により冷却され
る。このような運転において、発生器に供給する熱源が
過剰の場合は温度検出器16の指令により自動制御弁Vwを
制御して熱源を冷却水に放出する。On the other hand, the refrigerant vapor generated in the generator G reaches the condenser C,
It is cooled by the cooling water in the condenser C, condensed, and introduced into the evaporator E from the pipe 5. In the evaporator E, the refrigerant takes heat from the cold water, exhibits a freezing effect, and evaporates. The vaporized refrigerant vapor is absorbed by the solution in the absorber A. The absorbed heat during absorption is cooled by the cooling water from the pipe 24 flowing through the absorber. In such operation, when the heat source supplied to the generator is excessive, the automatic control valve Vw is controlled by the command of the temperature detector 16 to release the heat source to the cooling water.
また、暖房運転モードでは、自動制御弁Vrを閉として、
冷温水機には冷却水を通水せず暖房サイクルで運転す
る。In the heating operation mode, the automatic control valve Vr is closed,
The cooling / heating machine is operated by a heating cycle without passing cooling water.
次に、暖房運転モードにおける暖房サイクルを説明す
る。Next, the heating cycle in the heating operation mode will be described.
暖房運転では、吸収器Aからの溶液を管1から溶液熱交
換器Hの被加熱側に導入し、加熱側の濃溶液と熱交換し
て温度を高め、溶液熱交換器Hを出た後、管2から発生
器Gに導入される。ここで溶液は、外部熱源14により加
熱され濃縮される。濃縮された濃溶液は、発生器Gから
管3により溶液熱交換器Hの加熱側に入り、被加熱側の
希溶液を加熱して管4から吸収器Aに入る。In the heating operation, the solution from the absorber A is introduced from the pipe 1 to the heated side of the solution heat exchanger H, heat exchanged with the concentrated solution on the heating side to raise the temperature, and after leaving the solution heat exchanger H. , From tube 2 to generator G. Here, the solution is heated and concentrated by the external heat source 14. The concentrated concentrated solution enters the heating side of the solution heat exchanger H from the generator G through the tube 3, heats the dilute solution on the heated side, and enters the absorber A through the tube 4.
発生器Gで溶液の濃縮が行われる際発生する冷媒蒸気
は、高圧側低圧側とを結ぶ冷媒蒸気配管7の冷媒蒸気弁
9を開とすることにより、管7から蒸発器Eに導かれ、
蒸発器Eを通る管18からの温水(空調用流体)に熱を与
えて凝縮する。凝縮した冷媒液は、吸収器Aに流入す
る。ここでは、冷媒液は、管6、冷媒ポンプ12、管8及
び冷媒液弁10を通して流れる。冷媒ポンプ12は停止して
いても差支えない。また、冷媒蒸気弁9は、外部流体温
度検出器19による流体温度の検出により、開閉でき温度
調節ができる。The refrigerant vapor generated when the solution is concentrated in the generator G is introduced from the pipe 7 to the evaporator E by opening the refrigerant vapor valve 9 of the refrigerant vapor pipe 7 connecting the high pressure side and the low pressure side.
The hot water (air-conditioning fluid) from the pipe 18 passing through the evaporator E is heated and condensed. The condensed refrigerant liquid flows into the absorber A. Here, the refrigerant liquid flows through the pipe 6, the refrigerant pump 12, the pipe 8 and the refrigerant liquid valve 10. The refrigerant pump 12 may be stopped. The refrigerant vapor valve 9 can be opened / closed and the temperature can be adjusted by detecting the fluid temperature by the external fluid temperature detector 19.
吸収器に入った溶液は、吸収塔が低圧のため冷媒の蒸気
圧が高く、冷媒蒸気を放出して温度が低下する。放出さ
れた冷媒蒸気は、蒸発器Eで高圧側の冷媒蒸気と共に凝
縮する。溶液は、そのまま吸収器Aを出て、蒸発器Eか
らの冷媒液と混合されて希溶液となって、管1から溶液
熱交換器Hに入り、循環して暖房サイクルを形成する。Since the absorption tower has a low pressure, the solution entering the absorber has a high vapor pressure of the refrigerant and releases the refrigerant vapor to lower the temperature. The released refrigerant vapor is condensed in the evaporator E together with the refrigerant vapor on the high pressure side. The solution leaves the absorber A as it is, is mixed with the refrigerant liquid from the evaporator E to become a dilute solution, enters the solution heat exchanger H from the pipe 1, and circulates to form a heating cycle.
このような暖房サイクルの運転においても、発生器に供
給される熱源が過剰の場合は、温度検出器16の指令によ
り自動制御弁Vrを制御して、過剰熱源を冷却水に放出す
る。Even in such a heating cycle operation, when the heat source supplied to the generator is excessive, the automatic control valve Vr is controlled by the command of the temperature detector 16 to release the excess heat source to the cooling water.
また、熱源としてエンジンの排出熱などを用いる場合、
冷温水を製造する以外に熱源を冷却する役目もあるた
め、冷却塔単独運転を作り、冷却塔単独運転モードで
は、冷温水機のサイクル運転は停止して、自動制御弁Vw
を制御して、熱源冷却器15に冷却水を流し熱源を冷却水
に放出させる。When using engine exhaust heat as a heat source,
In addition to producing cold / hot water, it also has the role of cooling the heat source.Therefore, a cooling tower independent operation is created.In the cooling tower independent operation mode, the cycle operation of the chiller / heater is stopped and the automatic control valve Vw
Is controlled to cause the cooling water to flow through the heat source cooler 15 to release the heat source to the cooling water.
熱源冷却器15からの熱源の放出がない場合は、熱源冷却
器15内の冷却水は熱源温度と同程度まで高まるため、こ
のような高温の冷却水を流出する場合は、バイパス通路
22より冷却水を流し、高温の冷却水を低下させてから冷
却塔に流すよう操作する。If the heat source cooler 15 does not release the heat source, the cooling water in the heat source cooler 15 rises to the same level as the heat source temperature.
Operate cooling water from 22 to lower the high temperature cooling water and then to the cooling tower.
本発明によれば、上記のような構成としたことにより、
冷房運転モード、暖房運転モード、冷却塔単独運転モー
ドの間のモード変換がスムーズにでき、しかも、同一の
空調用流体の経路が冷房と暖房に使用でき、操作上、経
済上非常に有利である。According to the present invention, with the above configuration,
The mode can be smoothly switched between the cooling operation mode, the heating operation mode, and the cooling tower independent operation mode, and the same air conditioning fluid path can be used for cooling and heating, which is very advantageous in terms of operation and economy. .
第1図は、本発明の吸収冷温水装置のフロー構成図であ
る。 G……発生器、A……吸収器、E……蒸発器、C……凝
縮器、H……溶液熱交換器、Vr,Vw……自動調節弁、1
〜4……溶液通路、5〜8……冷媒通路、9……冷媒蒸
気弁、10……冷媒液弁、11,12……ポンプ、13,14……熱
源通路、15……熱源冷却器、16……熱源温度検出器、17
……冷却塔、18……冷温水通路、19……外部流体温度検
出器、21〜25……冷却水通路。FIG. 1 is a flow configuration diagram of the absorption cold / hot water device of the present invention. G ... Generator, A ... Absorber, E ... Evaporator, C ... Condenser, H ... Solution heat exchanger, Vr, Vw ... Automatic control valve, 1
~ 4 ... Solution passage, 5-8 ... Refrigerant passage, 9 ... Refrigerant vapor valve, 10 ... Refrigerant liquid valve, 11,12 ... Pump, 13,14 ... Heat source passage, 15 ... Heat source cooler , 16 …… Heat source temperature detector, 17
...... Cooling tower, 18 ...... Cold and hot water passage, 19 ...... External fluid temperature detector, 21 to 25 ...... Cooling water passage.
Claims (3)
交換器を主要構成機器とし、これらを溶液配管、冷媒配
管で結んでサイクルを構成する吸収冷温水装置におい
て、発生器への熱源供給通路に熱源冷却器を設け、ま
た、該熱源冷却器、吸収器及び凝縮器を冷却するための
冷却水を冷却する冷却塔を設けると共に、該冷却塔と吸
収器及び凝縮器に至る冷却水配管中及び該冷却塔と熱源
冷却器に至る冷却水配管中にそれぞれ自動制御弁を設け
たことを特徴とする吸収冷温水装置。1. An absorption cold / hot water device in which a generator, a condenser, an absorber, an evaporator, and a solution heat exchanger are main constituent devices, and these are connected by a solution pipe and a refrigerant pipe to form a cycle. A heat source cooler is provided in the heat source supply passage of the device, and a cooling tower for cooling the cooling water for cooling the heat source cooler, the absorber and the condenser is provided, and the cooling tower, the absorber and the condenser are provided. An absorption cold / hot water apparatus, wherein an automatic control valve is provided in each of the cooling water pipe and the cooling water pipe leading to the cooling tower and the heat source cooler.
剰度検出器を設けたことを特徴とする請求項1記載の吸
収冷温水装置。2. The absorption cold / hot water apparatus according to claim 1, wherein a heat source excess degree detector is provided in the heat source supply passage to the generator.
いて、冷房サイクルでは、冷却塔と吸収器及び凝縮器に
至る冷却水配管中の自動制御弁を開として冷却水を吸収
器及び凝縮器に通水し、一方暖房サイクルでは、前記自
動制御弁を閉として、吸収器及び凝縮器に通水せずに運
転し、また、冷房運転又は暖房運転において、熱源過剰
の場合は冷却塔と熱源冷却器に至る冷却水配管中の自動
制御弁を開として熱源を冷却水に放出する運転をするこ
とを特徴とする吸収冷温水装置の運転方法。3. In the operation of the absorption chilled / hot water apparatus according to claim 1, in a cooling cycle, an automatic control valve in a cooling water pipe leading to a cooling tower and an absorber and a condenser is opened to cool and condense the cooling water. In the heating cycle, the automatic control valve is closed to operate without passing water to the absorber and the condenser, and in the cooling operation or the heating operation, when the heat source is excessive, the cooling tower is used. A method for operating an absorption chilled / hot water device, which comprises operating an automatic control valve in a cooling water pipe to a heat source cooler to open to release the heat source to the cooling water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33023790A JPH0754209B2 (en) | 1990-11-30 | 1990-11-30 | Absorption cold / hot water device and its operating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33023790A JPH0754209B2 (en) | 1990-11-30 | 1990-11-30 | Absorption cold / hot water device and its operating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04203861A JPH04203861A (en) | 1992-07-24 |
| JPH0754209B2 true JPH0754209B2 (en) | 1995-06-07 |
Family
ID=18230398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33023790A Expired - Fee Related JPH0754209B2 (en) | 1990-11-30 | 1990-11-30 | Absorption cold / hot water device and its operating method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0754209B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6745059B2 (en) | 2001-11-28 | 2004-06-01 | American Superconductor Corporation | Superconductor cables and magnetic devices |
| JP2007309617A (en) * | 2006-05-22 | 2007-11-29 | Chugoku Electric Power Co Inc:The | Gas cooling system |
-
1990
- 1990-11-30 JP JP33023790A patent/JPH0754209B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04203861A (en) | 1992-07-24 |
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