JPH0222312B2 - - Google Patents

Info

Publication number
JPH0222312B2
JPH0222312B2 JP14722481A JP14722481A JPH0222312B2 JP H0222312 B2 JPH0222312 B2 JP H0222312B2 JP 14722481 A JP14722481 A JP 14722481A JP 14722481 A JP14722481 A JP 14722481A JP H0222312 B2 JPH0222312 B2 JP H0222312B2
Authority
JP
Japan
Prior art keywords
water
condenser
temperature
pipe
hot 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
Application number
JP14722481A
Other languages
Japanese (ja)
Other versions
JPS5847971A (en
Inventor
Kazuhiro Yoshii
Teruo Masuda
Akira Shiraishi
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP14722481A priority Critical patent/JPS5847971A/en
Publication of JPS5847971A publication Critical patent/JPS5847971A/en
Publication of JPH0222312B2 publication Critical patent/JPH0222312B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/006Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the sorption type system

Description

【発明の詳細な説明】 本発明は冷却水系凝縮器と温水系凝縮器とを有
する吸収冷温水機に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption chiller/heater having a cooling water system condenser and a hot water system condenser.

此種ダブルバンドル型吸収冷温水機は凝縮器か
ら取り出す温水が冷房用冷水負荷の変動に左右さ
れて安定した温度の温水を得ることができない欠
点を有する。すなわち、冷水負荷が大きいときは
通常再生器への加熱量を増して多量の冷媒を冷水
負荷に供するので再成器からの冷媒蒸気の凝縮器
内における放熱量が多く高温の温水を取り出し得
るが、冷水負荷が小さいときは再生器への加熱量
を減じるために凝縮器内での冷媒蒸気放熱量が少
く所望の温度の温水が得られない欠点を有する。
This type of double-bundle type absorption chiller/heater has the disadvantage that the hot water taken out from the condenser is affected by fluctuations in the cooling water load, making it impossible to obtain hot water at a stable temperature. In other words, when the chilled water load is large, the amount of heating to the regenerator is usually increased to provide a large amount of refrigerant to the chilled water load, so the amount of heat dissipated in the condenser of the refrigerant vapor from the regenerator is large, and high-temperature hot water can be taken out. However, when the chilled water load is small, the amount of heat released from the refrigerant vapor in the condenser is small in order to reduce the amount of heating to the regenerator, which has the disadvantage that hot water at the desired temperature cannot be obtained.

本発明は、斯る点に鑑み、温水を取り出す一方
の凝縮器の水管と高温再生器に付設された温水器
に設けられた水管とを連通し、他方の凝縮器の冷
却水管に制御弁を介して側路管を接続し、前記一
方の凝縮器の出口温度に基づいて前記制御弁の開
度を調整する制御器を備えた構成の吸収冷温水機
で、所望の温度の温水を安定して機外へ供給する
のを目的としたものである。
In view of this, the present invention communicates the water pipe of one condenser that takes out hot water with the water pipe provided in the water heater attached to the high-temperature regenerator, and provides a control valve to the cooling water pipe of the other condenser. The absorption chiller/heater is configured to include a controller that connects a side pipe through the condenser and adjusts the opening degree of the control valve based on the outlet temperature of one of the condensers, stabilizing hot water at a desired temperature. The purpose is to supply the liquid to the outside of the aircraft.

以下、本発明の一実施例を図面に基づき説明す
る。
Hereinafter, one embodiment of the present invention will be described based on the drawings.

1は都市ガス或いはオイル等の燃焼加熱室2と
該加熱室からの導熱管3,3を有し稀液から冷媒
蒸気を加熱分離して中間液を再生する高温再生
器、4は、前記高温再生器1からの冷媒蒸気によ
り中間液を加熱して更に冷媒蒸気を分離し濃液に
再生する低温再生器5と、前記両再生器1,5か
らの冷媒蒸気を凝縮冷却する温水系凝縮器6およ
び冷却水系凝縮器7とで構成する再生凝縮胴、8
は前記再生凝縮胴4からの液冷媒を散布して気化
させる際の潜熱を利用して冷房用冷水を得るよう
に蒸発器、9は前記低温再生器5からの濃液を散
布して気化冷媒を吸収することにより前記蒸発器
8内を低圧に維持して連続した冷水供給を行なえ
るようにした吸収器、10及び11は低温交換器
及び高温熱交換器で、これらは冷媒蒸気配管1
2、冷媒液流下管13、冷媒ポンプ14を有する
冷媒循環路15、吸収液ポンプ16を有する稀液
管17、中間液管18および濃液管19で配管接
続されて冷凍サイクルを構成している。20は前
記高温再生器1に付設された温水器で、該温水器
下部と高温再生器とを接続する冷媒管21にドレ
ン制御弁22が配設されている。23は前記温水
系凝縮器6から温水器20を経て温水を取り出す
水管であり、該水管の凝縮器6出口側と温水器2
0出口側とに夫々温度検出器24と25が設けら
れている。26は前記吸収器9から冷却水系凝縮
器7を経て濃液が気化冷媒を吸収する際の稀釈熱
および冷媒蒸気の凝縮潜熱を奪う冷却水管であ
り、該冷却水管には三方弁27を介して凝縮器7
をバイパスする側路管28が設けられている。2
9は前記蒸発器8を径て冷水を取り出す冷水管で
あり、該冷水管には温度検出器30が配設されて
いる。又31は前記燃焼加熱室2への燃料供給路
であり、該供給路には燃料制御弁32が配設され
ている。そして前記ドレン制御弁22は温度調節
器33を介して温度検出器25の信号により開度
調整され、燃料制御弁32は調節器34を介して
冷水側温度検出器30から送られる信号と調節器
33を介して温水側温度検出器25から送られる
信号とを数値処理する中央演算制御器35により
開度調整され、又三方弁27は調節器36を介し
て凝縮器6出口側温度検出器24の信号により開
度調整される。
1 is a high-temperature regenerator which has a combustion heating chamber 2 for city gas or oil, etc. and heat conduction pipes 3, 3 from the heating chamber, and heats and separates refrigerant vapor from a dilute liquid to regenerate an intermediate liquid; A low-temperature regenerator 5 that heats the intermediate liquid with the refrigerant vapor from the regenerator 1, further separates the refrigerant vapor, and regenerates it into a concentrated liquid; and a hot water system condenser that condenses and cools the refrigerant vapor from both the regenerators 1 and 5. 6 and a cooling water system condenser 7;
9 is an evaporator configured to obtain cold water for air conditioning by using the latent heat when the liquid refrigerant from the regenerated condensation barrel 4 is sprayed and vaporized; 9 is a vaporized refrigerant that is sprayed with the concentrated liquid from the low-temperature regenerator 5; 10 and 11 are a low temperature exchanger and a high temperature heat exchanger, which are connected to the refrigerant vapor pipe 1.
2. A refrigerant circulation path 15 having a refrigerant liquid flow pipe 13, a refrigerant pump 14, a dilute liquid pipe 17 having an absorption liquid pump 16, an intermediate liquid pipe 18, and a concentrated liquid pipe 19 are connected to form a refrigeration cycle. . 20 is a water heater attached to the high temperature regenerator 1, and a drain control valve 22 is disposed in a refrigerant pipe 21 connecting the lower part of the water heater and the high temperature regenerator. 23 is a water pipe that takes out hot water from the hot water system condenser 6 via the water heater 20, and the water pipe is connected to the outlet side of the condenser 6 and the water heater 2.
Temperature detectors 24 and 25 are provided on the zero exit side, respectively. Reference numeral 26 denotes a cooling water pipe which takes away the heat of dilution and the latent heat of condensation of the refrigerant vapor when the concentrated liquid absorbs the vaporized refrigerant from the absorber 9 through the cooling water system condenser 7. Condenser 7
A bypass pipe 28 is provided to bypass the. 2
Reference numeral 9 denotes a cold water pipe that takes out cold water through the evaporator 8, and a temperature detector 30 is disposed in the cold water pipe. Further, 31 is a fuel supply path to the combustion heating chamber 2, and a fuel control valve 32 is disposed in the supply path. The opening of the drain control valve 22 is adjusted by a signal from a temperature detector 25 via a temperature regulator 33, and the opening of the fuel control valve 32 is adjusted by a signal sent from a cold water side temperature detector 30 via a regulator 34. The opening degree of the three-way valve 27 is adjusted by a central processing controller 35 that numerically processes the signal sent from the hot water side temperature detector 25 via the controller 33, and the three-way valve 27 is connected to the condenser 6 outlet side temperature sensor 24 via the regulator 36. The opening is adjusted by the signal.

而して、吸収冷温水機の稼動中、冷房用冷水負
荷が小さくなつたとき即ち冷水温度が低くなつた
とき、前記冷水側温度検出器30の信号により調
節器34、中央演算制御器35を介して燃料制御
弁32開度を減じ高温再生器1への加熱量を減ら
して冷水負荷に対応する冷媒量を発生せしめる。
この際に、前記再生凝縮胴4に導入される冷媒蒸
気量が減少するために、温水の前記温水系凝縮器
6出口側温度が低下し、該温度を検出する前記温
度検出器24の信号により調節器36を介して三
方弁27の側路管28側開度を増し凝縮器7側開
度を減らして前記再生凝縮胴4への冷却水量を減
じる。その結果、再生凝縮胴4内の冷媒蒸気に冷
却水系凝縮器7での凝縮量を減じ、冷媒蒸気の多
くが温水系凝縮器6で凝縮して潜熱が温水に放熱
されるので、所定温度の温水が前記水管から取り
出すことができる。尚、前記冷却水系凝縮器7へ
の冷却水量を零にしても所定温度の温水が得られ
ない場合には、前記温水器20出口側の温度検出
器25の信号により調節器33を介してドレン制
御弁22の開度を増し、温水器20内の液冷媒水
位を下げ水管23の冷媒蒸気との伝熱面を増やし
て温水を昇温する。
During operation of the absorption chiller/heater, when the chilled water load for cooling becomes small, that is, when the chilled water temperature becomes low, the regulator 34 and the central processing controller 35 are activated by the signal from the chilled water side temperature detector 30. The opening degree of the fuel control valve 32 is reduced to reduce the amount of heating to the high temperature regenerator 1, thereby generating an amount of refrigerant corresponding to the chilled water load.
At this time, since the amount of refrigerant vapor introduced into the regeneration condensation shell 4 decreases, the temperature of hot water at the outlet side of the hot water system condenser 6 decreases, and the signal from the temperature detector 24 that detects the temperature decreases. The opening degree of the three-way valve 27 on the side pipe 28 side is increased and the opening degree on the condenser 7 side is decreased through the regulator 36, thereby reducing the amount of cooling water to the regenerated condensation shell 4. As a result, the amount of condensation in the cooling water system condenser 7 is reduced to the refrigerant vapor in the regenerating condensing shell 4, and most of the refrigerant vapor is condensed in the hot water system condenser 6, and the latent heat is radiated to the hot water, so that the predetermined temperature is Hot water can be drawn from the water tube. Note that if hot water at a predetermined temperature is not obtained even if the amount of cooling water to the cooling water system condenser 7 is reduced to zero, the water is drained via the regulator 33 according to the signal from the temperature sensor 25 on the outlet side of the water heater 20. The opening degree of the control valve 22 is increased, the liquid refrigerant level in the water heater 20 is lowered, and the heat transfer surface with the refrigerant vapor in the water pipe 23 is increased to raise the temperature of the hot water.

すなわち、斯る吸収冷温水機は高温再生器1へ
の加熱量を減じても所望温度の温水を取り出し得
るもので、供給加熱エネルギーを有効に利用する
熱効率の良い冷温水器である。
In other words, such an absorption water cooler/heater can take out hot water at a desired temperature even if the amount of heating to the high temperature regenerator 1 is reduced, and is a water cooler/heater with good thermal efficiency that effectively utilizes the supplied heating energy.

尚亦、冷水負荷が極めて小さく高温再生器1へ
の加熱量が不足するときには、前記温度検出器2
5の信号により調節器33、中央演算制御器35
を介して熱料制御弁32の開度を増して加熱量を
増やし温水器20内への冷媒蒸気導入量を増加さ
せて温水を昇温する。
Furthermore, when the cold water load is extremely small and the amount of heating to the high temperature regenerator 1 is insufficient, the temperature detector 2
5, the regulator 33 and the central processing controller 35
The opening degree of the heating material control valve 32 is increased to increase the amount of heating, and the amount of refrigerant vapor introduced into the water heater 20 is increased to raise the temperature of the hot water.

次に、吸収冷温水機の稼動中、冷水負荷が増大
したとき即ち冷水温度が高くなつたとき、増大し
た冷水負荷に対応して高温再生器1への加熱量が
増やされて再生凝縮胴4内に導入される冷媒蒸気
量が増加し、温水系凝縮器6出口側の温水温度が
上昇し、該温度を検出する温度検出器24の信号
により調節器36を介して三方弁27の側路管2
8側開度を減じ凝縮器7側開度を増して再生凝縮
胴4への冷却水量を増やす。その結果、再生凝縮
胴4内の冷媒蒸気凝縮潜熱の多くは冷却水に放熱
されるので、所定温度の温水が水管23から取り
出すことができる。
Next, during operation of the absorption chiller/heater, when the chilled water load increases, that is, when the chilled water temperature becomes high, the amount of heating to the high temperature regenerator 1 is increased in response to the increased chilled water load, and the regenerating condensing cylinder 4 The amount of refrigerant vapor introduced into the refrigerant vapor increases, and the hot water temperature at the outlet side of the hot water system condenser 6 rises, and a signal from the temperature detector 24 that detects this temperature causes the side passage of the three-way valve 27 to be increased via the regulator 36. tube 2
The opening degree on the 8th side is decreased and the opening degree on the condenser 7 side is increased to increase the amount of cooling water to the regenerated condensation shell 4. As a result, most of the latent heat of refrigerant vapor condensation in the regenerating condensation shell 4 is radiated to the cooling water, so hot water at a predetermined temperature can be taken out from the water pipe 23.

このように、斯る吸収冷温水機は、冷水負荷変
動に応じた加熱量制御に伴なう再生凝縮胴4内冷
媒蒸気の放熱量変動に対し冷却水量を変化させて
機外への放熱量を調整し温水への冷媒蒸気放熱量
を常時略一定となし得、冷水負荷に応じた冷水を
取り出すことができると同時に所望温度の温水を
効率良く安定して取り出すことができるものであ
る。
In this way, such an absorption chiller/heater changes the amount of cooling water to respond to changes in the amount of heat released from the refrigerant vapor inside the regenerating condensing shell 4 due to heating amount control according to changes in the chilled water load. By adjusting the amount of heat released from the refrigerant vapor to the hot water, the amount of heat released from the refrigerant vapor to the hot water can be kept substantially constant at all times, and at the same time, it is possible to take out cold water according to the cold water load, and at the same time, it is possible to efficiently and stably take out hot water at a desired temperature.

又、図示しないが、前記三方弁27に代えて制
御弁を側路管28に配設して該側路管の冷却水流
量を変化させ間接的に凝縮器7を流れる冷却水量
を変化させても良いが、三方弁27により直接に
凝縮器7を流れる冷却水量を変化させる方が精度
の高い制御となる。或いは、又、三方弁27に代
えて側路管28と分岐した冷却水管26とに夫々
制御弁(図示せず。)を設けても良い。
Although not shown, a control valve is provided in the side pipe 28 in place of the three-way valve 27 to change the flow rate of cooling water in the side pipe, thereby indirectly changing the amount of cooling water flowing through the condenser 7. However, using the three-way valve 27 to directly change the amount of cooling water flowing through the condenser 7 provides more accurate control. Alternatively, instead of the three-way valve 27, a control valve (not shown) may be provided in each of the side pipe 28 and the branched cooling water pipe 26.

亦、斯る吸収冷温水機は、再生凝縮胴4内の冷
媒凝縮温度以上の高温水(例えば80℃の高温水)
も前記温水器20の出口側水管23から取り出す
ことができるものである。
In addition, such an absorption chiller/heater uses high-temperature water (e.g., 80°C high-temperature water) that is higher than the refrigerant condensation temperature in the regeneration condensation shell 4.
It can also be taken out from the outlet side water pipe 23 of the water heater 20.

以上のように、本発明は、冷却水管で形成する
凝縮器と温水を取り出す水管で形成する別の凝縮
器を設け、温水を取り出す一方の凝縮器の水管と
高温再生器に付設された温水器に設けられた水管
とを連通し、他方の凝縮器の冷却水管に制御弁を
介して前記凝縮器をバイパスする側路管を設け、
且つ一方の凝縮器出口側の温水温度を検出して前
記制御弁の開度を調整して冷却水流量を制御する
ようにしたので、所望の温水を安定して取り出す
ことができ、さらに、凝縮器内の冷媒凝縮温度よ
り高い温度の温水を温水器から取り出すことがで
きる。
As described above, the present invention provides a condenser formed by a cooling water pipe and another condenser formed by a water pipe for taking out hot water, and a water pipe for one condenser for taking out hot water and a water heater attached to a high temperature regenerator. A side pipe is provided in the cooling water pipe of the other condenser to bypass the condenser through a control valve,
In addition, since the hot water temperature on the outlet side of one condenser is detected and the opening degree of the control valve is adjusted to control the cooling water flow rate, the desired hot water can be stably taken out, and furthermore, the desired hot water can be taken out stably. Hot water at a temperature higher than the condensation temperature of the refrigerant inside the vessel can be taken out from the water heater.

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

図面は本発明実施例の回路構成説明図である。 1……高温再生器、6……温水系凝縮器、7…
…冷却水系凝縮器、20……温水器、23……水
管、26……冷却水管、27……三方弁、28…
…側路管、35……制御器。
The drawing is an explanatory diagram of a circuit configuration of an embodiment of the present invention. 1...High temperature regenerator, 6...Hot water system condenser, 7...
... Cooling water system condenser, 20 ... Water heater, 23 ... Water pipe, 26 ... Cooling water pipe, 27 ... Three-way valve, 28 ...
...Side pipe, 35...Controller.

Claims (1)

【特許請求の範囲】[Claims] 1 2つの凝縮器を備えた吸収冷温水器におい
て、温水を取り出す一方の凝縮器の水管と、高温
再生器に付設された温水器に設けられた水管とを
連通し、他方の凝縮器の冷却水管に制御弁を介し
てこの他方の凝縮器を側路する管を接続し、前記
一方の凝縮器の出口側温度に基づいて前記制御弁
の開度を調整する制御器を備えたことを特徴とす
る吸収冷温水機。
1. In an absorption cold water heater equipped with two condensers, the water pipe of one condenser that takes out hot water is connected to the water pipe installed in the water heater attached to the high-temperature regenerator, and the water pipe of the other condenser is cooled. The water pipe is connected to a pipe that bypasses the other condenser through a control valve, and includes a controller that adjusts the opening degree of the control valve based on the outlet side temperature of the one condenser. Absorption chiller/heater.
JP14722481A 1981-09-17 1981-09-17 Absorption cold and hot water machine Granted JPS5847971A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14722481A JPS5847971A (en) 1981-09-17 1981-09-17 Absorption cold and hot water machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14722481A JPS5847971A (en) 1981-09-17 1981-09-17 Absorption cold and hot water machine

Publications (2)

Publication Number Publication Date
JPS5847971A JPS5847971A (en) 1983-03-19
JPH0222312B2 true JPH0222312B2 (en) 1990-05-18

Family

ID=15425373

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14722481A Granted JPS5847971A (en) 1981-09-17 1981-09-17 Absorption cold and hot water machine

Country Status (1)

Country Link
JP (1) JPS5847971A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6159166A (en) * 1984-08-29 1986-03-26 三洋電機株式会社 Absorption refrigerator

Also Published As

Publication number Publication date
JPS5847971A (en) 1983-03-19

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