JPH07120095A - Air-cooled absorption hot and chilled water generator and operating method therefor - Google Patents

Air-cooled absorption hot and chilled water generator and operating method therefor

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Publication number
JPH07120095A
JPH07120095A JP28982293A JP28982293A JPH07120095A JP H07120095 A JPH07120095 A JP H07120095A JP 28982293 A JP28982293 A JP 28982293A JP 28982293 A JP28982293 A JP 28982293A JP H07120095 A JPH07120095 A JP H07120095A
Authority
JP
Japan
Prior art keywords
air
refrigerant
solution
cooled
heat transfer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP28982293A
Other languages
Japanese (ja)
Inventor
Akiyoshi Suzuki
晃好 鈴木
Hajime Yatsuhashi
元 八橋
Osayuki Inoue
修行 井上
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP28982293A priority Critical patent/JPH07120095A/en
Publication of JPH07120095A publication Critical patent/JPH07120095A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To provide an air-cooled absorption hot and chilled water generator in which crystallization is prevented by obtaining circulation of solution at the time of heating and which has a high thermal efficiency. CONSTITUTION:An air-cooled absorption hot and chilled water generator comprises a regenerator 1, an air-cooled absorber 2, an air-cooled condenser 3, an evaporator 4, a water heater 5 connected to the regenerator 1 through a vapor tube, a solution pump 7 for connecting them, a solution passage and a refrigerant passage having a solution pump 8 and switching valves 11, 12 with water as a main ingredient of refrigerant, wherein the absorber 2 has a plurality of horizontal heat transfer tubes 10. The tubes 18 are provided outside the tubes with plate fins 9. A spray tube 15 having a plurality of spray nozzles 16 for spraying liquid to upper inner walls of the tubes in the tubes is provided in the tube 10. The evaporator 4 has a vertical heat transfer tube 13 which can supply refrigerant liquid or concentrated solution to the outside with chilled/hot water flowing therethrough. The absorber 2 is separated from the evaporator 4 by an eliminator 14. Accordingly, at the time of cooling and heating, the refrigerant liquid and the solution flowing through the absorber and the evaporator are switched to be operated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、吸収冷温水機に係り、
特に冷暖房時に冷媒通路と溶液通路を切換えて冷温水を
製造することのできる空冷吸収冷温水機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption chiller / heater,
In particular, the present invention relates to an air-cooled absorption cold / hot water machine capable of producing cold / hot water by switching the refrigerant passage and the solution passage at the time of cooling / heating.

【0002】[0002]

【従来の技術】従来、吸収冷温水機において、暖房運転
する場合は、凝縮器、蒸発器、吸収器を切り離して、溶
液ポンプ、冷媒ポンプを止めて、冷媒を再生器→温水器
→再生器と循環して、再生器からの冷媒蒸気を温水器に
送り、冷媒蒸気の凝縮熱を利用して暖房用の温水を加熱
し、凝縮した冷媒を再生器に送り再び蒸発させて循環し
ていた。
2. Description of the Related Art Conventionally, in heating and cooling an absorption chiller-heater, the condenser, the evaporator, and the absorber are separated, the solution pump and the refrigerant pump are stopped, and the refrigerant is regenerator-> water heater-> regenerator. The refrigerant vapor from the regenerator was sent to the water heater, the condensing heat of the refrigerant vapor was used to heat the hot water for heating, and the condensed refrigerant was sent to the regenerator for evaporation and circulation. .

【0003】このような暖房運転において、バーナー上
部に燃焼室を、さらに燃焼室の上に再生器溶液濃縮部を
設けた再生器では、燃焼室廻りに希溶液管を密着させ
て、燃焼室カバーを冷却しているため、溶液ポンプを止
めると、燃焼室廻りの配管に溶液の循環がなくなり、燃
焼すると、配管内溶液が結晶するという問題があった。
また、冷媒蒸気の凝縮熱のみを用いた暖房であり、熱効
率が悪かった。
In such a heating operation, in a regenerator having a combustion chamber above the burner and a regenerator solution concentrating portion above the combustion chamber, a dilute solution pipe is closely attached around the combustion chamber to cover the combustion chamber. Since the solution is cooled, there is a problem that when the solution pump is stopped, the solution does not circulate in the pipe around the combustion chamber, and when the solution is burned, the solution in the pipe is crystallized.
Further, the heating uses only the condensation heat of the refrigerant vapor, and the thermal efficiency is poor.

【0004】[0004]

【発明が解決しようとする課題】本発明は、暖房時であ
っても溶液ポンプを運転して、溶液循環を確保するとと
もに、暖房時の溶液循環系内で、極端な濃度分布をさ
け、溶液が結晶化せず、熱効率のよい空冷吸収冷温水機
とその運転方法を提供することを課題とする。
SUMMARY OF THE INVENTION According to the present invention, a solution pump is operated even during heating to ensure solution circulation, and an extreme concentration distribution is avoided in the solution circulation system during heating. It is an object of the present invention to provide an air-cooled absorption chiller-heater with good thermal efficiency and a method of operating the same that does not crystallize.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、再生器、空冷吸収器、空冷凝縮器、蒸
発器及び再生器と蒸気配管で結んだ温水器を有すると共
に、それらを連絡する溶液ポンプ、冷媒ポンプと切替え
弁を有する溶液通路及び冷媒通路を有し、水を冷媒の主
成分とする空冷吸収冷温水機において、前記空冷吸収器
は、複数の水平伝熱管からなり、該水平伝熱管は伝熱管
外にプレートフィンを設け、伝熱管内には伝熱管内壁上
部に液体をスプレーする複数のスプレーノズルを有する
スプレー管を設けて構成され、前記蒸発器は、内部に冷
温水を通し、外部に冷媒液又は濃溶液を供給できる構造
の垂直伝熱管を有し、前記空冷吸収器と蒸発器とはエリ
ミネータで分離されていることとしたものである。
In order to solve the above-mentioned problems, the present invention has a regenerator, an air-cooled absorber, an air-cooled condenser, an evaporator, and a water heater connected to the regenerator by a steam pipe. In the air-cooled absorption chiller-heater having a solution pump for communicating with each other, a solution passage having a refrigerant pump and a switching valve, and a refrigerant passage, and water as a main component of the refrigerant, the air-cooled absorber includes a plurality of horizontal heat transfer tubes. The horizontal heat transfer tube is provided with plate fins outside the heat transfer tube, and the inside of the heat transfer tube is provided with a spray tube having a plurality of spray nozzles for spraying a liquid on the inner wall of the heat transfer tube. A vertical heat transfer tube having a structure capable of supplying cold or hot water and supplying a refrigerant liquid or a concentrated solution to the outside is provided, and the air-cooled absorber and the evaporator are separated by an eliminator.

【0006】また、本発明では、前記空冷吸収冷温水機
の運転方法において、冷房運転時には、溶液ポンプと冷
媒ポンプを運転して、また再生器からの冷媒蒸気を空冷
凝縮器に導き、温水器には行かないよう遮断して吸収サ
イクルを形成し、暖房運転時には、冷媒ポンプを停止状
態として、再生器からの溶液を蒸発器スプレーヘッダー
に供給し、また再生器から空冷凝縮器への冷媒蒸気経路
を遮断するとともに、再生器から温水器への冷媒蒸気経
路を開放し、温水器内温水伝熱管と接触させ、温水器で
凝縮した冷媒液を吸収器の最上段部のスプレー管に供給
することとしたものである。
Further, according to the present invention, in the method of operating the air-cooled absorption chiller-heater, the solution pump and the refrigerant pump are operated during the cooling operation, and the refrigerant vapor from the regenerator is guided to the air-cooled condenser to cool the water heater. In the heating operation, the refrigerant pump is stopped, the solution from the regenerator is supplied to the evaporator spray header, and the refrigerant vapor from the regenerator to the air-cooled condenser is shut off so that it does not go to the In addition to shutting off the path, open the refrigerant vapor path from the regenerator to the water heater to bring it into contact with the hot water heat transfer tube in the water heater and supply the refrigerant liquid condensed in the water heater to the spray pipe at the top stage of the absorber. It was decided.

【0007】上記のように、本発明は、水を冷媒の主成
分とし、吸収溶液にLi塩水溶液等を用いる空冷吸収冷
暖房機において、空冷吸収器の伝熱管をほぼ水平に設置
し、伝熱管外にはプレートフィンを設けて、伝熱面積を
拡大して冷却空気と接触させ、伝熱管内に吸収溶液を供
給し、伝熱管内への吸収溶液の供給に当たっては、伝熱
管内に溶液を導くとともに、複数のスプレーノズルから
伝熱管内壁上部に溶液をスプレーするスプレー管を設け
ている吸収器とし、蒸発器は垂直伝熱管としている。そ
して、冷房運転時には、伝熱管内部に冷水を通し、伝熱
管外部に冷媒液を供給して蒸発させる構造として、蒸発
器下部の冷媒液を冷媒ポンプにて、蒸発器スプレーヘッ
ダーに供給し、また溶液ポンプと、冷媒ポンプを運転
し、再生器からの冷媒蒸気を空冷凝縮器に導き、(再生
器の冷媒蒸気が温水器には行かないよう遮断して)吸収
サイクルを形成する。
As described above, according to the present invention, in the air-cooled absorption cooling / heating machine in which water is the main component of the refrigerant and Li salt aqueous solution or the like is used as the absorbing solution, the heat-transfer tubes of the air-cooling absorber are installed substantially horizontally, A plate fin is provided outside to expand the heat transfer area to bring it into contact with cooling air, supply the absorbing solution into the heat transfer tube, and supply the absorbing solution into the heat transfer tube. An absorber is provided with a spray pipe that guides the solution from a plurality of spray nozzles onto the inner wall of the heat transfer pipe, and the evaporator is a vertical heat transfer pipe. Then, during the cooling operation, cold water is passed through the heat transfer tube, and the refrigerant liquid is supplied to the outside of the heat transfer tube to evaporate, and the refrigerant liquid at the bottom of the evaporator is supplied to the evaporator spray header by the refrigerant pump. The solution pump and the refrigerant pump are operated to direct the refrigerant vapor from the regenerator to the air-cooled condenser and form an absorption cycle (blocking the refrigerant vapor of the regenerator from going to the water heater).

【0008】また、暖房運転時には、蒸発器の伝熱管内
部に温水を通し、伝熱管外部に濃溶液を供給して蒸発し
た冷媒を吸収させる構造として、蒸発器下部の溶液を溶
液ポンプにて再生器に供給し、また冷媒ポンプを停止状
態として、再生器からの溶液を蒸発器スプレーヘッダー
に供給し、再生器から凝縮器への冷媒蒸気経路を遮断す
るとともに再生器から温水器への冷媒蒸気経路を開放し
温水器内温水伝熱管と接触させ、温水器で凝縮した冷媒
液を吸収器の最上段部のスプレー管に供給するものであ
る。
Further, during heating operation, hot water is passed through the heat transfer tube of the evaporator, and a concentrated solution is supplied to the outside of the heat transfer tube to absorb the evaporated refrigerant, so that the solution under the evaporator is regenerated by a solution pump. Supply the solution from the regenerator to the evaporator spray header, shut off the refrigerant vapor path from the regenerator to the condenser, and at the same time supply the refrigerant vapor from the regenerator to the water heater. The path is opened to contact the hot water heat transfer pipe in the water heater, and the refrigerant liquid condensed in the water heater is supplied to the spray pipe at the uppermost stage of the absorber.

【0009】[0009]

【作用】上記のように、本発明においては、空冷吸収器
と蒸発器を特殊な構造として、両者をエリミネータをは
さんで併設したことにより、冷房運転時と、暖房運転時
に冷媒液と濃溶液の液の流れを切換えることにより、暖
房時においても、溶液の循環が確保されて溶液が結晶化
せず、しかも暖房時において、冷媒の凝縮熱を2段で利
用でき非常に熱効率のよい空冷吸収冷温水機となった。
As described above, in the present invention, the air-cooled absorber and the evaporator have a special structure, and both are put side by side with the eliminator in between, so that the refrigerant liquid and the concentrated solution can be used during the cooling operation and the heating operation. By switching the flow of the liquid, the circulation of the solution is secured even during heating and the solution does not crystallize, and the heat of condensation of the refrigerant can be used in two stages during heating to absorb air with very high thermal efficiency. It became a water heater.

【0010】[0010]

【実施例】以下、本発明を図面を用いて具体的に説明す
るが、本発明はこれに限定されるものではない。 実施例1 図1は、本発明の単効用の空冷吸収冷温水機の一例で、
冷房時の操作を説明するための構成図であり、図2は暖
房時の操作を説明するための構成図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to the drawings, but the present invention is not limited thereto. Example 1 FIG. 1 is an example of a single-effect air-cooled absorption chiller-heater of the present invention,
It is a block diagram for explaining the operation at the time of cooling, and FIG. 2 is a block diagram for explaining the operation at the time of heating.

【0011】図1及び図2において、1は再生器、2は
空冷吸収器、3は空冷凝縮器、4は蒸発器、5は温水
器、6は熱交換器、7は溶液ポンプ、8は冷媒ポンプで
あり、空冷吸収器2はプレートフィン9を有する伝熱管
10からなり、伝熱管10は内部にスプレーノズル16
を有するスプレー管15が設けられている。蒸発機4は
垂直伝熱管13からなり、空冷吸収器2とはエリミネー
タ14で接続されており、エリミネータ14の下部に
は、冷媒と溶液を仕切る堰18が設けられている。1
1、12は切換え弁であり、17は液シールである。
1 and 2, 1 is a regenerator, 2 is an air-cooled absorber, 3 is an air-cooled condenser, 4 is an evaporator, 5 is a water heater, 6 is a heat exchanger, 7 is a solution pump, and 8 is It is a refrigerant pump, and the air-cooled absorber 2 is composed of a heat transfer tube 10 having a plate fin 9, and the heat transfer tube 10 has a spray nozzle 16 inside.
Is provided with a spray tube 15. The evaporator 4 comprises a vertical heat transfer tube 13, is connected to the air-cooled absorber 2 by an eliminator 14, and a weir 18 for partitioning the refrigerant and the solution is provided below the eliminator 14. 1
Reference numerals 1 and 12 are switching valves, and 17 is a liquid seal.

【0012】図面中に破線で示した経路は、弁等の操作
により、溶液、冷媒液、及び冷媒蒸気の流れが無いこと
を示しており、経路は存在している。次に、図1を用い
て単効用の冷房時について説明する。図1において、冷
媒ポンプ8と溶液ポンプ7は各々稼働している。蒸気用
三方弁11は再生器1から空冷凝縮器3方向に、液用三
方弁12は熱交換器6から空冷吸収器2最上部スプレー
管15の方向になっている。
The path shown by a broken line in the drawing indicates that there is no flow of the solution, the refrigerant liquid, and the refrigerant vapor due to the operation of the valve or the like, and the path exists. Next, a single effect cooling operation will be described with reference to FIG. In FIG. 1, the refrigerant pump 8 and the solution pump 7 are operating. The steam three-way valve 11 is directed from the regenerator 1 toward the air-cooled condenser 3, and the liquid three-way valve 12 is directed from the heat exchanger 6 toward the air-cooled absorber 2 uppermost spray pipe 15.

【0013】先ず、冷媒の流れを説明する。再生器1で
発生した冷媒蒸気は蒸気用三方弁11を通過し、空冷凝
縮器3に導かれ、空冷凝縮器3上部ヘッダに入る。空冷
凝縮器3で凝縮した冷媒液は、液シール17を経て蒸発
器4からの未蒸発冷媒液と合流し、冷媒ポンプ8吸い込
部に導かれ、冷媒ポンプ8により蒸発器4上部ヘッダに
送られる。送られた冷媒液は蒸発器4上部ヘッダから蒸
発器4垂直伝熱管13外面に沿って流下し、垂直管13
内を流れる冷水から熱を奪い蒸発する。蒸発した冷媒蒸
気は、エリミネータ14を通過して水平型空冷吸収器2
に向かい、ここで吸収溶液と接触し吸収溶液に吸収され
る。未蒸発冷媒液は蒸発器4下部の液溜まりから冷媒ポ
ンプ8吸い込みに導かれ、これを繰り返す。
First, the flow of the refrigerant will be described. The refrigerant vapor generated in the regenerator 1 passes through the vapor three-way valve 11, is guided to the air-cooled condenser 3, and enters the air-cooled condenser 3 upper header. The refrigerant liquid condensed in the air-cooled condenser 3 merges with the non-evaporated refrigerant liquid from the evaporator 4 through the liquid seal 17, is guided to the suction portion of the refrigerant pump 8, and is sent to the upper header of the evaporator 4 by the refrigerant pump 8. To be The sent refrigerant liquid flows down from the upper header of the evaporator 4 along the outer surface of the vertical heat transfer tube 13 of the evaporator 4,
It takes heat from the cold water flowing inside and evaporates. The evaporated refrigerant vapor passes through the eliminator 14 and the horizontal air-cooled absorber 2
Where it comes into contact with and is absorbed by the absorbing solution. The non-evaporated refrigerant liquid is guided from the liquid pool below the evaporator 4 to the suction of the refrigerant pump 8, and this is repeated.

【0014】次で、溶液の流れを説明する。再生器1で
濃縮された濃溶液は熱交換器6を経て、水平型空冷吸収
器2の最上部のスプレー管15に導かれる。吸収溶液は
吸収器2内で冷媒蒸気を吸収し、希釈された吸収溶液
は、水平伝熱管10底部を水平方向に沿って伝熱管10
開口部方向へ流れ、下位伝熱管のスプレー管15に行
き、伝熱管10内壁上部にスプレーされ冷媒蒸気に吸収
する。希釈された吸収溶液は吸収器2下部の溶液溜まり
に集まり、溶液ポンプ7吸い込みに流入し、溶液ポンプ
7より圧送され、熱交換器6を経て、再生器1に送ら
れ、以上を繰り返す。
Next, the flow of the solution will be described. The concentrated solution concentrated in the regenerator 1 is introduced into the uppermost spray pipe 15 of the horizontal air-cooled absorber 2 via the heat exchanger 6. The absorbing solution absorbs the refrigerant vapor in the absorber 2, and the diluted absorbing solution flows through the bottom of the horizontal heat transfer tube 10 along the horizontal direction.
It flows toward the opening, goes to the spray pipe 15 of the lower heat transfer pipe, is sprayed on the inner wall of the heat transfer pipe 10, and is absorbed by the refrigerant vapor. The diluted absorption solution collects in the solution pool below the absorber 2, flows into the suction of the solution pump 7, is pressure-fed by the solution pump 7, is fed to the regenerator 1 via the heat exchanger 6, and the above is repeated.

【0015】次に、図2を用いて単効用の暖房時(ヒー
トポンプ運転)を説明する。図2において、冷媒ポンプ
8は停止し、溶液ポンプ7は稼働している。蒸気用三方
弁11は再生器1から温水器5方向に、液用三方弁12
は熱交換器6から蒸発器4上部ヘッダの方向になってい
る。
Next, a single effect heating operation (heat pump operation) will be described with reference to FIG. In FIG. 2, the refrigerant pump 8 is stopped and the solution pump 7 is operating. The steam three-way valve 11 extends from the regenerator 1 toward the water heater 5 and the liquid three-way valve 12
Is from the heat exchanger 6 to the evaporator 4 upper header.

【0016】先ず、冷媒の流れを説明する。再生器1で
発生した冷媒蒸気は蒸気用三方弁11を通過して温水器
5に導かれ、温水伝熱管と接触し、凝縮する。凝縮した
冷媒液は温水器5下部より水平型空冷吸収器2の最上部
のスプレー管15に導かれる。送られた冷媒液は複数の
スプレー16から水平型空冷凝縮器伝熱管10内壁上部
にスプレーされ伝熱管10外部を流れる空気より熱を奪
い、蒸発する。未蒸発冷媒液は、水平伝熱管10底部を
水平方向に沿って伝熱管10開口部方向へ流れ、下位伝
熱管のスプレー管15に行き、伝熱管10内壁上部にス
プレーされ、蒸発する。蒸発した冷媒蒸気はエリミネー
タ14を通過して、蒸発器4に向かう。未蒸発の冷媒液
は吸収器2下部溶液溜まりに落ち、溶液ポンプ7吸い込
みに流入し、溶液ポンプ7により再生器1に送られ、こ
れを繰り返す。
First, the flow of the refrigerant will be described. The refrigerant vapor generated in the regenerator 1 passes through the vapor three-way valve 11 and is guided to the water heater 5, where it contacts the hot water heat transfer tube and is condensed. The condensed refrigerant liquid is guided from the lower part of the water heater 5 to the uppermost spray pipe 15 of the horizontal air-cooled absorber 2. The sent refrigerant liquid is sprayed from the plurality of sprays 16 onto the inner wall of the heat transfer tube 10 of the horizontal air-cooled condenser to remove heat from the air flowing outside the heat transfer tube 10 and evaporate. The non-evaporated refrigerant liquid flows through the bottom of the horizontal heat transfer tube 10 toward the opening of the heat transfer tube 10 along the horizontal direction, goes to the spray tube 15 of the lower heat transfer tube, and is sprayed on the inner wall of the heat transfer tube 10 and evaporated. The evaporated refrigerant vapor passes through the eliminator 14 and goes to the evaporator 4. The non-evaporated refrigerant liquid falls into the solution pool below the absorber 2, flows into the suction of the solution pump 7, is sent to the regenerator 1 by the solution pump 7, and this is repeated.

【0017】次で、溶液の流れを説明する。再生器1で
濃縮された濃溶液は熱交換器6を経て、液用三方弁12
を通過し、蒸発器4上部ヘッダに導かれる。吸収溶液は
蒸発器4上部ヘッダから蒸発器垂直伝熱管13外面に沿
って流下し、蒸発器4からの冷媒蒸気を吸収する。この
とき冷媒蒸気は吸収されるとともに潜熱を放出し、この
熱量は垂直伝熱管13内を流れる温水に奪われる。冷媒
蒸気を吸収して希釈された吸収溶液は蒸発器4下部溶液
溜まりに落ち、せき18から吸収器2下部液溜まり側に
オーバーフローし、前記未蒸発冷媒液と合流し溶液ポン
プ7に流入する。さらに、溶液ポンプ7により再生器1
に圧送され、以上を繰り返す。以上は単効用の吸収冷温
水機について説明したが、二重効用の吸収冷温水機につ
いても同様に適用可能である。
Next, the flow of the solution will be described. The concentrated solution concentrated in the regenerator 1 passes through the heat exchanger 6 and the three-way valve for liquid 12
And is led to the upper header of the evaporator 4. The absorbing solution flows down from the upper header of the evaporator 4 along the outer surface of the evaporator vertical heat transfer tube 13 and absorbs the refrigerant vapor from the evaporator 4. At this time, the refrigerant vapor is absorbed and releases latent heat, and the amount of this heat is taken by the hot water flowing in the vertical heat transfer tube 13. The absorption solution diluted by absorbing the refrigerant vapor falls into the solution pool at the bottom of the evaporator 4, overflows from the weir 18 to the liquid pool at the bottom of the absorber 2, merges with the unevaporated refrigerant liquid, and flows into the solution pump 7. Furthermore, the regenerator 1 is driven by the solution pump 7.
It is pumped to and repeated above. Although the above description has been given of the single-effect absorption chiller-heater, the same effect can be applied to the double-effect absorption chiller-heater.

【0018】[0018]

【発明の効果】本発明によれば暖房時においても溶液ポ
ンプを運転して溶液循環を確保でき、溶液循環系内で溶
液が結晶化するのを防止できると共に、暖房時の熱効率
の非常によい空冷吸収冷温水機が得られた。
EFFECTS OF THE INVENTION According to the present invention, the solution pump can be operated even during heating to ensure the solution circulation, the solution can be prevented from crystallizing in the solution circulation system, and the thermal efficiency during heating is very good. An air-cooled absorption chiller-heater was obtained.

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

【図1】本発明の単効用の空冷吸収冷温水機で冷房時の
操作を説明する構成図。
FIG. 1 is a configuration diagram illustrating an operation during cooling in a single-effect air-cooled absorption chiller-heater according to the present invention.

【図2】図1で暖房時の操作を説明する構成図。FIG. 2 is a configuration diagram illustrating an operation during heating in FIG.

【符号の説明】[Explanation of symbols]

1:再生器、2:空冷吸収器、3:空冷凝縮器、4:蒸
発器、5:温水器、6:熱交換器、7:溶液ポンプ、
8:冷媒ポンプ、9:プレートフィン、10:水平伝熱
管、11:蒸気三方弁、12:溶液三方弁、13:垂直
伝熱管、14:エリミネータ、15:スプレー管、1
6:スプレーノズル、17:液シール、18:せき
1: Regenerator, 2: Air-cooled absorber, 3: Air-cooled condenser, 4: Evaporator, 5: Water heater, 6: Heat exchanger, 7: Solution pump,
8: Refrigerant pump, 9: Plate fin, 10: Horizontal heat transfer tube, 11: Steam three-way valve, 12: Solution three-way valve, 13: Vertical heat transfer tube, 14: Eliminator, 15: Spray tube, 1
6: Spray nozzle, 17: Liquid seal, 18: Cough

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 再生器、空冷吸収器、空冷凝縮器、蒸発
器及び再生器と蒸気配管で結んだ温水器を有すると共
に、それらを連絡する溶液ポンプ、冷媒ポンプと切替え
弁を有する溶液通路及び冷媒通路を有し、水を冷媒の主
成分とする空冷吸収冷温水機において、前記空冷吸収器
は、複数の水平伝熱管からなり、該水平伝熱管は伝熱管
外にプレートフィンを設け、伝熱管内には伝熱管内壁上
部に液体をスプレーする複数のスプレーノズルを有する
スプレー管を設けて構成され、前記蒸発器は、内部に冷
温水を通し、外部に冷媒液又は濃溶液を供給できる構造
の垂直伝熱管を有し、前記空冷吸収器と蒸発器とはエリ
ミネータで分離されていることを特徴とする空冷吸収冷
温水機。
1. A regenerator, an air-cooled absorber, an air-cooled condenser, an evaporator and a water heater connected to the regenerator by a steam pipe, and a solution pump connecting them, a solution pump having a refrigerant pump and a switching valve, and In an air-cooled absorption chiller-heater having a refrigerant passage and water as a main component of the refrigerant, the air-cooled absorber is composed of a plurality of horizontal heat transfer tubes, and the horizontal heat transfer tubes are provided with plate fins outside the heat transfer tubes. In the heat pipe, a spray pipe having a plurality of spray nozzles for spraying a liquid is provided on the upper part of the inner wall of the heat transfer pipe, and the evaporator has a structure capable of passing cold / hot water inside and supplying a refrigerant liquid or a concentrated solution to the outside. 2. An air-cooled absorption chiller-heater having a vertical heat transfer tube, wherein the air-cooled absorber and the evaporator are separated by an eliminator.
【請求項2】 前記空冷吸収冷温水機の運転方法におい
て、冷房運転時には、溶液ポンプと冷媒ポンプを運転し
て、また再生器からの冷媒蒸気を空冷凝縮器に導き、温
水器には行かないよう遮断して吸収サイクルを形成し、
暖房運転時には、冷媒ポンプを停止状態として、再生器
からの溶液を蒸発器スプレーヘッダーに供給し、また再
生器から空冷凝縮器への冷媒蒸気経路を遮断するととも
に、再生器から温水器への冷媒蒸気経路を開放し、温水
器内温水伝熱管と接触させ、温水器で凝縮した冷媒液を
吸収器の最上段部のスプレー管に供給することを特徴と
する請求項1記載の空冷吸収冷温水機の運転方法。
2. In the operation method of the air-cooled absorption chiller-heater, during the cooling operation, the solution pump and the refrigerant pump are operated, and the refrigerant vapor from the regenerator is guided to the air-cooled condenser and does not go to the water heater. Shut off to form an absorption cycle,
During heating operation, the refrigerant pump is stopped, the solution from the regenerator is supplied to the evaporator spray header, and the refrigerant vapor path from the regenerator to the air-cooled condenser is cut off, and the refrigerant from the regenerator to the water heater is also cut off. The air-cooled absorption cold / hot water according to claim 1, wherein the steam path is opened, brought into contact with the hot water heat transfer pipe in the water heater, and the refrigerant liquid condensed in the water heater is supplied to the spray pipe at the uppermost stage of the absorber. How to operate the machine.
JP28982293A 1993-10-27 1993-10-27 Air-cooled absorption hot and chilled water generator and operating method therefor Pending JPH07120095A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28982293A JPH07120095A (en) 1993-10-27 1993-10-27 Air-cooled absorption hot and chilled water generator and operating method therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28982293A JPH07120095A (en) 1993-10-27 1993-10-27 Air-cooled absorption hot and chilled water generator and operating method therefor

Publications (1)

Publication Number Publication Date
JPH07120095A true JPH07120095A (en) 1995-05-12

Family

ID=17748222

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28982293A Pending JPH07120095A (en) 1993-10-27 1993-10-27 Air-cooled absorption hot and chilled water generator and operating method therefor

Country Status (1)

Country Link
JP (1) JPH07120095A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115388696A (en) * 2022-08-24 2022-11-25 北京建筑大学 Interdigitated honeycomb flat plate overflow heat exchanger for three-phase solution energy storage and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115388696A (en) * 2022-08-24 2022-11-25 北京建筑大学 Interdigitated honeycomb flat plate overflow heat exchanger for three-phase solution energy storage and method

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