JPH07120094A - Air cooled absorption cooler/heater and operating method therefor - Google Patents

Air cooled absorption cooler/heater and operating method therefor

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Publication number
JPH07120094A
JPH07120094A JP28982193A JP28982193A JPH07120094A JP H07120094 A JPH07120094 A JP H07120094A JP 28982193 A JP28982193 A JP 28982193A JP 28982193 A JP28982193 A JP 28982193A JP H07120094 A JPH07120094 A JP H07120094A
Authority
JP
Japan
Prior art keywords
air
cooled
refrigerant
heat transfer
evaporator
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
JP28982193A
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 JP28982193A priority Critical patent/JPH07120094A/en
Publication of JPH07120094A publication Critical patent/JPH07120094A/en
Pending legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To efficiently heat/cool the air by switching an operating cycle at the time of cooling, heating by forming an air-cooled absorber and an evaporator of a plurality of horizontal heat transfer tubes, providing plate fins out of the tubes, and providing a spray tube having a plurality of spray nozzles for spraying liquid to upper inner walls of the tubes. CONSTITUTION:At the time of single-effect cooling, a refrigerant pump 8 and a solution pump 7 are operated, a vapor three-way valve 11 is opened from a regenerator 1 toward an air-cooled condenser 3, a liquid three-way valve 13 is opened from the pump 8 toward an uppermost spray tube 16 of an evaporator 4, a liquid three-way valve 14 is opened from a heat exchanger 6 toward the valve 14, the valve 14 is opened toward a minimum spray tube 16 of an air-cooled absorber 2, and a liquid two-way valve 15 is opened. Since the absorber 2 and the evaporator 4 are formed as described above, an air-cooled aim absorption cooler/heater in which the efficiency of the exchanger 6 can be raised and the air can be directly cooled or heated can be reduced in size, and at the time of heating, warm air can be efficiently manufactured by using refrigerant vapor and heating solution from the regenerator 1.

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、吸収冷暖房機に係り、
特に冷暖房を切替えて冷風あるいは温風を製造する空冷
吸収冷暖房機とその運転方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption cooling / heating machine,
In particular, the present invention relates to an air-cooling absorption cooling / heating machine that switches cooling / heating to produce cold air or warm air and its operating method.

【0002】[0002]

【従来の技術】従来から、水あるいは主成分が水である
冷媒を用いて、空気を冷やして冷風を製造するタイプの
冷暖房機は、実公昭52−44929号公報、特開平5
−60414号公報等にしめされ公知である。また、従
来機の冷房時のサイクルは、たとえば、特公昭46−4
0073号公報に、暖房時のサイクルは、実公昭52−
44929号公報に記載されている。これら従来機の例
は、水冷却であり、冷房/暖房の切替えは冷却水を流す
かどうかで行う。冷却水を流さなければ、凝縮器、吸収
器からの放熱がなくなり、再生器内圧が上昇し、液シー
ルが破れ、冷媒蒸気が直接蒸発器に入り、暖房が可能に
なる。空気で吸収器、凝縮器を冷却する空冷式の場合、
熱交換器の効率の問題から、熱交換器は結果的に大きな
ものになっている。
2. Description of the Related Art Conventionally, an air conditioner of a type that cools air by using water or a refrigerant whose main component is water to produce cold air is disclosed in Japanese Utility Model Publication No. 52-44929.
It is publicly known as disclosed in Japanese Patent Publication No.-60414. The cycle for cooling the conventional machine is, for example, Japanese Patent Publication No. 46-4.
In the publication No. 0073, the heating cycle is described in Japanese Utility Model Publication No. 52-
It is described in Japanese Patent No. 44929. Examples of these conventional machines are water cooling, and switching between cooling and heating is performed depending on whether or not cooling water flows. If cooling water is not supplied, heat is no longer released from the condenser and absorber, the internal pressure of the regenerator rises, the liquid seal is broken, and refrigerant vapor directly enters the evaporator, enabling heating. In the case of air-cooled type that cools the absorber and condenser with air,
Due to heat exchanger efficiency issues, heat exchangers have consequently become larger.

【0003】[0003]

【発明が解決しようとする課題】本発明は、上記のよう
な従来技術の問題点を解消し、空冷式において効率のよ
い熱交換器を用いて、冷房、暖房時に運転サイクルを切
換えることにより効率よく冷暖房が行える空冷吸収冷暖
房機とその運転方法を提供することを課題とする。
DISCLOSURE OF THE INVENTION The present invention solves the problems of the prior art as described above, and uses an efficient heat exchanger in the air cooling system to switch the operation cycle during cooling and heating, thereby improving efficiency. An object of the present invention is to provide an air-cooled absorption cooling / heating machine that can be well cooled and heated, and an operating method thereof.

【0004】[0004]

【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暖房機において、前記空冷吸
収器と蒸発器とは、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ると共に、
空冷凝縮器とは別に、温風凝縮器を蒸発器と同一の冷、
温風の流水系統の下流側に設置したものである。
In order to solve the above problems, according to the present invention, a regenerator, an air-cooled absorber, an air-cooled condenser, an evaporator and a solution pump for connecting them, a solution having a refrigerant pump and a switching valve. In an air-cooling absorption cooling / heating machine that has a passage and a refrigerant passage, and water is a main component of the refrigerant, the air-cooling absorber and the evaporator are composed of a plurality of horizontal heat transfer tubes, and the horizontal heat transfer tubes are plates outside the heat transfer tubes. A fin is provided, and in the heat transfer tube, a spray tube having a plurality of spray nozzles for spraying a liquid is provided on the inner wall of the heat transfer tube, and
Separately from the air-cooled condenser, the warm air condenser is the same cooling as the evaporator,
It was installed on the downstream side of the warm air flow system.

【0005】また、本発明では、前記空冷吸収冷暖房機
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、温風凝縮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、再生器から温風凝縮器への冷
媒蒸気経路を開放し、冷媒蒸気と温風とを伝熱管を介し
て接触させ、温風凝縮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 for operating the air-cooled absorption cooling / heating machine, 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 to condense warm air. In the heating operation, the refrigerant pump is stopped, the solution from the regenerator is supplied to the evaporator spray header, and the refrigerant from the regenerator to the air-cooled condenser is shut off to prevent it from going to the regenerator. In addition to shutting off the vapor path, open the refrigerant vapor path from the regenerator to the warm air condenser to bring the refrigerant vapor and warm air into contact with each other via the heat transfer tube, and absorb the refrigerant liquid condensed in the warm air condenser. Is to be supplied to the spray tube at the top of the.

【0006】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、空冷吸収器は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、また、蒸発器は水平伝熱管とし、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
て被冷却空気(冷風)と接触させ、伝熱管内に冷媒液を
供給し、伝熱管内への冷媒供給に当たっては、伝熱管内
に冷媒液を導くとともに、複数のスプレーノズルから伝
熱管内壁上部に冷媒液をスプレーするスプレー管を設け
た構造とし、空冷凝縮器とは別に温風凝縮器を設け、蒸
発器と温風凝縮器とは、冷風/温風の同一の流れ系統に
設置し、流れ方向で蒸発器を上流側としたものである。
As described above, according to the present invention, in an air-cooled absorption air conditioner that uses water as the main component of the refrigerant and uses an aqueous solution of Li salt or the like as the absorption solution, the air-cooled absorber has heat transfer tubes 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 with a spray tube that sprays the solution from multiple spray nozzles onto the inner wall of the heat transfer tube is used as the absorber.The evaporator is a horizontal heat transfer tube, and plate fins are provided outside the heat transfer tube for heat transfer. The area is expanded to contact the air to be cooled (cold air) to supply the refrigerant liquid into the heat transfer tube. When supplying the refrigerant into the heat transfer tube, while guiding the refrigerant liquid into the heat transfer tube, the multiple spray nozzles are used. Cool the upper part of the inner wall of the heat transfer tube. It has a structure with a spray pipe for spraying the liquid, a warm air condenser is installed separately from the air-cooled condenser, and the evaporator and the warm air condenser are installed in the same cold / warm air flow system, and the flow direction is Therefore, the evaporator is on the upstream side.

【0007】また、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、(再生器の冷媒蒸気が温風凝縮器には行
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
器から温風凝縮器への冷媒蒸気経路を開放し、冷媒蒸気
と温風とを伝熱管を介して接触させ、温風凝縮器で凝縮
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。
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 so that the refrigerant vapor of the regenerator does not go to the hot air condenser. During the 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. At the same time, the refrigerant vapor path from the regenerator to the warm air condenser is opened, the refrigerant vapor and the warm air are brought into contact with each other via the heat transfer tube, and the refrigerant liquid condensed by the warm air condenser is placed at the uppermost stage of the absorber. Supply to spray tube.

【0008】[0008]

【作用】本発明によれば、上記のような空冷吸収器及び
蒸発器の構成としたことにより、熱交換器の効率を上昇
でき、直接空気を冷暖できる空冷吸収冷暖房機を小型化
できると共に、暖房運転時には再生器からの冷媒蒸気と
加熱溶液を用いて蒸発器と温風凝縮器により、効率よく
温風を製造できるものである。
According to the present invention, the air-cooling absorber and evaporator having the above-described configurations can increase the efficiency of the heat exchanger and can downsize the air-cooling absorption air conditioner that can directly heat and cool the air. During the heating operation, the hot air can be efficiently produced by the evaporator and the hot air condenser using the refrigerant vapor from the regenerator and the heating solution.

【0009】[0009]

【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暖房機の一例で、
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 shows an example of a single-effect air-cooled absorption air conditioner 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.

【0010】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は温風凝
縮器、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及び蒸発器4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には、中にス
プレーノズル17を有するスプレー管16が設置されて
いる。11〜15は切換え弁であり、18は蒸発蒸気の
通る蒸気管、19は溶液戻り管で、20は液シールであ
る。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。
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 hot air condenser, 6 is a heat exchanger, 7 is a solution pump, 8 is a refrigerant pump, and the air-cooled absorber 2 and the evaporator 4 are plate fins 9.
The heat transfer tube 10 is provided with a spray tube 16 having a spray nozzle 17 therein. 11 to 15 are switching valves, 18 is a vapor pipe through which vaporized vapor passes, 19 is a solution return pipe, and 20 is a liquid seal. The route shown by the broken line in the drawing is
There is no flow of solution, refrigerant liquid, or refrigerant vapor, and the path exists.

【0011】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13は冷媒ポンプ8
から蒸発器4最上部スプレー管16方向に、液用三方弁
12は熱交換器6から液用三方弁14方向に液用三方弁
14は12から空冷吸収器2最上部スプレー管16方向
に、液用二方弁15は開に各々なっている。
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 to the air-cooled condenser 3 and the liquid three-way valve 13 is the refrigerant pump 8
From the evaporator 4 to the uppermost spray pipe 16 direction, the liquid three-way valve 12 from the heat exchanger 6 to the liquid three-way valve 14 direction, the liquid three-way valve 12 from 12 to the air-cooled absorber 2 uppermost spray pipe 16 direction, The liquid two-way valves 15 are each open.

【0012】次で、図1を用いて冷媒の流れを説明す
る。再生器で発生した冷媒蒸気は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20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最上部スプレー管1
6に送られる。送られた冷媒液は蒸発器4水平伝熱管1
0外周を流れる冷風と熱交換し蒸発する。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16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21を通過し、蒸気管1
8及び溶液戻り管19を通過し空冷吸収器2に導かれ、
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弁15を経て、冷
媒ポンプ8吸い込みに導かれ、空冷凝縮器3からの冷媒
液とともに再び蒸発器4最上部スプレー管16に導か
れ、これを繰り返す。
Next, the flow of the refrigerant will be described with reference to FIG. The refrigerant vapor generated in the regenerator passes through 11 and is guided to the air-cooled condenser 3 to enter the upper header of the air-cooled condenser 3. The refrigerant liquid condensed in the air-cooled condenser 3 merges with the non-evaporated refrigerant liquid from the evaporator 4 via the liquid seal 20, is guided to the suction portion of the refrigerant pump 8, and the refrigerant pump 8 sprays the uppermost spray pipe 1 of the evaporator 4.
Sent to 6. The sent refrigerant liquid is the evaporator 4 Horizontal heat transfer tube 1
Heat is exchanged with the cold air flowing around the outer circumference to evaporate. The non-evaporated refrigerant liquid flows through the bottom of the horizontal heat transfer tube 10 along the horizontal direction.
It flows toward the opening, goes to the spray tube 16 of the lower heat transfer tube, is sprayed on the inner wall of the heat transfer tube 10, and evaporates. The vaporized refrigerant vapor passes through the eliminator 21, and the vapor pipe 1
8 and the solution return pipe 19 to be guided to the air-cooled absorber 2,
Here, it comes into contact with the absorption solution and is absorbed by the absorption solution. The non-evaporated refrigerant liquid is guided from the liquid pool under the evaporator 4 through the valve 15 to the suction of the refrigerant pump 8 and again to the uppermost spray pipe 16 of the evaporator 4 together with the refrigerant liquid from the air-cooled condenser 3. repeat.

【0013】次に、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、弁12および弁14を
経て空冷吸収器2最上部スプレー管16に導かれる。吸
収溶液は空冷吸収器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
16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により圧送され、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 led to the uppermost spray pipe 16 of the air-cooled absorber 2 via the heat exchanger 6, the valve 12 and the valve 14. The absorbing solution absorbs the refrigerant vapor in the air-cooled absorber 2, and the diluted absorbing solution flows horizontally along the bottom of the horizontal heat transfer tube 10 toward the opening of the heat transfer tube 10 and then into the spray tube 16 of the lower heat transfer tube. It goes, is sprayed on the inner wall of the heat transfer tube 10, and is absorbed by the refrigerant vapor. The diluted absorption solution gathers in the solution pool below the absorber 2 and flows into the suction of the solution pump 7,
The solution is pumped under pressure by the solution pump 7, passed through the heat exchanger 6, and sent to the regenerator 1, and the above is repeated.

【0014】次に、図2を用いて単効用の暖房時を説明
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
温風凝縮器5方向に、液用三方弁12は熱交換器6から
液用三方弁13方向に、液用三方弁13は弁12から蒸
発器4最上部スプレー管16方向に、液用三方弁14は
温風凝縮器5から空冷吸収器2最上部スプレー管16方
向に、液用二方弁15は閉に、各々なっている。
Next, a single effect heating 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 is from the regenerator 1 toward the warm air condenser 5, the liquid three-way valve 12 is from the heat exchanger 6 toward the liquid three-way valve 13, and the liquid three-way valve 13 is from the valve 12 to the evaporator 4. In the direction of the upper spray pipe 16, the liquid three-way valve 14 is in the direction from the hot air condenser 5 to the uppermost spray pipe 16 of the air-cooled absorber 2, and the liquid two-way valve 15 is closed.

【0015】次で、図2を用いて冷媒の流れを説明す
る。再生器1で発生した冷媒蒸気は弁11を通過し温風
凝縮器5に導かれ温風凝縮器5上部ヘッダに入る。温風
凝縮器5で伝熱管外周を流れる温風と熱交換し凝縮した
冷媒液は、液シール20を経て弁14を通過し空冷吸収
器2最上部スプレー管16に導かれる。導かれた冷媒液
は空冷吸収器2水平伝熱管10外周を流れる熱源空気と
熱交換し蒸発する。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
位伝熱管スプレー管16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蒸気管1
8を通過し蒸発器4に導かれ、ここで蒸発器4水平伝熱
管10内を流れる吸収溶液と接触し吸収溶液に吸収され
る。未蒸発冷媒液は空冷吸収器2下部溶液溜まりに集ま
り、溶液戻り管19からの吸収溶液(稀溶液)と一緒に
溶液ポンプ7吸い込みに流入し、溶液ポンプ7により圧
送され、熱交換器6を経て、再生器1に戻り、以上を繰
り返す。
Next, the flow of the refrigerant will be described with reference to FIG. The refrigerant vapor generated in the regenerator 1 passes through the valve 11 and is guided to the warm air condenser 5 and enters the warm air condenser 5 upper header. The refrigerant liquid that has exchanged heat with the hot air flowing through the outer circumference of the heat transfer tube in the hot air condenser 5 and condensed passes through the valve 14 through the liquid seal 20 and is guided to the uppermost spray pipe 16 of the air-cooled absorber 2. The introduced refrigerant liquid exchanges heat with the heat source air flowing around the outer circumference of the air-cooling absorber 2 horizontal heat transfer tube 10 and evaporates. 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 lower heat transfer tube spray tube 16, is sprayed on the inner wall of the heat transfer tube 10, and evaporates. Evaporated refrigerant vapor is vapor pipe 1
8 is guided to the evaporator 4, where it comes into contact with the absorbing solution flowing in the horizontal heat transfer tube 10 of the evaporator 4 and is absorbed by the absorbing solution. The non-evaporated refrigerant liquid collects in the solution pool at the lower part of the air-cooled absorber 2, flows into the suction of the solution pump 7 together with the absorbing solution (diluted solution) from the solution return pipe 19, is pumped by the solution pump 7, and is passed through the heat exchanger 6. After that, it returns to the regenerator 1 and repeats the above.

【0016】次に、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、弁12および弁13を
経て蒸発器4最上部スプレー管16に導かれる。吸収溶
液は蒸発器4水平伝熱管10内で冷媒蒸気を吸収し、冷
媒が放出した潜熱の熱量を、蒸発器4水平伝熱管10外
周を流れる温風に与える。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16に行き、伝熱管1
0内壁上部にスプレーされ蒸発する。希釈された吸収溶
液は蒸発器4下部液溜まりに集まり、溶液戻り管19の
上端からオーバーフローし、空冷吸収器2下部溶液溜ま
りに導かれ、未蒸発冷媒液と一緒に溶液ポンプ7吸い込
みに流入し、再生器1へ圧送られ、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 led to the uppermost spray pipe 16 of the evaporator 4 via the heat exchanger 6, the valve 12 and the valve 13. The absorbing solution absorbs the refrigerant vapor in the horizontal heat transfer tube 10 of the evaporator 4 and gives the amount of latent heat released by the refrigerant to the warm air flowing around the outer heat transfer tube 10 of the evaporator 4. The diluted absorbing solution flows through the bottom of the horizontal heat transfer tube 10 along the horizontal direction toward the opening of the heat transfer tube 10 and then to the spray tube 16 of the lower heat transfer tube, where the heat transfer tube 1
0 is sprayed on the inner wall and evaporated. The diluted absorption solution collects in the lower liquid pool of the evaporator 4, overflows from the upper end of the solution return pipe 19, is guided to the lower liquid pool of the air-cooled absorber 2, and flows into the suction of the solution pump 7 together with the non-evaporated refrigerant liquid. , Is pressure fed to the regenerator 1, and the above is repeated.

【0017】なお、蒸気管18及び溶液戻り管19は条
件次第で兼用可能(溶液戻り管を省略する)である。つ
まり、冷房時に蒸発器18下部において、蒸気管上端部
が突き出し、未蒸発冷媒が溜まる様につくられ、暖房時
は前記蒸気管18上端部から吸収溶液がオーバーフロー
し、蒸気管18を降下し空冷吸収器2へ行き、空冷吸収
器2からの冷媒蒸気が蒸発管18を、降下吸収溶液とす
れ違い、上昇出来るように、蒸気管18の太さを十分に
したとき、兼用が可能である。
The vapor pipe 18 and the solution return pipe 19 can be used together depending on the conditions (the solution return pipe is omitted). That is, at the time of cooling, the upper end of the steam pipe is made to protrude in the lower part of the evaporator 18 so that the non-evaporated refrigerant is accumulated. When the vapor pipe 18 has a sufficient thickness so that the refrigerant vapor from the air-cooled absorber 2 can pass through the evaporator pipe 18 with the descending absorbing solution and rise, the dual use is possible.

【0018】図3に冷温風ファンの風向きを示す。蒸発
器4と温風凝縮器5とは、冷風/温風の同一の流れ系統
に設置され、さらに蒸発器4を上流側に、温風凝縮器5
を下流側に設置することを特徴とする。また、上記にお
いては単効用について説明したが二重効用のものについ
ても同様に適用できる。
FIG. 3 shows the wind direction of the cool and warm air fan. The evaporator 4 and the hot air condenser 5 are installed in the same flow system of cold air / warm air, and the evaporator 4 is placed upstream and the hot air condenser 5 is installed.
Is installed on the downstream side. Further, in the above description, a single effect is explained, but a double effect can be similarly applied.

【0019】[0019]

【発明の効果】本発明によれば、効率のよい熱交換器を
用いて、冷房、暖房時に運転サイクルを切換えることに
より効率よく冷暖房が行える空冷吸収冷暖房機を得るこ
とができた。
According to the present invention, it is possible to obtain an air-cooled absorption cooling / heating machine that can efficiently perform cooling / heating by switching operation cycles during cooling / heating using a highly efficient heat exchanger.

【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暖房機で冷房時の
操作を説明するための構成図。
FIG. 1 is a configuration diagram for explaining an operation during cooling in a single-effect air-cooled absorption cooling / heating machine of the present invention.

【図2】図1の冷暖房機で暖房時の操作を説明するため
の構成図。
FIG. 2 is a configuration diagram for explaining an operation during heating in the air conditioner of FIG.

【図3】冷温風ファンの風向きを示す概略図。FIG. 3 is a schematic view showing a wind direction of a cold / hot air fan.

【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:温風凝縮器、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:伝熱
管10、11〜15:弁、16:スプレー管、17:ス
プレーノズル、18:蒸気管、19:溶液戻り管、2
0:液シール、21:エリミネータ
1: Regenerator, 2: Air-cooled absorber, 3: Air-cooled condenser, 4: Evaporator, 5: Warm air condenser, 6: Heat exchanger, 7: Solution pump, 8: Refrigerant pump, 9: Plate fin, 10: Heat transfer tube 10, 11-15: Valve, 16: Spray tube, 17: Spray nozzle, 18: Steam tube, 19: Solution return tube, 2
0: Liquid seal, 21: Eliminator

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暖房機において、前記空冷吸収
器と蒸発器とは、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ると共に、空
冷凝縮器とは別に、温風凝縮器を蒸発器と同一の冷、温
風の流水系統の下流側に設置したことを特徴とする空冷
吸収冷暖房機。
1. A regenerator, an air-cooled absorber, an air-cooled condenser, an evaporator, a solution pump connecting them, a solution passage having a refrigerant pump and a switching valve, and a refrigerant passage, and water as a main component of the refrigerant. In the air-cooled absorption air conditioner / heater, the air-cooled absorber and the evaporator are composed of a plurality of horizontal heat transfer tubes, the horizontal heat transfer tubes are provided with plate fins outside the heat transfer tubes, and liquid is provided inside the heat transfer tubes at the upper part of the heat transfer tubes. In addition to being equipped with a spray pipe with multiple spray nozzles for spraying, in addition to the air-cooled condenser, a warm air condenser was installed downstream of the same cold and warm air flow system as the evaporator. A characteristic air-cooled absorption air conditioner.
【請求項2】 前記空冷吸収冷暖房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
風凝縮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、再生器から温風凝縮器への冷媒蒸気経路を開放
し、冷媒蒸気と温風とを伝熱管を介して接触させ、温風
凝縮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
冷暖房機の運転方法。
2. In the method for operating an air-cooled absorption cooling / heating machine, during a cooling operation, a solution pump and a refrigerant pump are operated, and refrigerant vapor from a regenerator is led to an air-cooled condenser and not to a warm air condenser. 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 path from the regenerator to the air-cooled condenser is shut off. In addition, the refrigerant vapor path from the regenerator to the warm air condenser is opened, the refrigerant vapor and the warm air are brought into contact with each other via the heat transfer tube, and the refrigerant liquid condensed in the warm air condenser is placed at the uppermost stage of the absorber. The method for operating an air-cooled absorption cooling / heating machine according to claim 1, characterized in that the air is supplied to the spray pipe.
JP28982193A 1993-10-27 1993-10-27 Air cooled absorption cooler/heater and operating method therefor Pending JPH07120094A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28982193A JPH07120094A (en) 1993-10-27 1993-10-27 Air cooled absorption cooler/heater and operating method therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28982193A JPH07120094A (en) 1993-10-27 1993-10-27 Air cooled absorption cooler/heater and operating method therefor

Publications (1)

Publication Number Publication Date
JPH07120094A true JPH07120094A (en) 1995-05-12

Family

ID=17748210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28982193A Pending JPH07120094A (en) 1993-10-27 1993-10-27 Air cooled absorption cooler/heater and operating method therefor

Country Status (1)

Country Link
JP (1) JPH07120094A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6254078B1 (en) 1998-12-17 2001-07-03 Ricoh Company, Ltd. Automatic document feeder for an image forming apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6254078B1 (en) 1998-12-17 2001-07-03 Ricoh Company, Ltd. Automatic document feeder for an image forming apparatus

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