JPS58203362A - Absorption type refrigerator - Google Patents

Absorption type refrigerator

Info

Publication number
JPS58203362A
JPS58203362A JP57084739A JP8473982A JPS58203362A JP S58203362 A JPS58203362 A JP S58203362A JP 57084739 A JP57084739 A JP 57084739A JP 8473982 A JP8473982 A JP 8473982A JP S58203362 A JPS58203362 A JP S58203362A
Authority
JP
Japan
Prior art keywords
cooling water
pipe
solution
heat
absorber
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
JP57084739A
Other languages
Japanese (ja)
Inventor
昭典 山口
杉本 滋郎
町沢 健司
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP57084739A priority Critical patent/JPS58203362A/en
Publication of JPS58203362A publication Critical patent/JPS58203362A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、太陽熱や排熱のごとく、入熱が不安定な熱源
を溶液の加熱源として利用するものにおいて、冷凍機自
体に蓄熱機能をもたせた吸収式冷凍機に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigerator that uses a heat source with unstable heat input, such as solar heat or waste heat, as a heating source for a solution, and in which the refrigerator itself has a heat storage function. .

・太陽熱は、天候の変動、太陽光線の入射角、風速など
の影響を受は易く、冷凍機への入熱が不安定である。ま
た、原動機の排ガス等が有する排熱も、これを排出する
側の運転状態などによって変動する。
・Solar heat is easily affected by weather fluctuations, the angle of incidence of sunlight, wind speed, etc., and the heat input to the refrigerator is unstable. Furthermore, the exhaust heat contained in the exhaust gas of the prime mover also varies depending on the operating conditions of the side that discharges it.

従来、かかる不安定な熱源を加熱源として利用する吸収
式冷凍機では、蓄熱槽を別に設置するようにしていた。
Conventionally, in absorption refrigerators that utilize such unstable heat sources as heating sources, a heat storage tank has been installed separately.

従って、従来技術では設備が大型化し、かつ設備費が嵩
む欠点があった。
Therefore, the conventional technology has the disadvantage that the equipment becomes large and the equipment cost increases.

本発明の目的は、前記従来技術の欠点をなくし、冷凍機
自体に蓄熱機能を有する吸収式冷凍機を提供するにある
SUMMARY OF THE INVENTION An object of the present invention is to eliminate the drawbacks of the prior art and provide an absorption refrigerator having a heat storage function in the refrigerator itself.

本発明の特徴は、吸収器を通って凝縮器に冷却水を挿通
する冷却水管に、入熱がありかつ無負荷時に凝縮器へ直
接冷却水をバイパスさせ得る冷却水バイパスを設けたと
ころにあシ、入熱がありながら一時的な無負荷時に運転
を継続して行い、溶液の濃度を高めることで蓄熱し得る
ようにしたことによって、前記目的を確実に達成するこ
とができたものである。
A feature of the present invention is that the cooling water pipe that passes cooling water through the absorber and into the condenser is provided with a cooling water bypass that can directly bypass the cooling water to the condenser when there is heat input and no load. The above objective was reliably achieved by continuing to operate during temporary no-load conditions despite heat input, and by increasing the concentration of the solution so that heat could be stored. .

以下、本発明を図面に基づいて説明する。Hereinafter, the present invention will be explained based on the drawings.

図は本発明吸収式冷凍機の一実施例を示すもので、太陽
熱の集熱器1、再生器3、凝縮器5、蒸発器7、吸収器
9、溶液循環ポンプ13、熱交換器14、冷却水バイパ
ス15を備えて構成されている。
The figure shows an embodiment of the absorption refrigerator of the present invention, which includes a solar heat collector 1, a regenerator 3, a condenser 5, an evaporator 7, an absorber 9, a solution circulation pump 13, a heat exchanger 14, It is configured to include a cooling water bypass 15.

前記集熱器1には、加熱媒体である温水を循環させる加
熱媒体管2が連結されておシ、該加熱媒体管2は再生器
3に挿入されている。
A heating medium pipe 2 for circulating hot water as a heating medium is connected to the heat collector 1, and the heating medium pipe 2 is inserted into a regenerator 3.

前記再生器3は、7111熱媒体管2内を流れる温水に
よシ稀溶液を加熱し、該稀溶液を力ロ熱することによっ
て発生する冷媒蒸気を、冷媒蒸気管4を通じて凝縮器5
に送シ込む。
The regenerator 3 heats the dilute solution with hot water flowing in the 7111 heat medium pipe 2, and transfers the refrigerant vapor generated by forcefully heating the dilute solution to the condenser 5 through the refrigerant vapor pipe 4.
Send it to.

前記凝縮器5には、冷却水管10が導入されている。こ
の凝縮器5では、冷却水管10内を流れて蒸発器7へ送
るようになっている。      (前記蒸発器7は、
冷水を循環させる冷水管8を備えている。この蒸発器7
では、冷媒液が前記冷水管8内を流れる冷水を冷却し、
該冷水から蒸発潜熱を奪って蒸発し、その冷媒蒸気は吸
収器9に流入する。
A cooling water pipe 10 is introduced into the condenser 5 . In this condenser 5, the cooling water flows through a cooling water pipe 10 and is sent to an evaporator 7. (The evaporator 7 is
A cold water pipe 8 for circulating cold water is provided. This evaporator 7
Then, the refrigerant liquid cools the cold water flowing inside the cold water pipe 8,
The latent heat of vaporization is removed from the cold water and the refrigerant vapor flows into the absorber 9.

前記吸収器9には、スプレーへツタ責図示せず)および
冷却水管10が配備されている。まだ、吸収器9は溶液
供給管11と溶液戻り管12とを介して前記再生器3に
連結されている。そして、吸収器9では再生器3から溶
液戻シ管12を通じて送シ込まれかつスプレーヘッダか
ら散布される濃溶液に冷媒蒸気を吸収させ、この冷媒蒸
気を吸収した稀溶液を、溶液供給管11を通じて再生器
3に供給するようになっている。
The absorber 9 is equipped with a spray pipe (not shown) and a cooling water pipe 10. Still, the absorber 9 is connected to the regenerator 3 via a solution supply pipe 11 and a solution return pipe 12. In the absorber 9, the refrigerant vapor is absorbed by the concentrated solution fed from the regenerator 3 through the solution return pipe 12 and sprayed from the spray header, and the dilute solution that has absorbed this refrigerant vapor is transferred to the solution supply pipe 11. The regenerator 3 is supplied through the regenerator 3.

前記溶液循環ポンプ13は、吸収器9の底部側に設けら
れ、吸収器9で生成される稀溶液を汲み出し、該稀溶液
を溶液供給管11を通じて前記再生器3へ送シ込む。
The solution circulation pump 13 is provided at the bottom side of the absorber 9, pumps out the dilute solution produced in the absorber 9, and sends the dilute solution to the regenerator 3 through the solution supply pipe 11.

前記熱交換器14は、溶液供給管11と溶液戻シ管12
間に跨設され、吸収器9から再生器3へ流れる稀溶液と
、再生器3から吸収器9へ流れる濃溶液とを熱交換させ
る。
The heat exchanger 14 includes a solution supply pipe 11 and a solution return pipe 12.
The dilute solution flowing from the absorber 9 to the regenerator 3 and the concentrated solution flowing from the regenerator 3 to the absorber 9 exchange heat.

前記冷却水パイ・パス15は、冷却水管10の吸収器入
口側配管10aと凝縮器入口側配管10b間に接続され
た冷却水バイパス管16、前記吸収器入口側配管10a
に設けられた第1の弁17、前記冷却水バイパス管16
に設けられた第2の弁18とを備え、入熱がありかつ無
負荷時に、凝縮器5に直接冷却水をバイパスさせ得るよ
うに構成されている。
The cooling water pipe path 15 includes a cooling water bypass pipe 16 connected between the absorber inlet side pipe 10a and the condenser inlet side pipe 10b of the cooling water pipe 10, and the absorber inlet side pipe 10a.
the first valve 17 provided in the cooling water bypass pipe 16;
The second valve 18 provided in the condenser 5 is configured to allow cooling water to be bypassed directly to the condenser 5 when there is heat input and there is no load.

前記実施例の吸収式冷凍機は、定常運転時、つまシ入熱
があシ、負荷が存在するときは、冷却水バイパス15の
第1の弁17を開、第2の弁18を閉として運転するこ
とによシ、次のように作用する。
During steady operation, the absorption chiller of the embodiment opens the first valve 17 of the cooling water bypass 15 and closes the second valve 18 when there is a large heat input or a load. Depending on the driving, it works as follows.

すなわち、集熱器1で太陽熱を集熱することによって加
熱された温水は、加熱媒体管2を通じて再生器3に送ら
れる。一方、吸収器9から溶液循環ポンプ13および溶
液供給管11を通じて再生器3へ稀溶液が送られる。
That is, hot water heated by collecting solar heat in the heat collector 1 is sent to the regenerator 3 through the heating medium pipe 2. On the other hand, the dilute solution is sent from the absorber 9 to the regenerator 3 through the solution circulation pump 13 and the solution supply pipe 11.

そして、再生器3内で温水により稀溶液が加熱され、冷
媒は蒸気となり、その冷媒蒸気は冷媒蒸気管4を通じて
凝縮器5へ送られ、冷媒を蒸発させた濃溶液は溶液戻シ
管12を通じて吸収器9へ戻され、前記稀溶液と濃溶液
とは熱交換器14において熱交換する。
Then, the dilute solution is heated with hot water in the regenerator 3, the refrigerant becomes vapor, the refrigerant vapor is sent to the condenser 5 through the refrigerant vapor pipe 4, and the concentrated solution with the refrigerant evaporated is passed through the solution return pipe 12. Returned to the absorber 9, the dilute solution and concentrated solution exchange heat in a heat exchanger 14.

前記凝縮器5では、冷却水管10を通じて挿通される冷
却水によシ冷媒蒸気が冷却され、凝縮し、その冷媒液は
冷媒戻シ管6を通って蒸発器7へ流入し、回収される。
In the condenser 5, the refrigerant vapor is cooled and condensed by the cooling water passed through the cooling water pipe 10, and the refrigerant liquid flows into the evaporator 7 through the refrigerant return pipe 6 and is recovered.

前記蒸発器7には、冷水管8を通じて冷水が循環され、
この蒸発器7では冷媒液が冷水管8内を流れる冷水の潜
熱を奪って蒸発し、冷水を冷却して冷凍能力を発揮する
。そして、蒸発器7で発生した冷媒ガスは吸収器9に流
れる。
Cold water is circulated through the evaporator 7 through a cold water pipe 8,
In the evaporator 7, the refrigerant liquid absorbs the latent heat of the cold water flowing in the cold water pipe 8 and evaporates, thereby cooling the cold water and exerting its refrigerating ability. The refrigerant gas generated in the evaporator 7 then flows to the absorber 9.

前記吸収器9には、冷却水管10を通じて冷却水が挿通
されており、冷却水で温度が低下されている状態で濃溶
液中に冷媒ガスが吸収される。この吸収器9における溶
液の飽和圧力は、冷却水によシ温度が低くなるほど、ま
た溶液の濃度が高くなるほど低くなシ、よ)大きな吸収
力をもつ。
Cooling water is passed through the absorber 9 through a cooling water pipe 10, and the refrigerant gas is absorbed into the concentrated solution while the temperature is lowered by the cooling water. The saturation pressure of the solution in this absorber 9 decreases as the temperature of the cooling water decreases, and as the concentration of the solution increases, the absorption capacity increases.

ついで、入熱がありながら一時的に無負荷になったとき
は、従来冷凍機の運転を停止していたが、本発明の実施
例では次のように運転する。
Next, when there is heat input but there is no load temporarily, the operation of the refrigerator is conventionally stopped, but in the embodiment of the present invention, the operation is performed as follows.

すなわち、冷却水バイパス15の第1の弁17を閉、第
2の弁18を開とし、冷却水バイパス管16および冷却
水の凝縮器入口側配管10bを通じて凝縮器5に直接冷
却水をバイパスさせ、冷凍能力が出ない状態にして溶液
循環ポンプ13を運転し続ける。
That is, the first valve 17 of the cooling water bypass 15 is closed, the second valve 18 is opened, and the cooling water is bypassed directly to the condenser 5 through the cooling water bypass pipe 16 and the cooling water condenser inlet side pipe 10b. , the solution circulation pump 13 continues to operate with no refrigerating capacity.

これによυ、溶液は継続して濃縮され、入熱は溶液濃度
を高めることで蓄積されることになる。
As a result, the solution will continue to be concentrated, and heat input will be accumulated by increasing the concentration of the solution.

その結果、次の負荷時に、入熱がなくても、吸収器9に
は濃溶液が供給されるので、冷却水管10を通じて吸収
器9に再び冷却水を挿通することによシ、蓄熱された分
の冷凍能力が得られる。
As a result, when the next load is applied, the concentrated solution is supplied to the absorber 9 even if there is no heat input, so that by passing cooling water through the cooling water pipe 10 into the absorber 9 again, the heat can be stored. Freezing capacity for 30 minutes can be obtained.

なお、図面では太陽熱を溶液の加熱源として利用する場
合について例示しているが、太陽熱の集熱器に代えて排
熱の貯熱器を用いることによシ、排熱を利用する吸収式
冷凍機にも適用することができる。
Although the drawing shows an example of using solar heat as a heating source for the solution, absorption refrigeration using waste heat can also be achieved by using a waste heat storage device instead of a solar heat collector. It can also be applied to machines.

本発明は、以上説明した構成1作用のもので、入熱があ
シかつ無負荷時には冷:′動水バイパスを通′1: じて凝縮器へ直接冷却水をバイパスさせ、運転を継続し
、溶液の濃度を高めることで蓄熱することができ、冷凍
機自体に蓄熱機能をもたせているので、設備全体を著し
く小型化できる効果を有する外、設備費を大幅に節減し
得る効果がある。
The present invention has the above-described configuration 1, and when there is no heat input and no load, the cooling water is directly bypassed to the condenser through the dynamic water bypass, and operation is continued. Since heat can be stored by increasing the concentration of the solution, and the refrigerator itself has a heat storage function, it not only has the effect of significantly downsizing the entire equipment, but also has the effect of significantly reducing equipment costs.

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

図は本発明吸収式冷凍機の一実施例を示す系統図である
。 1・・・集熱器、2・・・加熱媒体管、3・・・再生器
、4・・・冷媒蒸気管、5・・・凝縮器、6・・・冷媒
戻υ管、7・・・蒸発器、8・・・冷水管、9・・・吸
収器、10・・・冷却水管、10a・・・吸収器入口側
配管、10b・・・凝縮器入口側配管、11・・・溶液
供給管、12・・・溶液戻シ管、13・・・溶液循環ポ
ンプ、14・・・熱交換器、15・・・冷却水バイパス
全体、16・・・冷却水バイパス管、17・・・第1の
弁、18・・・第2の弁。
The figure is a system diagram showing an embodiment of an absorption refrigerator according to the present invention. DESCRIPTION OF SYMBOLS 1... Heat collector, 2... Heating medium pipe, 3... Regenerator, 4... Refrigerant vapor pipe, 5... Condenser, 6... Refrigerant return pipe, 7...・Evaporator, 8... Cold water pipe, 9... Absorber, 10... Cooling water pipe, 10a... Absorber inlet side piping, 10b... Condenser inlet side piping, 11... Solution Supply pipe, 12... Solution return pipe, 13... Solution circulation pump, 14... Heat exchanger, 15... Entire cooling water bypass, 16... Cooling water bypass pipe, 17... First valve, 18... second valve.

Claims (1)

【特許請求の範囲】[Claims] 蒸発器、吸収器、凝縮器、再生器、溶液循環ポンプおよ
び熱交換器等を配管で連絡するとともに、再生器内の溶
液の加熱源として太陽熱や排熱などを利用するものにお
いて、前記吸収器を通って凝縮器に冷却水を挿通する冷
却水管に、入熱があシかつ無負荷時に凝縮器へ直接冷却
水をバイパスさせ得る冷却水バイパス機構を設けたこと
を特徴とする吸収式冷凍機。
In a device that connects an evaporator, absorber, condenser, regenerator, solution circulation pump, heat exchanger, etc. with piping, and uses solar heat, waste heat, etc. as a heating source for the solution in the regenerator, the absorber An absorption chiller characterized in that a cooling water pipe through which cooling water is inserted into a condenser is provided with a cooling water bypass mechanism that allows cooling water to bypass directly to the condenser when there is no load and there is no heat input. .
JP57084739A 1982-05-21 1982-05-21 Absorption type refrigerator Pending JPS58203362A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57084739A JPS58203362A (en) 1982-05-21 1982-05-21 Absorption type refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57084739A JPS58203362A (en) 1982-05-21 1982-05-21 Absorption type refrigerator

Publications (1)

Publication Number Publication Date
JPS58203362A true JPS58203362A (en) 1983-11-26

Family

ID=13839061

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57084739A Pending JPS58203362A (en) 1982-05-21 1982-05-21 Absorption type refrigerator

Country Status (1)

Country Link
JP (1) JPS58203362A (en)

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