JPH0571858B2 - - Google Patents

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Publication number
JPH0571858B2
JPH0571858B2 JP59018629A JP1862984A JPH0571858B2 JP H0571858 B2 JPH0571858 B2 JP H0571858B2 JP 59018629 A JP59018629 A JP 59018629A JP 1862984 A JP1862984 A JP 1862984A JP H0571858 B2 JPH0571858 B2 JP H0571858B2
Authority
JP
Japan
Prior art keywords
container
substance
heat transfer
refrigerant
heat pump
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 - Lifetime
Application number
JP59018629A
Other languages
Japanese (ja)
Other versions
JPS60162167A (en
Inventor
Isao Takeshita
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP1862984A priority Critical patent/JPS60162167A/en
Publication of JPS60162167A publication Critical patent/JPS60162167A/en
Publication of JPH0571858B2 publication Critical patent/JPH0571858B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は熱サイクル機器として冷房,暖房,給
湯に用いられ、又蓄熱器として用いられる間欠作
動化学ヒートポンプ装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to an intermittent chemical heat pump device used as a thermal cycle device for cooling, heating, and hot water supply, and also used as a heat storage device.

従来例の構成とその問題点 第1図は太陽熱を用いた間欠式化学ヒートポン
プの例で、太陽熱で加熱される容器1にナトリウ
ムチオシアネートとこれに吸着させたアンモニア
を収容してある。この容器から配管3,弁4を経
て凝縮容器5に結ばれている。今容器1を加熱
し、弁4を開き、凝縮器5に設けた冷却水管6で
冷却すると、容器1よりアンモニアガスが発生
し、凝縮器5内を液化アンモニア8が貯溜する。
Structure of a conventional example and its problems FIG. 1 shows an example of an intermittent chemical heat pump using solar heat, in which a container 1 heated by solar heat contains sodium thiocyanate and ammonia adsorbed thereon. This container is connected to a condensing container 5 via a pipe 3 and a valve 4. Now, when the container 1 is heated, the valve 4 is opened, and the cooling water pipe 6 provided in the condenser 5 is cooled, ammonia gas is generated from the container 1, and liquefied ammonia 8 is stored in the condenser 5.

十分アンモニア液が貯溜した所で弁4を閉じれ
ばその状態で保存できる。次に夜間など日射のな
い時に弁4を開くとアンモニア液は気化し、再び
容器1内のナトリウムチオシアネートにアンモニ
ア吸収されるため、凝縮器5は蒸発器となり、冷
却水管6に水を流せば冷水がえられる。
If the valve 4 is closed when a sufficient amount of ammonia solution has been stored, the ammonia solution can be stored in that state. Next, when valve 4 is opened when there is no sunlight, such as at night, the ammonia liquid evaporates, and the ammonia is absorbed by the sodium thiocyanate in container 1 again, so condenser 5 becomes an evaporator, and when water is passed through cooling water pipe 6, cold water is generated. It can be grown.

この装置はこのような物質の組み合せで使用す
る時は殆んど問題はないが、分離され、凝縮,蒸
発を行う物質が今の例のアンモニアのように使用
温度域で圧力の高い気体ではなく、水のごとく使
用温度域で圧力の低い物質の場合は、配管3,弁
4によつて生ずる圧力損失が相対的に大きな値と
なるため、かなり口径の大きい配管と弁が必要と
なり、特に口径の大きい弁は高価であり、電磁弁
などにより自動化も困難であるなど実施上での大
きな障害となる。
There is almost no problem when using this device with such a combination of substances, but the substance that is separated, condensed, and evaporated is not a gas with high pressure in the operating temperature range, like ammonia in the current example. In the case of substances such as water that have low pressure in the operating temperature range, the pressure loss caused by piping 3 and valve 4 will be relatively large, so piping and valves with considerably large diameters will be required. Large valves are expensive, and automation is difficult due to the use of electromagnetic valves, which poses major obstacles to implementation.

発明の目的 間欠作動化学ヒートポンプ装置で、長期間の蓄
熱を目的として、分離された冷媒と吸収材を隔離
する簡便で圧力損失の少い装置を与えるものであ
る。
OBJECT OF THE INVENTION It is an intermittent chemical heat pump device to provide a simple and low pressure loss device for isolating separated refrigerant and absorbent material for the purpose of long-term heat storage.

発明の構成 本発明は冷媒と吸収材よりなる間欠作動化学ヒ
ートポンプ装置の冷媒を凝縮させるための伝熱手
段を有する容器に対し、これと連通した、前記凝
縮液を貯溜する容器を設け、この2つの容器を連
通する部分に開閉しうる弁を設け、この凝縮液を
貯溜する容器にも伝熱手段を設けた間欠作動化学
ヒートポンプ装置である。
Structure of the Invention The present invention provides a container having a heat transfer means for condensing a refrigerant of an intermittent operating chemical heat pump device consisting of a refrigerant and an absorbent, and a container communicating with the container for storing the condensed liquid. This is an intermittent chemical heat pump device in which a valve that can be opened and closed is provided in the part that communicates the two containers, and a heat transfer means is also provided in the container that stores the condensate.

実施例の説明 第2図は本発明の一実施例を示す図である。容
器9には吸収材10が収納されており、これと熱
的に接触した伝熱管11が設けてある。吸収材1
0としては例えばゼオライトのようなものをあげ
ることができ、これに吸着される冷媒としては水
がしばしば使われる。今水を吸着したゼオライト
を伝熱管11に温水を流して加熱すると水蒸気を
発生する。この水蒸気、一般的にいえば冷媒蒸気
は太い配管12を通つて、凝縮容器13に流れて
ゆく。この中には冷媒蒸気を冷却する伝熱管14
が存在し、底部に細い配管15,弁16を経て凝
縮液貯溜容器17に連通している。従つて凝縮し
た液はこの貯溜容器17に流入する。この際流入
し易くするためこの容器も伝熱管18を設けて冷
却してある。
DESCRIPTION OF THE EMBODIMENT FIG. 2 is a diagram showing an embodiment of the present invention. An absorbent material 10 is housed in the container 9, and a heat transfer tube 11 is provided in thermal contact with the absorbent material 10. Absorbent material 1
For example, zeolite can be used as the refrigerant, and water is often used as the refrigerant adsorbed on this. When the zeolite that has now adsorbed water is heated by flowing hot water through the heat transfer tube 11, water vapor is generated. This water vapor, generally speaking, refrigerant vapor, flows through a thick pipe 12 to a condensing vessel 13. Inside this is a heat transfer tube 14 that cools the refrigerant vapor.
exists, and communicates with a condensate storage container 17 through a thin pipe 15 and a valve 16 at the bottom. The condensed liquid therefore flows into this storage container 17. At this time, in order to facilitate the inflow, this container is also provided with a heat transfer tube 18 to cool it.

吸収材の加温温度と冷媒の凝縮温度を定めると
ある平衡状態が存在し、それ以上冷媒は凝縮しな
いから、この時点で加熱を止め、弁16を閉じる
とこの状態はいつまでも接続する。次に使用する
時に弁16を開き、伝熱管14,18用いて冷媒
を暖めると冷媒は液相で容器13へ移り、ここで
蒸発し吸収材10が発熱して伝熱管11から熱を
取出すことができる。なお、配管15の端部は貯
溜容器17の底部に位置させているので、貯溜容
器17から配管15を介して凝縮容器13へ流れ
る冷媒は液相で移動する。又伝熱管11により吸
収材10を冷却すると冷媒19の蒸発が促進さ
れ、伝熱管14,18に流す水の温度が低下し、
冷房などに使用することができる。
When the heating temperature of the absorbent material and the condensing temperature of the refrigerant are determined, a certain equilibrium state exists, and the refrigerant does not condense any further, so if the heating is stopped at this point and the valve 16 is closed, this state will remain forever. When the valve 16 is opened for next use and the refrigerant is heated using the heat transfer tubes 14 and 18, the refrigerant moves in a liquid phase to the container 13, where it evaporates, causing the absorbent material 10 to generate heat and extracting heat from the heat transfer tubes 11. I can do it. Note that since the end of the pipe 15 is located at the bottom of the storage container 17, the refrigerant flowing from the storage container 17 to the condensation container 13 via the pipe 15 moves in a liquid phase. Furthermore, when the absorbent material 10 is cooled by the heat exchanger tube 11, the evaporation of the refrigerant 19 is promoted, and the temperature of the water flowing through the heat exchanger tubes 14 and 18 is lowered.
It can be used for cooling, etc.

吸収材の加熱を圧縮式冷房機の凝縮器、冷却を
前記冷房機の蒸発器とすることにより圧縮式の出
力を蓄熱する装置としても有用である。
It is also useful as a device for storing heat from the output of a compression type by using the condenser of a compression type air conditioner to heat the absorbent material and the evaporator of the air conditioner to cool it.

今、凝縮温度を30℃とすれば冷媒に水を用いた
場合蒸気の圧力は32Torrとかなり低い値である。
さらに逆に冷媒を蒸発させて吸収材に吸収させる
時は、冷房を考えて蒸気温度を50℃とすると圧力
は7Torr位となる。
Now, if the condensation temperature is 30°C, the steam pressure will be 32 Torr, which is quite low when water is used as the refrigerant.
Conversely, when the refrigerant is evaporated and absorbed by an absorbent material, the pressure will be approximately 7 Torr if the steam temperature is set to 50°C for cooling purposes.

この場合配管径が5cm,長さ60cmとして、配管
による圧力損失と平均圧力の比を2%におさえる
と、冷房能力は4000kcal/h程度となる。
In this case, if the pipe diameter is 5 cm and the length is 60 cm, and the ratio of pressure loss due to the pipe to average pressure is kept to 2%, the cooling capacity will be approximately 4000 kcal/h.

この値はやゝ大形の家庭用の冷房機の能力に相
当するが、これを実現するにはこれ位の太さの配
管が必要であり、これに従来例のごとく弁を設け
るとすれば、かなり大きな弁が必要で、実用し難
い。
This value corresponds to the capacity of a fairly large household air conditioner, but to achieve this, pipes of this thickness are required, and if a valve is installed in this as in the conventional example, , which requires a fairly large valve and is difficult to put into practice.

しかし本発明によれば配管15を流れるのは低
圧の蒸気ではなく、液体であるから、体積は
33000分の1位に小となつているため、内径数mm
の管で十分であり、弁も極く小形のものでよい。
However, according to the present invention, what flows through the pipe 15 is not low-pressure steam but a liquid, so the volume is
Because it is small to 1/33000, the inner diameter is several mm.
A tube of approximately 100 mm is sufficient, and the valve may also be extremely small.

特に冷却用の伝熱管18と14を図のごとく直
列にし18から14に向つて冷却水を流せば、冷
媒貯溜容器17内の圧力は、容器13内の圧力よ
りも低くなり、液化冷媒は自然に容器17に流入
する。又逆に冷媒を蒸発させる時は同じく18か
ら14へ水を流せば、容器17内の圧力が容器1
3より高まり、凝縮液は自然に容器13の中へ流
入する。
In particular, if the cooling heat transfer tubes 18 and 14 are connected in series as shown in the figure and the cooling water flows from 18 to 14, the pressure inside the refrigerant storage container 17 will be lower than the pressure inside the container 13, and the liquefied refrigerant will naturally flow. flows into the container 17. Conversely, when evaporating the refrigerant, by flowing water from 18 to 14, the pressure inside container 17 will decrease to 1.
3, the condensate naturally flows into the container 13.

なお、本実施例は液体による冷却加熱方法につ
いて述べたが、勿論空冷などの方法も考えられ
る。又貯溜した液が、蒸発時自然に容器13にも
どる例を示したが、ポンプなどを用いて強制的に
循環させてもよいことは勿論である。
Note that although this embodiment has described a cooling/heating method using a liquid, methods such as air cooling are of course also conceivable. Further, although an example has been shown in which the stored liquid naturally returns to the container 13 upon evaporation, it is of course possible to forcefully circulate the liquid using a pump or the like.

発明の効果 本発明の間欠作動化学ヒートポンプ装置におい
ては、口径の小さい配管や弁を用いても高性能を
得ることができる。
Effects of the Invention In the intermittent-operating chemical heat pump device of the present invention, high performance can be obtained even if pipes and valves with small diameters are used.

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

第1図は従来の一実施例の間欠作動化学ヒート
ポンプの構成図、第2図は本発明の一実施例の間
欠作動化学ヒートポンプの構成図である。 9……吸収材容器、10……吸収材、11……
伝熱管、12………配管(冷媒蒸気用)、13…
…凝縮容器、14,18……伝熱管、15……配
管(冷媒液用)、16……弁、17……凝縮冷媒
液貯溜容器、19……液化冷媒。
FIG. 1 is a block diagram of a conventional intermittent chemical heat pump according to an embodiment of the present invention, and FIG. 2 is a block diagram of an intermittent chemical heat pump according to an embodiment of the present invention. 9... Absorbent container, 10... Absorbent material, 11...
Heat exchanger tube, 12... Piping (for refrigerant vapor), 13...
... Condensation container, 14, 18 ... Heat transfer tube, 15 ... Piping (for refrigerant liquid), 16 ... Valve, 17 ... Condensed refrigerant liquid storage container, 19 ... Liquefied refrigerant.

Claims (1)

【特許請求の範囲】 1 使用する温度域で凝縮蒸発しうる第1の物質
と、その第1の物質を吸着などにより固定しかつ
加熱により放出しうる第2の物質とを構成要素と
して、前記第2の物質を収納する第1の容器と、
前記第1の容器と連通し前記第1の物質を凝縮及
び蒸発させるための第2の容器と、前記第1の物
質の凝縮液を貯溜するため前記第2の容器の下部
に配した第3の容器と、前記第2及び第3の容器
内に設けた伝熱手段と、前記第2の容器と前記第
3の容器を連通する配管と、前記配管に設けた開
閉弁を具備し、前記配管の一端を前記第3の容器
の底部に位置させたことを特徴とする間欠作動化
学ヒートポンプ装置。 2 第1の容器に伝熱手段を設けた特許請求の範
囲第1項記載の間欠作動化学ヒートポンプ装置。 3 第2、第3の容器に設けた伝熱手段は直列接
続された媒体通路であり、第1の物質の凝縮時も
蒸発時も伝熱媒体を、第3の容器側から流入させ
ることを特徴とする特許請求の範囲第1項記載の
間欠作動化学ヒートポンプ装置。
[Scope of Claims] 1. The above-mentioned method comprises a first substance that can be condensed and vaporized in the temperature range used, and a second substance that can fix the first substance by adsorption or the like and can be released by heating. a first container containing a second substance;
a second container communicating with the first container to condense and evaporate the first substance; and a third container disposed below the second container to store a condensate of the first substance. a container, a heat transfer means provided in the second and third containers, a pipe communicating the second container and the third container, and an on-off valve provided in the pipe, An intermittent chemical heat pump device, characterized in that one end of the piping is located at the bottom of the third container. 2. An intermittent operating chemical heat pump device according to claim 1, wherein the first container is provided with heat transfer means. 3 The heat transfer means provided in the second and third containers are medium passages connected in series, and the heat transfer medium is allowed to flow from the third container side both when the first substance is condensed and when it evaporates. An intermittent chemical heat pump device as claimed in claim 1.
JP1862984A 1984-02-03 1984-02-03 Intermittently operable chemical heat pump device Granted JPS60162167A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1862984A JPS60162167A (en) 1984-02-03 1984-02-03 Intermittently operable chemical heat pump device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1862984A JPS60162167A (en) 1984-02-03 1984-02-03 Intermittently operable chemical heat pump device

Publications (2)

Publication Number Publication Date
JPS60162167A JPS60162167A (en) 1985-08-23
JPH0571858B2 true JPH0571858B2 (en) 1993-10-08

Family

ID=11976906

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1862984A Granted JPS60162167A (en) 1984-02-03 1984-02-03 Intermittently operable chemical heat pump device

Country Status (1)

Country Link
JP (1) JPS60162167A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5157311A (en) * 1990-07-31 1992-10-20 Matsushita Electric Industrial Co., Ltd. Brushless motor

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58190669A (en) * 1982-05-01 1983-11-07 鹿島建設株式会社 Heat accumulation type cold water generator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60104676U (en) * 1983-12-19 1985-07-17 三洋電機株式会社 Closed type adsorption refrigerator

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58190669A (en) * 1982-05-01 1983-11-07 鹿島建設株式会社 Heat accumulation type cold water generator

Also Published As

Publication number Publication date
JPS60162167A (en) 1985-08-23

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