JPS586231Y2 - Small absorption refrigerator - Google Patents

Small absorption refrigerator

Info

Publication number
JPS586231Y2
JPS586231Y2 JP13365177U JP13365177U JPS586231Y2 JP S586231 Y2 JPS586231 Y2 JP S586231Y2 JP 13365177 U JP13365177 U JP 13365177U JP 13365177 U JP13365177 U JP 13365177U JP S586231 Y2 JPS586231 Y2 JP S586231Y2
Authority
JP
Japan
Prior art keywords
regenerator
refrigerant
storage chamber
pipe
absorbent solution
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
JP13365177U
Other languages
Japanese (ja)
Other versions
JPS5460350U (en
Inventor
佐登志 内藤
Original Assignee
矢崎総業株式会社
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 矢崎総業株式会社 filed Critical 矢崎総業株式会社
Priority to JP13365177U priority Critical patent/JPS586231Y2/en
Publication of JPS5460350U publication Critical patent/JPS5460350U/ja
Application granted granted Critical
Publication of JPS586231Y2 publication Critical patent/JPS586231Y2/en
Expired legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【考案の詳細な説明】 本考案は比較的低温の熱源、たとえば太陽集熱器で得ら
れる温水等を利用する水−リチウム塩系小型吸収式冷凍
機の改良に係わる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a water-lithium salt compact absorption refrigerator that utilizes a relatively low-temperature heat source, such as hot water obtained from a solar collector.

さらに詳述すれば、本考案は一時運転停止後の運転再開
を容易なものとした小型収納式冷凍機に係わる。
More specifically, the present invention relates to a compact retractable refrigerator that facilitates restarting operation after a temporary stop.

従来、この種の冷凍機において温度に変動のある温水等
を熱源として使用する場合には、特開昭51−3444
6号によれば、再生器での吸収剤溶液の沸騰を補償する
ために循環する吸収剤溶液の濃度を調整する冷媒貯蔵室
を設けることにより安定がつ効率のよい運転が行なえる
ことが開示されている。
Conventionally, when hot water or the like whose temperature fluctuates is used as a heat source in this type of refrigerator, Japanese Patent Application Laid-Open No. 51-3444
According to No. 6, it is disclosed that stable and efficient operation can be achieved by providing a refrigerant storage chamber that adjusts the concentration of the circulating absorbent solution in order to compensate for boiling of the absorbent solution in the regenerator. has been done.

このような温度に変動がある温水等を熱源とし冷媒貯蔵
室を具備する小型吸収式冷凍機では重大な欠点があった
Small-sized absorption refrigerators that use hot water or the like as a heat source whose temperature fluctuates and are equipped with a refrigerant storage chamber have serious drawbacks.

すなわち高い温度の温水が加熱源として使用されている
際の系内の吸収剤溶液の濃度は高い値となっているが、
この時点で運転を停止した場合には、次に運転する際の
再生器内の吸収剤溶液の濃度は高いため、加熱源が高温
であればよいが、低温では沸騰を行なうことができず運
転不能となることがあった。
In other words, when hot water at a high temperature is used as a heating source, the concentration of the absorbent solution in the system is high, but
If the operation is stopped at this point, the concentration of the absorbent solution in the regenerator will be high the next time the operation is started, so the heating source only needs to be at a high temperature. Sometimes it became impossible.

従って連続した運転では冷媒貯蔵室によって設定された
濃度範囲で運転可能であるが、一旦停止した場合には停
止時の熱源温水の温度以上でないと運転再開ができない
こととなる。
Therefore, in continuous operation, it is possible to operate within the concentration range set by the refrigerant storage chamber, but once it is stopped, operation cannot be resumed unless the temperature of the heat source hot water is higher than the temperature at the time of stopping.

考案者の実験によれば、95℃の温水温度で停止した場
合、■時間後においてもはや88℃以下の温度の温水で
は運転再開が不可能であった。
According to the inventor's experiments, when the machine was stopped at a hot water temperature of 95°C, it was no longer possible to restart operation with hot water at a temperature of 88°C or lower after hours.

また停止した場合、再生器の液深は運転時よりも深くな
るが(これは循環していた液が下に落るため)、これに
よって運転開始を更に困難にしている。
Furthermore, when the regenerator is stopped, the liquid depth in the regenerator becomes deeper than during operation (because the circulating liquid falls to the bottom), which makes it even more difficult to start operation.

特に温水温度が低い場合(80℃以下)では、その液深
増加による圧力上昇は無視できなくなり(温水温度が下
ると、その蒸気圧も低下し、液深増加による圧力上昇の
占める割合が大きくなる)、実験では停止した温度以上
でなければ運転を開始できなかった。
Especially when the hot water temperature is low (below 80℃), the pressure increase due to the increase in liquid depth cannot be ignored (as the hot water temperature decreases, its vapor pressure also decreases, and the proportion of the pressure increase due to increase in liquid depth becomes large) ), in experiments, operation could not be started unless the temperature was higher than the temperature at which it stopped.

また75℃で停止した場合には、78℃以上でなければ
運転開始できなかった。
In addition, when stopped at 75°C, operation could not be started unless the temperature was 78°C or higher.

本考案は、運転停止時に冷媒貯蔵室に貯った冷媒を再生
器に戻し再生器の吸収剤溶液の濃度を低下させ、これに
より運転再開を容易にした小型吸収式冷凍機に係わる。
The present invention relates to a small absorption refrigerating machine that returns refrigerant stored in a refrigerant storage chamber to a regenerator at the time of shutdown to reduce the concentration of an absorbent solution in the regenerator, thereby facilitating restart of operation.

本考案の目的は、再生器、凝縮器、蒸発器および吸収器
でなる吸収剤溶液回路から前記再生器での加熱源の温度
の変動に応じて冷媒の取出しおよび放出を行ない吸収剤
溶液の濃度を調節する冷媒貯蔵室を備えた小型吸収式冷
凍機において、前記凝縮器から前記蒸発器への管路と前
記冷媒貯蔵室とを接続するU字管と前記再生器とを連結
する管路を設けるとともに、この管路の途中にオリフィ
スまたは弁を介装して、前記冷媒貯蔵室に貯った冷媒を
運転停止時に前記再生器に戻すようにしたことを特徴と
する、小型吸収式冷凍機を提供することにある。
The purpose of the present invention is to take out and release refrigerant from an absorbent solution circuit consisting of a regenerator, a condenser, an evaporator, and an absorber in response to fluctuations in the temperature of the heating source in the regenerator, thereby increasing the concentration of the absorbent solution. In a small absorption refrigerator equipped with a refrigerant storage chamber for adjusting the refrigerant, the regenerator is connected to a U-shaped pipe that connects the refrigerant storage chamber and a conduit from the condenser to the evaporator. and an orifice or valve is interposed in the middle of the conduit so that the refrigerant stored in the refrigerant storage chamber is returned to the regenerator when the operation is stopped. Our goal is to provide the following.

本考案の好適な1具体例を示す図面を参照して本考案に
ついて詳述する。
The present invention will be described in detail with reference to the drawings showing a preferred embodiment of the present invention.

図面において、参照番号1は再生器、2は分離器、3は
凝縮器、4は蒸発器、5は吸収器、6は冷媒貯蔵室、7
は熱交換器、8は蒸発器コイル、9は加熱温水入口、9
′は加熱温水出口、10.10’、10″はそれぞれ冷
却水コイル、11はオリフィス、12は分離器圧力伝達
管、13は冷媒戻し管、14はオリフィスである。
In the drawings, reference number 1 is a regenerator, 2 is a separator, 3 is a condenser, 4 is an evaporator, 5 is an absorber, 6 is a refrigerant storage chamber, and 7 is a regenerator.
is a heat exchanger, 8 is an evaporator coil, 9 is a heating hot water inlet, 9
' is a heated hot water outlet, 10, 10' and 10'' are cooling water coils, 11 is an orifice, 12 is a separator pressure transmission pipe, 13 is a refrigerant return pipe, and 14 is an orifice.

この小型吸収式冷凍機では、稀吸収剤溶液は再生器1に
おいて加熱温水人口9から入って加熱温水出口9′から
出る加熱温水によって上昇濃縮され、分離器2で水蒸気
および濃吸収剤溶液に分離される。
In this small-sized absorption refrigerator, the dilute absorbent solution is raised and concentrated in the regenerator 1 by heated hot water that enters from the heated hot water port 9 and exits from the heated hot water outlet 9', and is separated into steam and concentrated absorbent solution in the separator 2. be done.

分離された水蒸気は凝縮器3において冷却水コイル10
″を介して流れる冷却水によって冷却されて水となる。
The separated water vapor is sent to the cooling water coil 10 in the condenser 3.
It is cooled by the cooling water flowing through it and becomes water.

このようにして得られた水は凝縮器3から管路を介して
蒸発器4に入って蒸発するが、その間に該蒸発器4のコ
イル8を流れる二次冷媒から熱をうばって蒸発する。
The water thus obtained enters the evaporator 4 from the condenser 3 via a pipe and is evaporated, during which time it absorbs heat from the secondary refrigerant flowing through the coil 8 of the evaporator 4 and evaporates.

ついで水蒸気は吸収器5に入り、分離器2で分離され熱
交換器7で昇温されてきた吸収剤濃溶液に吸収され、吸
収剤稀溶液となったのち再生器1に戻る。
The water vapor then enters the absorber 5, is separated by the separator 2, is absorbed by the concentrated absorbent solution heated by the heat exchanger 7, and returns to the regenerator 1 after becoming a dilute absorbent solution.

凝縮器3から蒸発器4への1管路にはU字形の管によっ
て冷媒貯蔵蒸6が設けである。
One line from the condenser 3 to the evaporator 4 is provided with a refrigerant storage 6 by a U-shaped tube.

該冷媒貯蔵室6内の圧力は冷却水コイル10を介して流
れる冷却水によって常時一定に保っである。
The pressure inside the refrigerant storage chamber 6 is always kept constant by the cooling water flowing through the cooling water coil 10.

また前記管路には分離器2の圧力を伝達する分離器圧力
伝達管が設けである。
Further, the pipeline is provided with a separator pressure transmission pipe for transmitting the pressure of the separator 2.

したがって凝縮器3から蒸発器4へ水が移動する場合、
分離器の圧力の変動に応じて、すなわち再生器へ入る加
熱温水の温度の変動に応じて水が冷媒貯蔵室に貯えられ
る。
Therefore, when water moves from condenser 3 to evaporator 4,
Water is stored in the refrigerant reservoir in response to variations in the pressure of the separator, ie in response to variations in the temperature of the heated hot water entering the regenerator.

したがって系内の吸収剤溶液の濃度が加熱温水の温度の
変動に応じて調節されるため再生器1での沸騰が安定し
て行なわれる。
Therefore, the concentration of the absorbent solution in the system is adjusted according to the temperature fluctuation of the heated hot water, so that boiling in the regenerator 1 is performed stably.

本考案によれば、凝縮器3から蒸発器4への管路と冷媒
貯蔵室6とを接続するU字形の管と再生器1とを連結す
る冷媒戻し管13が設けられており、しかも鉄管13に
は弁機能を果すオリフィス14が設けられている。
According to the present invention, a refrigerant return pipe 13 is provided that connects the regenerator 1 with the U-shaped pipe that connects the pipe line from the condenser 3 to the evaporator 4 and the refrigerant storage chamber 6, and the iron pipe 13 is provided with an orifice 14 that functions as a valve.

したがって、運転時には分離器と冷媒貯蔵室との間に圧
力差により冷媒貯蔵室に冷媒が押上げられているが、運
転を停止した場合にはこの冷媒はオリフィス11および
14を通って冷媒戻し管13を介して再生器1に戻され
、再生器1内の吸収剤溶液を稀釈する。
Therefore, during operation, the refrigerant is pushed up into the refrigerant storage chamber due to the pressure difference between the separator and the refrigerant storage chamber, but when the operation is stopped, this refrigerant passes through the orifices 11 and 14 into the refrigerant return pipe. 13 to the regenerator 1 to dilute the absorbent solution in the regenerator 1.

その結果、運転を再開する場合には再生器1内の吸収剤
溶液はうすくなっており、常に設定された温度範囲にお
いて安定した運転が行なわれる。
As a result, when the operation is restarted, the absorbent solution in the regenerator 1 is diluted, and stable operation is always performed within the set temperature range.

以上本考案をその具体例について詳述したが、本考案は
この特定の実施例に限定されるものではなく、本考案の
精神を逸脱しないで幾多の変化変形がなし得ることはも
ちろんである。
Although the present invention has been described above in detail with reference to a specific example, the present invention is not limited to this particular embodiment, and it goes without saying that many changes and modifications can be made without departing from the spirit of the present invention.

たとえば上記具体例では弁機能を有する部材としてオリ
フィス14を使用しているが、もちろん手動弁あるいは
自動弁でもよい。
For example, in the above specific example, the orifice 14 is used as a member having a valve function, but of course a manual valve or an automatic valve may be used.

オリフィスの場合には運転時に該オリフィスを介して若
干の冷媒が再生器に流入することが考えられるが、量的
には非常に少量であり、弁等の手段でなくても充分その
機能を果す。
In the case of an orifice, it is possible that some refrigerant may flow into the regenerator through the orifice during operation, but the amount is very small and the function is sufficient even without a valve or other means. .

さらに上記具体例では冷媒を再生器の吸収剤溶液中に直
接混入させているが、再生器下部に別途に設けた加熱装
置に導入してここで戻した冷媒を蒸気としたのち前記再
生器内に吹込むようにしてもよい。
Furthermore, in the above specific example, the refrigerant is directly mixed into the absorbent solution in the regenerator, but the refrigerant is introduced into a heating device separately installed at the bottom of the regenerator, and the returned refrigerant is turned into vapor and then placed inside the regenerator. You may also inject it into the

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

図面は本考案の小型吸収式冷凍機の好適な1具体例を示
す図である。 1・・・・・・再生器、2・・・・・・分離器、3・・
・・・・凝縮器、4・・・・・・蒸発器、5・・・・・
・吸収器、6・・・・・・冷媒貯蔵室、7・・・・・・
熱交換器、8・・・・・・蒸発器コイル、9・・・・・
・加熱温水入口、9′・・・・・・加熱温水出口、10
.10’、10”・・・・・・冷却水コイル、11・・
・・・・オリフィス、12・・・・・・分離器圧力伝達
管、13・・・・・・冷媒戻し管、14・・・・・・オ
リフィス。
The drawing shows a preferred embodiment of the small-sized absorption refrigerator of the present invention. 1...Regenerator, 2...Separator, 3...
... Condenser, 4 ... Evaporator, 5 ...
・Absorber, 6... Refrigerant storage room, 7...
Heat exchanger, 8...Evaporator coil, 9...
・Heating hot water inlet, 9'... Heating hot water outlet, 10
.. 10', 10"... Cooling water coil, 11...
... Orifice, 12 ... Separator pressure transmission pipe, 13 ... Refrigerant return pipe, 14 ... Orifice.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 再生器、凝縮器、蒸発器および吸収器でなる吸収剤溶液
回路から前記再生器の加熱源の温度の変動に応じて冷媒
の取出しおよび放出を行ない吸収剤溶液の濃度を調節す
る冷媒貯蔵室を備えた小型吸収式冷凍機において、前記
凝縮器から前記蒸発器への管路と前記冷媒貯蔵室とを接
続するU字管と前記再生器とを連結する管路を設けると
ともに、この管路の途中にオリフィスまたは弁を介装し
て、前記冷媒貯蔵室に貯った冷媒を運転停止時に前記再
生器に戻すようにしたことを特徴とする、小型吸収式冷
凍機。
A refrigerant storage chamber for extracting and discharging refrigerant from an absorbent solution circuit consisting of a regenerator, a condenser, an evaporator, and an absorber in response to fluctuations in the temperature of the heating source of the regenerator to adjust the concentration of the absorbent solution. In the small-sized absorption refrigerating machine, a pipe is provided that connects a U-shaped pipe that connects a pipe from the condenser to the evaporator and the refrigerant storage chamber, and a pipe that connects the regenerator. A small-sized absorption refrigerator, characterized in that an orifice or a valve is interposed in the middle so that the refrigerant stored in the refrigerant storage chamber is returned to the regenerator when the operation is stopped.
JP13365177U 1977-10-06 1977-10-06 Small absorption refrigerator Expired JPS586231Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13365177U JPS586231Y2 (en) 1977-10-06 1977-10-06 Small absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13365177U JPS586231Y2 (en) 1977-10-06 1977-10-06 Small absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS5460350U JPS5460350U (en) 1979-04-26
JPS586231Y2 true JPS586231Y2 (en) 1983-02-02

Family

ID=29102302

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13365177U Expired JPS586231Y2 (en) 1977-10-06 1977-10-06 Small absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS586231Y2 (en)

Also Published As

Publication number Publication date
JPS5460350U (en) 1979-04-26

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