JPS6311571Y2 - - Google Patents

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Publication number
JPS6311571Y2
JPS6311571Y2 JP1982192520U JP19252082U JPS6311571Y2 JP S6311571 Y2 JPS6311571 Y2 JP S6311571Y2 JP 1982192520 U JP1982192520 U JP 1982192520U JP 19252082 U JP19252082 U JP 19252082U JP S6311571 Y2 JPS6311571 Y2 JP S6311571Y2
Authority
JP
Japan
Prior art keywords
regenerator
evaporator
absorber
heat
absorption
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
JP1982192520U
Other languages
Japanese (ja)
Other versions
JPS5996565U (en
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 filed Critical
Priority to JP19252082U priority Critical patent/JPS5996565U/en
Publication of JPS5996565U publication Critical patent/JPS5996565U/en
Application granted granted Critical
Publication of JPS6311571Y2 publication Critical patent/JPS6311571Y2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【考案の詳細な説明】 本考案は吸収ヒートポンプにおいて簡単にボイ
ラ運転切換をできる如くしたボイラ機能付吸収ヒ
ートポンプに関するものである。
[Detailed Description of the Invention] The present invention relates to an absorption heat pump with a boiler function that allows easy boiler operation switching in the absorption heat pump.

従来、一般に用いられている吸収ヒートポンプ
はヒートポンプ機能だけでボイラ機能が生かせな
かつた。例えば、第1図に示す様に、その構成は
再生器1の稀吸収液が分離器2にて冷媒蒸気と濃
吸収液に分離し、この冷媒蒸気を単に凝縮器3を
経て蒸発器4へ導くと共に、前記濃吸収液を熱交
換器5を介して吸収器6へ導くものである。この
ため、吸収ヒートポンプは廃熱がなくなつた場
合、熱源水・冷媒の凍結、吸収液の結晶化を招く
ため、安全装置を別途に配し停止させる等の面倒
な操作をしいられていた。
Conventionally, commonly used absorption heat pumps have only a heat pump function and cannot utilize boiler functions. For example, as shown in FIG. 1, the structure is such that the dilute absorption liquid in the regenerator 1 is separated into refrigerant vapor and concentrated absorption liquid in the separator 2, and this refrigerant vapor is simply sent to the evaporator 4 through the condenser 3. At the same time, the concentrated absorption liquid is guided to the absorber 6 via the heat exchanger 5. For this reason, when absorption heat pumps run out of waste heat, the heat source water and refrigerant may freeze and the absorption liquid may crystallize, so they have had to perform troublesome operations such as installing a separate safety device to shut down the pump.

本考案は上記実情に鑑み、廃熱が減少し、吸収
ヒートポンプへの熱源水の供給温度が低下,停止
をみても、再生器への供給熱によつてボイラ運転
を可能とした吸収ヒートポンプを提供するもので
ある。
In view of the above-mentioned circumstances, the present invention provides an absorption heat pump that can operate the boiler using the heat supplied to the regenerator even if the waste heat decreases and the supply temperature of heat source water to the absorption heat pump drops or stops. It is something to do.

以下、本考案を実施例の図面について説明すれ
ば、次の通りである。
Hereinafter, the present invention will be described with reference to the drawings of embodiments.

1は駆動用燃料aを受ける再生器で、この上部
に配した揚液管7の先端に分離器2を設け、該分
離器2と凝縮器3間を結ぶ冷媒蒸気配管8に、蒸
発器4および吸収器6の胴9に向う分岐配管10
を分岐接続し、該分岐配管10の途中に弁11を
設置するする。この弁11の制御は、蒸発器4部
に配した熱源水供給管12の入口部または出口部
に設けたサーモスタツト13に連動する如くなつ
ている。5は分離器2より分離した濃吸収液を一
旦導く熱交換器で、該熱交換器5部を経た濃吸収
液を吸収器6へ導き、且つ該熱交換器5部には吸
収器6部にて冷媒蒸気を吸収した稀吸収液を導
き、再生器6部にて冷媒蒸気を吸収した稀吸収液
を導き、再生器1へ戻す構成としてなる。
Reference numeral 1 denotes a regenerator for receiving driving fuel a, and a separator 2 is provided at the tip of a liquid lift pipe 7 disposed above the regenerator. and a branch pipe 10 toward the shell 9 of the absorber 6
A valve 11 is installed in the middle of the branch pipe 10. This valve 11 is controlled in conjunction with a thermostat 13 provided at the inlet or outlet of the heat source water supply pipe 12 disposed in the evaporator 4 section. 5 is a heat exchanger for once guiding the concentrated absorption liquid separated from the separator 2; the concentrated absorption liquid that has passed through the 5 parts of the heat exchanger is guided to the absorber 6; The dilute absorption liquid that has absorbed refrigerant vapor is introduced at the regenerator 6 section, and the dilute absorption liquid that has absorbed the refrigerant vapor is introduced at the regenerator 6 section and returned to the regenerator 1.

いまこの作用を説明すると、先ず正常な吸収ヒ
ートポンプの運転は、従来のものと同様に再生器
1に流入した稀吸収液を燃焼ガスによつて加熱沸
騰し、この気泡流を揚液管7を経て分離器2へ導
き、該分離器2部にて冷媒蒸気と濃吸収液に分離
する。次に、この冷媒蒸気を蒸発器3部にて冷却
し、冷媒液を蒸発器4へ送り、該蒸発器4内の熱
源水供給管12を流れる熱源水より熱を奪つて蒸
発し、この熱源水供給管12路内の水を冷房等に
用いるものである。また、この蒸発した冷媒蒸気
は吸収器6部にあつて熱交換器5側より供給され
る濃吸収液をもつて吸収され冷媒で濃度の下がつ
た稀吸収液は、前記熱交換器5を経て再生器1へ
戻される。
To explain this effect now, first of all, in the normal operation of an absorption heat pump, the dilute absorption liquid that has flowed into the regenerator 1 is heated to boiling point by the combustion gas, and this bubble flow is sent through the pumping pipe 7, as in the conventional absorption heat pump. The liquid is then led to a separator 2, where it is separated into refrigerant vapor and concentrated absorption liquid. Next, this refrigerant vapor is cooled in the evaporator 3, and the refrigerant liquid is sent to the evaporator 4, where it absorbs heat from the heat source water flowing through the heat source water supply pipe 12 in the evaporator 4 and evaporates. The water in the 12 water supply pipes is used for cooling, etc. The evaporated refrigerant vapor is absorbed by the concentrated absorption liquid supplied from the heat exchanger 5 side in the absorber 6, and the dilute absorption liquid whose concentration has been reduced by the refrigerant passes through the heat exchanger 5. After that, it is returned to the regenerator 1.

ここにおいて、熱源水の供給温度が設定値より
低下した場合および熱源水供給ポンプが停止した
場合等にあつて、熱源水入口部または出口部のサ
ーモスタツト13の検出信号或いは熱源水ポンプ
(図示せず)との電気的インターロツクの信号に
連動して弁11を操作して切換える。即ち、ヒー
トポンプ運転時に弁11を開くと、比較的(蒸発
器,吸収器に比べて)高圧高温の冷媒蒸気が蒸発
器4および吸収器6に流入し、蒸発器4の圧力お
よび温度を上昇し、熱源水の凍結、冷媒の凍結が
防止できると共に、冷媒蒸気が吸収器6の吸収液
に吸収されるため、吸収液の吸収器6における結
晶化も防止でき、且つ吸収器6における温水の加
熱が可能となる。
Here, when the supply temperature of the heat source water falls below the set value or when the heat source water supply pump stops, etc., the detection signal of the thermostat 13 at the heat source water inlet or outlet or the heat source water pump (not shown) is detected. Switching is performed by operating the valve 11 in conjunction with the electrical interlock signal from the That is, when the valve 11 is opened during heat pump operation, refrigerant vapor at relatively high pressure and high temperature (compared to the evaporator and absorber) flows into the evaporator 4 and absorber 6, increasing the pressure and temperature of the evaporator 4. , freezing of the heat source water and freezing of the refrigerant can be prevented, and since refrigerant vapor is absorbed into the absorption liquid of the absorber 6, crystallization of the absorption liquid in the absorber 6 can also be prevented, and heating of hot water in the absorber 6 can be prevented. becomes possible.

従つて、吸収ヒートポンプにおいて、熱源水の
有無、熱源水の温度レベルに関係なく吸収器6お
よび凝縮器3において温水を作りだすことが可能
である。尚、温水負荷が減少し吸収ヒートポンプ
の出力が余る場合は、サーモスタツト14により
燃料量を制御し、温水温度の一定化を図るもので
ある。
Therefore, in the absorption heat pump, hot water can be produced in the absorber 6 and the condenser 3 regardless of the presence or absence of heat source water and the temperature level of the heat source water. Incidentally, when the hot water load decreases and the output of the absorption heat pump remains, the thermostat 14 controls the amount of fuel to keep the hot water temperature constant.

上述の様に本考案のボイラ機能付吸収ヒートポ
ンプは、再生器から凝縮器への冷媒蒸気配管から
分岐して吸収器,蒸発器胴に配管を設け、この分
岐配管の途中に熱源水入口または出口温度を検出
するサーモスタツトにて操作される切換用弁を備
えた構成としたことにより、廃熱が不足した場合
にサーモスタツトが感知して弁を自動的に開かせ
るため、高温の冷媒蒸気で吸収器および蒸発器の
圧力を上昇し得るので、熱源水や冷媒の凍結防止
ができ、冷媒蒸気により吸収器および凝縮器で温
水を加熱することもできる。更に、蒸発器への熱
源水の供給がなくとも再生器への加熱の温水を作
るボイラ運転が可能となる等の実用的効果を奏す
る。
As mentioned above, the absorption heat pump with boiler function of the present invention has piping branched from the refrigerant vapor piping from the regenerator to the condenser to the absorber and evaporator body, and a heat source water inlet or outlet is installed in the middle of this branch piping. By having a configuration equipped with a switching valve operated by a thermostat that detects temperature, the thermostat senses when there is insufficient waste heat and automatically opens the valve, so high-temperature refrigerant vapor can be used. Since the pressure of the absorber and the evaporator can be increased, the heat source water and the refrigerant can be prevented from freezing, and the refrigerant vapor can also be used to heat the hot water in the absorber and the condenser. Furthermore, there are practical effects such as being able to operate the boiler to produce hot water for heating the regenerator even without supplying heat source water to the evaporator.

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

第1図は従来の吸収ヒートポンプの説明図、第
2図は本考案の説明図である。 1……再生器、2……分離器、3……凝縮器、
4……蒸発器、5……熱交換器、6……吸収器、
8……冷媒蒸気配管、9……胴、10……分岐配
管、11……弁、12……熱源水供給管、13…
…サーモスタツト。
FIG. 1 is an explanatory diagram of a conventional absorption heat pump, and FIG. 2 is an explanatory diagram of the present invention. 1... Regenerator, 2... Separator, 3... Condenser,
4...evaporator, 5...heat exchanger, 6...absorber,
8... Refrigerant vapor piping, 9... Shell, 10... Branch piping, 11... Valve, 12... Heat source water supply pipe, 13...
...Thermostat.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 再生器からの冷媒蒸気を分離器を介して凝縮器
へ導き、この冷媒液を蒸発器へ導くと共に、前記
分離器より分流せる濃吸収液を熱交換器を経て吸
収器へ導く吸収ヒートポンプにおいて、再生器か
ら凝縮器への冷媒蒸気配管に、吸収器,蒸発器の
胴へ向う分岐配管を分岐接続し、該分岐配管部に
取付けた弁に、前記蒸発器に配管せる熱源水供給
管の熱源水入口又は出口温度を検出するサーモス
タツトを連絡し、且つ再生器の燃焼部に前記凝縮
器を経た熱交換パイプに取付けた他のサーモスタ
ツトを連絡してなるボイラ機能付吸収ヒートポン
プ。
An absorption heat pump that guides refrigerant vapor from a regenerator to a condenser via a separator, guides this refrigerant liquid to an evaporator, and guides a concentrated absorption liquid that can be separated from the separator to the absorber via a heat exchanger, A branch pipe leading to the body of the absorber and evaporator is connected to the refrigerant vapor pipe from the regenerator to the condenser, and a heat source water supply pipe connected to the evaporator is connected to a valve attached to the branch pipe. An absorption heat pump with a boiler function, which is connected to a thermostat that detects the water inlet or outlet temperature, and is connected to another thermostat attached to the heat exchange pipe that passes through the condenser to the combustion section of the regenerator.
JP19252082U 1982-12-20 1982-12-20 Absorption heat pump with boiler function Granted JPS5996565U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19252082U JPS5996565U (en) 1982-12-20 1982-12-20 Absorption heat pump with boiler function

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19252082U JPS5996565U (en) 1982-12-20 1982-12-20 Absorption heat pump with boiler function

Publications (2)

Publication Number Publication Date
JPS5996565U JPS5996565U (en) 1984-06-30
JPS6311571Y2 true JPS6311571Y2 (en) 1988-04-04

Family

ID=30414298

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19252082U Granted JPS5996565U (en) 1982-12-20 1982-12-20 Absorption heat pump with boiler function

Country Status (1)

Country Link
JP (1) JPS5996565U (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5097593B2 (en) * 2008-03-28 2012-12-12 三洋電機株式会社 Absorption heat pump

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5687751A (en) * 1979-12-17 1981-07-16 Ebara Mfg Method of preventing crystallization in water cooling and heating machine

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5844298Y2 (en) * 1979-11-06 1983-10-07 大阪瓦斯株式会社 Absorption heat pump
JPS6018760Y2 (en) * 1980-03-11 1985-06-06 大阪瓦斯株式会社 Absorption heat pump

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5687751A (en) * 1979-12-17 1981-07-16 Ebara Mfg Method of preventing crystallization in water cooling and heating machine

Also Published As

Publication number Publication date
JPS5996565U (en) 1984-06-30

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