JPH04156A - Absorption heat source device - Google Patents
Absorption heat source deviceInfo
- Publication number
- JPH04156A JPH04156A JP9869590A JP9869590A JPH04156A JP H04156 A JPH04156 A JP H04156A JP 9869590 A JP9869590 A JP 9869590A JP 9869590 A JP9869590 A JP 9869590A JP H04156 A JPH04156 A JP H04156A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- heat
- absorption liquid
- heat transfer
- gas
- 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.)
- Granted
Links
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 70
- 239000007788 liquid Substances 0.000 claims abstract description 108
- 239000003507 refrigerant Substances 0.000 claims abstract description 50
- 238000001816 cooling Methods 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 3
- 239000006096 absorbing agent Substances 0.000 claims description 28
- 238000010438 heat treatment Methods 0.000 abstract description 18
- 230000005855 radiation Effects 0.000 abstract description 4
- 239000012530 fluid Substances 0.000 abstract 3
- 230000002745 absorbent Effects 0.000 description 7
- 239000002250 absorbent Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 5
- 238000005057 refrigeration Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、吸収式熱源装置に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to an absorption heat source device.
従来の技術
従来、冷暖房設備の熱源装置としては、吸収式のものが
ある。この吸収式熱源装置は、冷媒(例えば水)を蒸発
させる蒸発器と、この蒸発器で蒸発された冷媒蒸気を吸
収液(例えば臭化リチウム水溶液)に吸収する吸収器と
、この吸収器で冷媒蒸気を吸収して濃度が薄くなった稀
吸収液を加熱する再生器と、この再生器で加熱されて液
体から分離された冷媒蒸気を凝縮させる凝縮器と、上記
再生器で冷媒蒸気が分離されて濃くなった濃吸収液を吸
収器に送る濃吸収液移送管と、途中に溶液ポンプを有し
て上記吸収器で薄くなった稀吸収液を再生器に送る稀吸
収液移送管とから構成されている。そして、この構成に
おいて、室内の冷房運転を行う場合、冷媒の蒸発→吸収
→再生→凝縮という冷凍サイクルを行わせるとともに、
室内機側の熱媒を蒸発器内に導いて冷却させていた。ま
た、室内の暖房運転を行う場合、再生器を作動させると
ともに、室内機側の熱媒を再生器に導いて加熱していた
。2. Description of the Related Art Conventionally, there are absorption type heat source devices for heating and cooling equipment. This absorption heat source device consists of an evaporator that evaporates a refrigerant (e.g., water), an absorber that absorbs the refrigerant vapor evaporated in the evaporator into an absorbing liquid (e.g., lithium bromide aqueous solution), and a refrigerant in the absorber. A regenerator that absorbs vapor and heats the diluted absorption liquid, a condenser that condenses the refrigerant vapor heated by the regenerator and separated from the liquid, and a refrigerant vapor separated by the regenerator. It consists of a concentrated absorption liquid transfer pipe that sends the concentrated absorption liquid that has become concentrated in the absorber to the absorber, and a dilute absorption liquid transfer pipe that has a solution pump in the middle and sends the diluted absorption liquid that has become diluted in the absorber to the regenerator. has been done. In this configuration, when performing indoor cooling operation, a refrigeration cycle of evaporation → absorption → regeneration → condensation of the refrigerant is performed, and
The heat medium from the indoor unit was guided into the evaporator for cooling. Furthermore, when performing indoor heating operation, a regenerator is operated and the heating medium from the indoor unit is guided to the regenerator for heating.
発明が解決しようとする課題
ところで、上記従来の構成によると、暖房運転時におい
ては、再生器で蒸発分離された冷媒蒸気は冷媒蒸気移送
管を介して自然に凝縮器に送られてしまう。このため、
凝縮器が空冷式の場合には、どうしても熱が放出されて
熱損失が生じるという問題があった。Problems to be Solved by the Invention According to the above conventional configuration, during heating operation, the refrigerant vapor evaporated and separated in the regenerator is naturally sent to the condenser via the refrigerant vapor transfer pipe. For this reason,
When the condenser is air-cooled, there is a problem in that heat is inevitably released and heat loss occurs.
そこで、本発明は凝縮器が空冷式の場合でも、熱損失が
生じない吸収式熱源装置を提供することを目的とする。Therefore, an object of the present invention is to provide an absorption type heat source device that does not cause heat loss even when the condenser is air-cooled.
課題を解決するための手段
上記課題を解決するため、本発明の吸収式熱源装置は、
冷媒を蒸発させるとももに内部に伝熱媒体冷却用の第1
伝熱部が配置された蒸発器と、この蒸発器で蒸発された
冷媒蒸気を吸収液に吸収する吸収器と、この吸収器で冷
媒蒸気を吸収して濃度が薄くなった稀吸収液を加熱する
再生器と、この再生器で加熱された気液混合状態の液体
から冷媒蒸気を分離するとともに内部に伝熱媒体冷却用
の第2伝熱部が配置された気液分離器と、この気液分離
器で分離された冷媒蒸気を凝縮させる空冷式の凝縮器と
、上記気液分離器で冷媒蒸気が分離されて濃くなった濃
吸収液を吸収器に送る濃吸収液移送管と、途中に溶液ポ
ンプを有して上記吸収器で薄くなった稀吸収液を再生器
に送る稀吸収液移送管と、途中に第1開閉弁が介装され
るとともに上記気液分離で分離された冷媒蒸気を凝縮器
に移送する冷媒蒸気移送管と、上記凝縮器で凝縮された
冷媒液を上記吸収器に移送する冷媒液移送管と、途中に
介装された切換手段により伝熱媒体を上記第1伝熱部お
よび第2伝熱部のいずれかに循環移送する伝熱媒体循環
移送管と、途中に第2開閉弁が介装されるとともに上記
濃吸収液移送管と稀吸収液移送管とを連通して吸収器を
バイパスさせる吸収液バイパス管と、上記濃吸収液移送
管と稀吸収液移送管との間に設けられて濃吸収液の持つ
熱を稀吸収液に与えて熱回収を行う熱交換器とを具備し
たものである。Means for Solving the Problems In order to solve the above problems, the absorption type heat source device of the present invention includes:
When the refrigerant is evaporated, there is also a first heat transfer medium inside for cooling.
An evaporator in which a heat transfer section is placed, an absorber that absorbs the refrigerant vapor evaporated by the evaporator into an absorption liquid, and this absorber absorbs the refrigerant vapor and heats the diluted absorption liquid. a gas-liquid separator that separates refrigerant vapor from the gas-liquid mixed liquid heated by the regenerator and is provided with a second heat transfer section for cooling the heat transfer medium; An air-cooled condenser that condenses the refrigerant vapor separated by the liquid separator, and a concentrated absorption liquid transfer pipe that sends the concentrated absorption liquid, which is concentrated after the refrigerant vapor is separated by the gas-liquid separator, to the absorber, and A diluted absorption liquid transfer pipe having a solution pump thereon and sending the diluted absorption liquid diluted in the absorber to the regenerator, and a first on-off valve interposed in the middle, and a refrigerant separated by the gas-liquid separation. A refrigerant vapor transfer pipe for transferring vapor to the condenser, a refrigerant liquid transfer pipe for transferring the refrigerant liquid condensed in the condenser to the absorber, and a switching means interposed in the middle to transfer the heat transfer medium to the above-mentioned absorber. A heat transfer medium circulation transfer pipe that circulates and transfers the heat transfer medium to either the first heat transfer section or the second heat transfer section, a second on-off valve interposed in the middle, and the concentrated absorption liquid transfer pipe and the dilute absorption liquid transfer pipe. An absorbent bypass pipe is provided between the concentrated absorbent liquid transfer pipe and the dilute absorbent liquid transfer pipe to communicate with each other and bypass the absorber, and is provided between the concentrated absorbent liquid transfer pipe and the dilute absorbent liquid transfer pipe to transfer the heat of the concentrated absorbent liquid to the dilute absorbent liquid for heat recovery. It is equipped with a heat exchanger that performs
作用
上記構成を冷暖房設備の室外機として使用する場合につ
いて説明する。Function: A case will be described in which the above configuration is used as an outdoor unit of air-conditioning equipment.
まず、冷房運転を行う場合、第1開閉弁が開に、第2開
閉弁が閉に、また切換手段により室内機からの伝熱媒体
が第1伝熱部に循環移送されるようにして、通常の冷凍
サイクルを行なえば、室内機からの伝熱媒体は冷却され
る。First, when performing cooling operation, the first on-off valve is opened, the second on-off valve is closed, and the heat transfer medium from the indoor unit is circulated and transferred to the first heat transfer section by the switching means, If a normal refrigeration cycle is performed, the heat transfer medium from the indoor unit is cooled.
次に、暖房運転を行う場合、第1開閉弁を閉に、第2開
閉弁を開に、また切換手段により室内機からの伝熱媒体
を第2伝熱部に循環移送されるようにするとともに、再
生器および気液分離器を作動させる。すると、気液分離
器内の吸収液は、濃吸収液移送管、吸収液バイパス管お
よび稀吸収液移送管を介して再生器内に循環移送されて
加熱される。この時、室外機からの伝熱媒体は、気液分
離器内の第2伝熱部に移送されているため、吸収液の持
つ熱によって加熱され、暖房サイクルが行われることに
なる。しかも、この暖房サイクルにおいては、気液分離
器内で発生した冷媒蒸気は凝縮器に移送されないので、
凝縮器が空冷式の場合でも、従来のような大気放熱が行
われない。Next, when performing heating operation, the first on-off valve is closed, the second on-off valve is opened, and the heat transfer medium from the indoor unit is circulated and transferred to the second heat transfer section by the switching means. At the same time, the regenerator and gas-liquid separator are operated. Then, the absorption liquid in the gas-liquid separator is circulated and heated in the regenerator via the concentrated absorption liquid transfer pipe, the absorption liquid bypass pipe, and the dilute absorption liquid transfer pipe. At this time, since the heat transfer medium from the outdoor unit is transferred to the second heat transfer section in the gas-liquid separator, it is heated by the heat of the absorption liquid, and a heating cycle is performed. Moreover, in this heating cycle, the refrigerant vapor generated in the gas-liquid separator is not transferred to the condenser.
Even when the condenser is air-cooled, heat is not radiated to the atmosphere like in the past.
実施例 以下、本発明の一実施例を第1図に基づき説明する。Example An embodiment of the present invention will be described below with reference to FIG.
本実施例における吸収式熱源装置は、例えば室内機と室
外機とからなる冷暖房設備の室外機として使用されるも
のについて説明する。The absorption type heat source device in this embodiment will be described, for example, as one used as an outdoor unit of an air-conditioning equipment consisting of an indoor unit and an outdoor unit.
すなわち、この吸収式熱源装置は、冷媒を蒸発させると
ももに内部に室内機(図示せず)との間で熱交換を行う
伝熱媒体(例えば水)の冷却用の第1伝熱管(第1伝熱
部)11が配置された蒸発器1と、この蒸発器1で蒸発
された冷媒蒸気を連通部(例えば連通管)12を介して
導入して吸収液に吸収させる吸収器2と、この吸収器2
で冷媒蒸気を吸収して濃度が薄くなった稀吸収液を加熱
する再生器3と、この再生器3で加熱された気液混合状
態の液体から冷媒蒸気を分離するとともに内部に伝熱媒
体冷却用の第2伝熱管(第2伝熱部)13が配置された
気液分離器4と、この気液分離器4で分離された冷媒蒸
気を凝縮させる空冷式の凝縮器5と、上記気液分離器4
で冷媒蒸気が分離されて濃くなった濃吸収液を吸収器2
に送る濃吸収液移送管14と、途中に溶液ポンプ15を
有して上記吸収器2で薄くなった稀吸収液を再生器3に
送る稀吸収液移送管16と、途中に第1開閉弁17が介
装されるとともに上記気液分離器4で分離された冷媒蒸
気を凝縮器5に移送する冷媒蒸気移送管18と、途中に
冷媒ポンプ19を有するとともに上記凝縮器5で凝縮さ
れた冷媒液を上記吸収器2に移送する冷媒液移送管20
と、途中に介装された切換手段21により伝熱媒体を上
記第1伝熱管11および第2伝熱管13のいずれかに循
環移送する伝熱媒体循環移送管22と、途中に第2開閉
弁23が介装されるとともに上記濃吸収液移送管14と
稀吸収液移送管16とを連通して吸収器2をバイパスさ
せる吸収液バイパス管24と、上記濃吸収液移送管14
と稀吸収液移送管16との間に設けられて濃吸収液の持
つ熱を稀吸収液に与えて熱回収を行う熱交換器25とが
具備されている。That is, this absorption type heat source device evaporates the refrigerant and also has a first heat transfer tube (first heat transfer tube) for cooling a heat transfer medium (for example, water) that exchanges heat with an indoor unit (not shown) inside. 1; an absorber 2 in which refrigerant vapor evaporated in the evaporator 1 is introduced through a communication part (for example, a communication pipe) 12 and absorbed into an absorption liquid; This absorber 2
A regenerator 3 absorbs refrigerant vapor and heats the diluted absorption liquid, and a regenerator 3 separates the refrigerant vapor from the gas-liquid mixed liquid heated by the regenerator 3, and a heat transfer medium cooling device is installed inside. a gas-liquid separator 4 in which a second heat transfer tube (second heat transfer section) 13 is arranged; an air-cooled condenser 5 for condensing the refrigerant vapor separated by the gas-liquid separator 4; Liquid separator 4
The refrigerant vapor is separated and the concentrated absorption liquid is transferred to absorber 2.
A concentrated absorption liquid transfer pipe 14 for sending the concentrated absorption liquid to the regenerator 3, a dilute absorption liquid transfer pipe 16 having a solution pump 15 on the way to send the diluted absorption liquid diluted in the absorber 2 to the regenerator 3, and a first on-off valve on the way. A refrigerant vapor transfer pipe 18 is provided with a refrigerant vapor transfer pipe 17 for transferring the refrigerant vapor separated by the gas-liquid separator 4 to the condenser 5, and a refrigerant pump 19 is provided in the middle, and the refrigerant condensed in the condenser 5 is provided. Refrigerant liquid transfer pipe 20 for transferring liquid to the absorber 2
, a heat transfer medium circulation transfer pipe 22 that circulates and transfers the heat transfer medium to either the first heat transfer tube 11 or the second heat transfer tube 13 by means of a switching means 21 disposed in the middle, and a second on-off valve in the middle. 23 is interposed, and an absorption liquid bypass pipe 24 that connects the concentrated absorption liquid transfer pipe 14 and the dilute absorption liquid transfer pipe 16 to bypass the absorber 2; and the concentrated absorption liquid transfer pipe 14.
A heat exchanger 25 is provided between the absorbing liquid and the dilute absorbing liquid transfer pipe 16 to recover heat by imparting heat of the concentrated absorbing liquid to the dilute absorbing liquid.
また、上記伝熱媒体循環移送管22は、室内機からの伝
熱媒体を第1伝熱管11に移送するための第1移送管3
1と、途中に循環ポンプ32を有するとともに上記第1
伝熱管11と第2伝熱管13とを接続する伝熱媒体移送
用の第2移送管33と、第2伝熱管13からの伝熱媒体
を室内機側に移送するための第3移送管34と、第1移
送管31途中と循環ポンプ32よりも上流側の第2移送
管33途中とを接続する第1接続管35と、第2移送管
33の循環ポンプ32よりも下流側途中と第3移送管3
4途中とを接続する第2接続管36とから構成されてい
る。Further, the heat transfer medium circulation transfer pipe 22 is a first transfer pipe 3 for transferring the heat transfer medium from the indoor unit to the first heat transfer pipe 11.
1, and a circulation pump 32 in the middle, and the above-mentioned first
A second transfer tube 33 for transferring the heat transfer medium that connects the heat transfer tube 11 and the second heat transfer tube 13, and a third transfer tube 34 for transferring the heat transfer medium from the second heat transfer tube 13 to the indoor unit side. , a first connecting pipe 35 that connects the middle of the first transfer pipe 31 and the middle of the second transfer pipe 33 on the upstream side of the circulation pump 32; 3 transfer pipe 3
4, and a second connecting pipe 36 that connects the middle part of the pipe.
さらに、上記切換手段21は、第1移送管31と第1接
続管35との接続箇所に介装された第1三方切換弁41
と、第2移送管33と第2接続管36との接続箇所に介
装された第2三方切換弁42とから構成されている。Further, the switching means 21 includes a first three-way switching valve 41 interposed at a connection point between the first transfer pipe 31 and the first connecting pipe 35.
and a second three-way switching valve 42 interposed at the connection point between the second transfer pipe 33 and the second connection pipe 36.
次に、上記構成における動作について説明する。Next, the operation in the above configuration will be explained.
■冷房運転
冷房運転時においては、第1開閉弁17が開に、第2開
閉弁23が閉に、また第1および第2三方切換弁41.
42を第1図の矢印Aで示す方向に伝熱媒体が流れるよ
うにしておく。■Cooling operation During cooling operation, the first on-off valve 17 is open, the second on-off valve 23 is closed, and the first and second three-way switching valves 41.
42 so that the heat transfer medium flows in the direction shown by arrow A in FIG.
この状態で、上記吸収式熱源装置を作動させて冷凍サイ
クルを行わせるとともに、室内機側の伝熱媒体を吸収器
2内の第1伝熱管11に循環移送させればよい。なお、
この冷凍サイクルについては、従来と同様であるため、
その説明を省略する。In this state, the above-mentioned absorption heat source device is operated to perform a refrigeration cycle, and the heat transfer medium on the indoor unit side is circulated and transferred to the first heat transfer tube 11 in the absorber 2. In addition,
This refrigeration cycle is the same as before, so
The explanation will be omitted.
■暖房運転
暖房運転時においては、第1開閉弁17を閉に、第2開
閉弁23を開に、また第1および第2三方切換弁41,
42を第1図の矢印Bで示す方向に伝熱媒体が流れるよ
うにしておく。■Heating operation During heating operation, the first on-off valve 17 is closed, the second on-off valve 23 is opened, and the first and second three-way switching valves 41,
42 so that the heat transfer medium flows in the direction shown by arrow B in FIG.
この状態で、再生器3、気液分離器4、溶液ポンプ15
および循環ポンプ32を作動させる。In this state, the regenerator 3, gas-liquid separator 4, solution pump 15
and operates the circulation pump 32.
すると、室外機である吸収式熱源装置側の気液分離器4
内に溜っている吸収液は、濃吸収液移送管14、吸収液
バイパス管24および稀吸収液移送管16を介して再生
器3内に移送されて加熱された後、気液分離器4内に戻
され、以後このサイクルが繰り返されることになる。一
方、室内機側の伝熱媒体は、第1移送管31、第1接続
管35および第2移送管33を介して気液分離器4内の
第2伝熱管13に移送され、ここで再生器3で加熱され
て移送されてきた吸収液の持つ熱によって加熱される。Then, the gas-liquid separator 4 on the side of the absorption heat source device which is the outdoor unit
The absorption liquid accumulated in the gas-liquid separator 4 is transferred to the regenerator 3 through the concentrated absorption liquid transfer pipe 14, the absorption liquid bypass pipe 24, and the dilute absorption liquid transfer pipe 16, where it is heated. This cycle will then be repeated. On the other hand, the heat transfer medium on the indoor unit side is transferred to the second heat transfer pipe 13 in the gas-liquid separator 4 via the first transfer pipe 31, first connection pipe 35, and second transfer pipe 33, and is recycled here. It is heated by the heat of the absorption liquid that has been heated and transferred in the vessel 3.
そして、この第2伝熱管13内で加熱された伝熱媒体は
、第3移送管34を介して室内機側に戻されて熱源とし
て使用される。The heat transfer medium heated within the second heat transfer tube 13 is returned to the indoor unit via the third transfer tube 34 and used as a heat source.
このように暖房運転時においては、冷媒蒸気は凝縮器5
に移送されないので、従来のように大気放熱による熱損
失が生じないとともに、吸収液は吸収器2に移送されな
いので、やはり余分な熱損失が生じない。In this way, during heating operation, the refrigerant vapor is transferred to the condenser 5.
Since the absorption liquid is not transferred to the absorber 2, there is no heat loss due to atmospheric heat radiation as in the conventional case, and since the absorption liquid is not transferred to the absorber 2, no extra heat loss occurs.
なお、上記実施例においては、暖房運転時に第1接続管
35を介して蒸発器1をバイパスさせたが、場合によっ
ては、伝熱媒体を蒸発器1内を通過させるようにしても
よい。In the above embodiment, the evaporator 1 was bypassed via the first connecting pipe 35 during heating operation, but the heat transfer medium may be passed through the evaporator 1 depending on the case.
また、上記実施例における三方切換弁41,42の替わ
りに、それぞれ2個の開閉弁を用いて同様の機能を持た
せることもできる。Further, instead of the three-way switching valves 41 and 42 in the above embodiment, two on-off valves may be used to provide the same function.
また、第2図および第3図に示すように、暖房運転時の
熱効率を高めるために、第2移送管33と濃吸収液移送
管14との間、または第2移送管33と稀吸収液移送管
16との間で熱交換を行う熱交換器51.52を設ける
ようにしてもよい。In addition, as shown in FIGS. 2 and 3, in order to increase thermal efficiency during heating operation, between the second transfer pipe 33 and the concentrated absorption liquid transfer pipe 14, or between the second transfer pipe 33 and the dilute absorption liquid Heat exchangers 51 and 52 for exchanging heat with the transfer pipe 16 may be provided.
さらに、上記実施例においては、第1伝熱部として伝熱
管を示したが、例えば第4図に示すように、フラッシュ
式のものを採用してもよく、この場合、暖房時における
伝熱媒体は第1接続管35を介して第2伝熱部に循環移
送される。Further, in the above embodiment, a heat transfer tube is shown as the first heat transfer section, but a flash type may be adopted, for example, as shown in FIG. is circulated and transferred to the second heat transfer section via the first connecting pipe 35.
発明の効果
以上のように本発明の構成によると、気液分離器から凝
縮器に冷媒蒸気を移送する冷媒蒸気移送管途中に第1開
閉弁を介装したので、例えば室内機からの伝熱媒体を再
生器に導いて暖房運転を行う場合に、気液分離器で発生
した冷媒蒸気は凝縮器には移動しないため、空冷式の凝
縮器を使用した場合でも、従来のような大気放熱による
熱損失が生じない。Effects of the Invention As described above, according to the configuration of the present invention, the first on-off valve is interposed in the middle of the refrigerant vapor transfer pipe that transfers refrigerant vapor from the gas-liquid separator to the condenser. When conducting heating operation by guiding the medium to the regenerator, the refrigerant vapor generated in the gas-liquid separator does not move to the condenser, so even if an air-cooled condenser is used, it will not be affected by the conventional atmospheric heat radiation. No heat loss occurs.
第1図は本発明の一実施例を示す全体概略構成図、第2
図および第3図は本実施例の変形例を示す要部概略構成
図、第4図は第1伝熱部の他の実施例を示す要部概略構
成図である。
1・・・・蒸発器、2・・・・吸収器、3・・・・再生
器、4・・・・気液分離器、6・・・・凝縮器、11・
・・・第1伝熱管、12・・・・冷媒蒸気移送管、13
・・・・第2伝熱管、14・・・・濃吸収液移送管、1
5・・・・溶液ポンプ、16・・・・稀吸収液移送管、
17・・・・第1開閉弁、18・・・・冷媒蒸気移送管
、20・−76媒液移送管、21・・・・切換手段、2
2・・・・伝熱媒体循環移送管、23・・・・第2開閉
弁、24・・・・稀吸収液バイパス管、25・・・・熱
交換器。FIG. 1 is an overall schematic configuration diagram showing one embodiment of the present invention, and FIG.
3 and 3 are schematic diagrams showing the main parts of a modified example of the present embodiment, and FIG. 4 is a schematic diagram of the main parts showing another embodiment of the first heat transfer section. 1... Evaporator, 2... Absorber, 3... Regenerator, 4... Gas-liquid separator, 6... Condenser, 11...
...first heat transfer tube, 12...refrigerant vapor transfer tube, 13
...Second heat transfer tube, 14...Concentrated absorption liquid transfer pipe, 1
5... Solution pump, 16... Dilute absorption liquid transfer pipe,
17...First on-off valve, 18...Refrigerant vapor transfer pipe, 20-76 medium liquid transfer pipe, 21...Switching means, 2
2... Heat transfer medium circulation transfer pipe, 23... Second on-off valve, 24... Dilute absorption liquid bypass pipe, 25... Heat exchanger.
Claims (1)
第1伝熱部が配置された蒸発器と、この蒸発器で蒸発さ
れた冷媒蒸気を吸収液に吸収する吸収器と、この吸収器
で冷媒蒸気を吸収して濃度が薄くなった稀吸収液を加熱
する再生器と、この再生器で加熱された気液混合状態の
液体から冷媒蒸気を分離するとともに内部に伝熱媒体冷
却用の第2伝熱部が配置された気液分離器と、この気液
分離器で分離された冷媒蒸気を凝縮させる空冷式の凝縮
器と、上記気液分離器で冷媒蒸気が分離されて濃くなっ
た濃吸収液を吸収器に送る濃吸収液移送管と、途中に溶
液ポンプを有して上記吸収器で薄くなった稀吸収液を再
生器に送る稀吸収液移送管と、途中に第1開閉弁が介装
されるとともに上記気液分離で分離された冷媒蒸気を凝
縮器に移送する冷媒蒸気移送管と、上記凝縮器で凝縮さ
れた冷媒液を上記吸収器に移送する冷媒液移送管と、途
中に介装された切換手段により伝熱媒体を上記第1伝熱
部および第2伝熱部のいずれかに循環移送する伝熱媒体
循環移送管と、途中に第2開閉弁が介装されるとともに
上記濃吸収液移送管と稀吸収液移送管とを連通して吸収
器をバイパスさせる吸収液バイパス管と、上記濃吸収液
移送管と稀吸収液移送管との間に設けられて濃吸収液の
持つ熱を稀吸収液に与えて熱回収を行う熱交換器とを具
備したことを特徴とする吸収式熱源装置。1. An evaporator that evaporates refrigerant and has a first heat transfer section disposed therein for cooling the heat transfer medium; an absorber that absorbs the refrigerant vapor evaporated by the evaporator into an absorption liquid; A regenerator that absorbs refrigerant vapor in an absorber and heats the diluted absorption liquid, and a regenerator that separates the refrigerant vapor from the gas-liquid mixed liquid heated by the regenerator, and a heat transfer medium cooling device inside. a gas-liquid separator in which a second heat transfer section is arranged; an air-cooled condenser for condensing the refrigerant vapor separated by the gas-liquid separator; A concentrated absorption liquid transfer pipe that sends the concentrated concentrated absorption liquid to the absorber, a dilute absorption liquid transfer pipe that has a solution pump in the middle and sends the diluted absorption liquid that has become diluted in the absorber to the regenerator, and A refrigerant vapor transfer pipe that is provided with a first on-off valve and that transfers the refrigerant vapor separated by the gas-liquid separation to the condenser; and a refrigerant liquid that transfers the refrigerant liquid condensed in the condenser to the absorber. A transfer pipe, a heat transfer medium circulation transfer pipe that circulates and transfers the heat transfer medium to either the first heat transfer section or the second heat transfer section by means of a switching means interposed in the middle, and a second on-off valve in the middle. is interposed between an absorption liquid bypass pipe that connects the concentrated absorption liquid transfer pipe and the dilute absorption liquid transfer pipe to bypass the absorber, and the concentrated absorption liquid transfer pipe and the dilute absorption liquid transfer pipe. What is claimed is: 1. An absorption heat source device comprising: a heat exchanger that is provided to recover heat by imparting heat possessed by a concentrated absorption liquid to a dilute absorption liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9869590A JPH086981B2 (en) | 1990-04-13 | 1990-04-13 | Absorption heat source device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9869590A JPH086981B2 (en) | 1990-04-13 | 1990-04-13 | Absorption heat source device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04156A true JPH04156A (en) | 1992-01-06 |
| JPH086981B2 JPH086981B2 (en) | 1996-01-29 |
Family
ID=14226642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9869590A Expired - Lifetime JPH086981B2 (en) | 1990-04-13 | 1990-04-13 | Absorption heat source device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH086981B2 (en) |
-
1990
- 1990-04-13 JP JP9869590A patent/JPH086981B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH086981B2 (en) | 1996-01-29 |
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