JPH04268175A - Absorption heat source device - Google Patents
Absorption heat source deviceInfo
- Publication number
- JPH04268175A JPH04268175A JP2659791A JP2659791A JPH04268175A JP H04268175 A JPH04268175 A JP H04268175A JP 2659791 A JP2659791 A JP 2659791A JP 2659791 A JP2659791 A JP 2659791A JP H04268175 A JPH04268175 A JP H04268175A
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- absorber
- refrigerant
- regenerator
- absorption liquid
- 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 description 80
- 239000007788 liquid Substances 0.000 claims description 73
- 239000006096 absorbing agent Substances 0.000 claims description 63
- 239000003507 refrigerant Substances 0.000 claims description 63
- 239000012530 fluid Substances 0.000 claims description 20
- 238000010438 heat treatment Methods 0.000 claims description 16
- 230000008929 regeneration Effects 0.000 claims description 13
- 238000011069 regeneration method Methods 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 10
- 230000008020 evaporation Effects 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 230000002745 absorbent Effects 0.000 description 7
- 239000002250 absorbent Substances 0.000 description 7
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 230000009102 absorption Effects 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
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
【0001】0001
【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。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption heat source device.
【0002】0002
【従来の技術】空調設備に使用される熱源装置として、
吸収式のものがある。従来、この種の吸収式熱源装置(
より具体的には冷温水機)は、蒸発器、吸収器、再生器
および凝縮器などを有しており、冷房時には、冷凍サイ
クルが行われ、また暖房時には、暖房サイクルが行われ
ていた。[Prior Art] As a heat source device used in air conditioning equipment,
There are absorption types. Conventionally, this type of absorption heat source device (
More specifically, a water cooler/heater (water cooler/heater) has an evaporator, an absorber, a regenerator, a condenser, etc., and performs a refrigeration cycle during cooling, and a heating cycle during heating.
【0003】また、上記冷房サイクルでは、冷媒の蒸発
→吸収→再生→凝縮の各作用が行われ吸収冷凍サイクル
により冷房用冷水を製造していた。一方、暖房サイクル
では、吸収液が燃料や高温の蒸気、水により再生器で加
熱され、発生した水蒸気により直接暖用の温水を加熱製
造していた。[0003] Furthermore, in the above-mentioned cooling cycle, the following actions of evaporation, absorption, regeneration, and condensation of the refrigerant are carried out to produce cold water for cooling through the absorption refrigeration cycle. On the other hand, in the heating cycle, the absorption liquid is heated in a regenerator using fuel, high-temperature steam, and water, and the generated steam is used to directly heat and produce hot water for warming purposes.
【0004】0004
【発明が解決しようとする課題】上記従来の構成による
と、暖房サイクルでは、装置自体はヒートポンプの機能
を有しているにもかかわらず、吸収液の結晶限界により
、低温の熱源から熱を汲み上げて暖房に利用することが
できず、したがって熱効率が悪く不経済であるという問
題があった。[Problems to be Solved by the Invention] According to the above-mentioned conventional configuration, in the heating cycle, although the device itself has the function of a heat pump, heat is pumped up from a low-temperature heat source due to the crystallization limit of the absorption liquid. Therefore, there was a problem that the heat efficiency was poor and it was uneconomical.
【0005】そこで、本発明は暖房サイクルにおいても
、低温の熱源が利用できる吸収式熱源装置をを提供する
ことを目的とする。[0005] Accordingly, an object of the present invention is to provide an absorption type heat source device that can utilize a low-temperature heat source even in a heating cycle.
【0006】[0006]
【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、熱交換流体が供給される
蒸発器と、蒸発兼吸収器と、吸収器と、再生器と、再生
兼凝縮器と、凝縮器と、この凝縮器内と上記再生兼凝縮
器内とを連通させる連通管と、上記再生器で蒸発された
冷媒を上記再生兼凝縮器内の伝熱管内に移送する冷媒移
送管と、上記再生兼凝縮器内の伝熱管からの冷媒を上記
凝縮器に移送する冷媒移送管と、上記凝縮器からの冷媒
を上記蒸発器内および蒸発兼吸収器の伝熱管内に移送す
る冷媒移送管と、上記再生器で分離された濃吸収液を上
記吸収器内および上記再生兼凝縮器内に移送する濃吸収
液移送管と、上記再生兼凝縮器からの濃吸収液を上記吸
収器および上記蒸発兼吸収器内に移送する濃吸収液移送
管と、上記吸収器で冷媒を吸収して希釈された稀吸収液
を上記再生器に移送する稀吸収液移送管と、上記蒸発兼
吸収器で冷媒を吸収して希釈された稀吸収液を上記再生
兼凝縮器に移送する稀吸収液移送管と、熱交換流体を上
記吸収器および上記凝縮器内の各伝熱管内に移送する熱
交換流体移送管とから構成し、かつ暖房サイクル作動時
には、上記再生器と吸収器との間で吸収液を循環させる
ようになすとともに、上記再生兼凝縮器と蒸発兼吸収器
との間で吸収液を循環させるようになし、また冷房サイ
クル作動時には、上記蒸発器で蒸発された冷媒を上記吸
収器に直接移送するとともに、再生器で分離された濃吸
収液を上記再生兼凝縮器を介して上記吸収器内に移送さ
せるようにしたものである。[Means for Solving the Problems] In order to solve the above problems, an absorption type heat source device of the present invention includes an evaporator to which a heat exchange fluid is supplied, an evaporator/absorber, an absorber, a regenerator, a regenerator and condenser, a condenser, a communication pipe that communicates the inside of the condenser with the inside of the regenerator and condenser, and transfers the refrigerant evaporated in the regenerator to a heat transfer tube in the regenerator and condenser. A refrigerant transfer pipe that transfers the refrigerant from the heat transfer tube in the regeneration/condenser to the condenser, and a refrigerant transfer pipe that transfers the refrigerant from the condenser to the evaporator and the heat transfer tube of the evaporator/absorber. A refrigerant transfer pipe that transfers the concentrated absorption liquid separated by the regenerator to the absorber and the regeneration/condenser, and a concentrated absorption liquid transfer pipe that transfers the concentrated absorption liquid separated by the regenerator to the regeneration/condenser. a concentrated absorption liquid transfer pipe that transfers the refrigerant into the absorber and the evaporator/absorber, and a dilute absorption liquid transfer pipe that transfers the diluted diluted absorption liquid by absorbing the refrigerant in the absorber to the regenerator. A dilute absorption liquid transfer pipe that absorbs the refrigerant in the evaporator/absorber and transfers the diluted diluted absorption liquid to the regeneration/condenser, and a heat exchange fluid in each heat transfer tube in the absorber and the condenser. and a heat exchange fluid transfer pipe for transferring the heat exchange fluid to the regenerator and absorber, and when the heating cycle is in operation, the absorption liquid is circulated between the regenerator and the absorber, and the regenerator/condenser and the evaporator/absorber During the operation of the cooling cycle, the refrigerant evaporated in the evaporator is directly transferred to the absorber, and the concentrated absorption liquid separated in the regenerator is regenerated and condensed. The liquid is transferred into the absorber through a container.
【0007】[0007]
【作用】上記構成において、暖房運転を行う際には、吸
収液が吸収器と再生器との間、および蒸発兼吸収器と再
生兼凝縮器との間で独立して循環させられる。[Operation] In the above structure, during heating operation, the absorption liquid is circulated independently between the absorber and the regenerator, and between the evaporator/absorber and the regenerator/condenser.
【0008】すなわち、再生器で蒸発分離された冷媒は
再生兼凝縮器および凝縮器で凝縮された後、冷媒移送管
を介して蒸発器および蒸発兼吸収器に移送される。蒸発
器では例えば低温の河川水により、冷媒が蒸発され、こ
の蒸発された冷媒が蒸発兼吸収器内に移送され、ここで
吸収液に吸収されて発熱し、この発熱により伝熱管内を
通過する冷媒を蒸発させる。そして、この伝熱管から出
た冷媒が吸収器内に移送され、ここで本来の吸収作用が
行われ、その伝熱管内を通過する熱交換流体である温水
を加熱する。また、ここで加熱された温水は、凝縮器内
の伝熱管を通過する際に、凝縮熱を奪いさらに加熱され
る。That is, the refrigerant evaporated and separated in the regenerator is condensed in the regenerator/condenser and the condenser, and then transferred to the evaporator and the evaporator/absorber via the refrigerant transfer pipe. In the evaporator, the refrigerant is evaporated by, for example, low-temperature river water, and the evaporated refrigerant is transferred to the evaporator/absorber, where it is absorbed by the absorption liquid and generates heat, which causes it to pass through the heat transfer tube. Evaporate the refrigerant. The refrigerant discharged from the heat transfer tube is transferred into the absorber, where the original absorption action takes place and heats the hot water, which is the heat exchange fluid, that passes through the heat transfer tube. Furthermore, when the hot water heated here passes through a heat transfer tube in the condenser, it absorbs condensation heat and is further heated.
【0009】このように、吸収が2段で行われるため、
蒸発器の熱源流体として低温の熱源、例えば河川水を利
用して暖房を行うことができる。また、冷房運転時には
、蒸発兼吸収器を使用せずに、再生器、凝縮器、蒸発器
、低温再生器および吸収器だけを使用して吸収サイクル
を行わせることにより、通常の冷房サイクルを行わせる
。[0009] In this way, since absorption is performed in two stages,
Heating can be performed using a low-temperature heat source, such as river water, as the heat source fluid for the evaporator. In addition, during cooling operation, the normal cooling cycle is performed by performing the absorption cycle using only the regenerator, condenser, evaporator, low-temperature regenerator, and absorber without using the evaporator/absorber. let
【0010】0010
【実施例】以下、本発明の一実施例を図1に基づき説明
する。本実施例に係る吸収式熱源装置は、伝熱管11を
有するとともにこの伝熱管11内に熱交換流体が供給さ
れる蒸発器1と、内部に伝熱管12が配置された蒸発兼
吸収器2、内部に伝熱管13が配置された吸収器3と、
再生器4と、内部に伝熱管15が配置された再生兼凝縮
器5と、内部に伝熱管16が配置された凝縮器6と、こ
の凝縮器6内と再生兼凝縮器5内とを連通させる連通管
21と、再生器4で蒸発された冷媒を再生兼凝縮器5内
の伝熱管15内に移送する第1冷媒移送管22と、再生
兼凝縮器5内の伝熱管15からの冷媒を凝縮器6に移送
する第2冷媒移送管23と、凝縮器6からの冷媒を蒸発
器1および蒸発兼吸収器2の伝熱管12内に移送する第
3冷媒移送管24と、途中に開閉弁41が介装され、か
つ一端が上記第3冷媒移送管24途中に接続されるとと
もに他端が蒸発兼吸収器2内の伝熱管12に接続された
第4冷媒移送管25と、途中に開閉弁42が介装されて
上記蒸発器1内の冷媒を蒸発兼吸収器2に移送する第5
冷媒移送管26と、上記蒸発兼吸収器2内の伝熱管12
内の冷媒を吸収器3内に移送する第6冷媒移送管27と
、途中に開閉弁43が介装されて上記再生器4で分離さ
れた濃吸収液を吸収器3内に移送する第1濃吸収液移送
管31と、途中に開閉弁44が介装され、かつ一端が上
記第1濃吸収液移送管31に接続されるとともに他端が
上記再生兼凝縮器5に接続された第2濃吸収液移送管3
2と、途中に開閉弁45が介装されて上記再生兼凝縮器
5で再生された濃吸収液を蒸発器3に移送する第3濃吸
収液移送管33と、途中に開閉弁46が介装され、かつ
一端が第3濃吸収液移送管33途中に接続されるととも
に他端が蒸発兼吸収器2に接続された第4濃吸収液移送
管34と、途中に溶液ポンプ71および開閉弁47が介
装され、かつ吸収器3で冷媒を吸収して希釈された稀吸
収液を再生器4に移送する第1稀吸収液移送管36と、
途中に溶液ポンプ72および開閉弁48,49が介装さ
れ、かつ蒸発兼吸収器2で冷媒を吸収して希釈された稀
吸収液を再生兼凝縮器5に移送する第2稀吸収液移送管
37と、それぞれ途中に開閉弁51,52が介装される
とともに上記第1稀吸収液移送管36および第2稀吸収
液移送管37の途中同士を2箇所で互いに接続する第1
および第2吸収液バイパス管61,62と、途中に開閉
弁53が介装されて第5冷媒移送管26と第6冷媒移送
管27とを接続して蒸発兼吸収器2をバイパスする冷媒
バイパス管63と、蒸発器1の伝熱管11内に熱交換流
体を移送する第1熱交換流体移送管38と、熱交換流体
を吸収器3および凝縮器6の各伝熱管13,16内に移
送する第2熱交換流体移送管39と、途中に冷媒ポンプ
73が介装されて上記蒸発器1内の冷媒を循環移動させ
る冷媒循環管28と、上記第1濃吸収液移送管31と第
1吸収液移送管36との間、および第3濃吸収液移送間
33と第2稀吸収液移送管37との間で互いに熱交換を
行い、濃吸収液の持つ熱を稀吸収液に回収するための熱
交換器7,8とから構成されている。[Embodiment] An embodiment of the present invention will be described below with reference to FIG. The absorption type heat source device according to this embodiment includes an evaporator 1 having a heat exchanger tube 11 and into which a heat exchange fluid is supplied, an evaporator/absorber 2 having a heat exchanger tube 12 disposed therein, an absorber 3 in which a heat exchanger tube 13 is arranged;
The regenerator 4, the regenerator/condenser 5 in which the heat transfer tube 15 is arranged, the condenser 6 in which the heat transfer tube 16 is arranged, and the inside of this condenser 6 and the inside of the regenerator/condenser 5 are communicated. a first refrigerant transfer pipe 22 that transfers the refrigerant evaporated in the regenerator 4 into the heat exchanger tube 15 in the regenerator/condenser 5; A second refrigerant transfer pipe 23 transfers the refrigerant to the condenser 6, and a third refrigerant transfer pipe 24 transfers the refrigerant from the condenser 6 into the heat transfer tubes 12 of the evaporator 1 and the evaporator/absorber 2. A fourth refrigerant transfer pipe 25 is provided with a valve 41, and one end is connected to the third refrigerant transfer pipe 24 midway, and the other end is connected to the heat transfer pipe 12 in the evaporator/absorber 2; A fifth valve is provided with an on-off valve 42 to transfer the refrigerant in the evaporator 1 to the evaporator/absorber 2.
A refrigerant transfer pipe 26 and a heat transfer pipe 12 in the evaporator/absorber 2
a sixth refrigerant transfer pipe 27 that transfers the refrigerant inside the absorber 3 into the absorber 3; and a first refrigerant transfer pipe 27 with an on-off valve 43 interposed in the middle to transfer the concentrated absorption liquid separated in the regenerator 4 into the absorber 3. A second condensed liquid transfer pipe 31 and a second condensed liquid transfer pipe 31 having an on-off valve 44 interposed therebetween, one end of which is connected to the first concentrated absorption liquid transfer pipe 31 and the other end connected to the regenerator and condenser 5. Concentrated absorption liquid transfer tube 3
2, a third concentrated absorption liquid transfer pipe 33 with an on-off valve 45 interposed in the middle to transfer the concentrated absorption liquid regenerated in the regeneration/condenser 5 to the evaporator 3, and a third concentrated absorption liquid transfer pipe 33 with an on-off valve 46 interposed in the middle. A fourth concentrated absorption liquid transfer pipe 34 is installed, and one end is connected to the middle of the third concentrated absorption liquid transfer pipe 33, and the other end is connected to the evaporator/absorber 2, and a solution pump 71 and an on-off valve are connected to the middle of the fourth concentrated absorption liquid transfer pipe 34. 47 is interposed, and a first dilute absorption liquid transfer pipe 36 that transfers the diluted diluted absorption liquid by absorbing the refrigerant in the absorber 3 to the regenerator 4;
A second dilute absorption liquid transfer pipe, in which a solution pump 72 and on-off valves 48 and 49 are interposed, and which transfers the diluted diluted absorption liquid by absorbing the refrigerant in the evaporator/absorber 2 to the regeneration/condenser 5 37, and a first diode, in which on-off valves 51 and 52 are interposed in the middle, respectively, and the first dilute absorbent liquid transfer pipe 36 and the second dilute absorbent liquid transfer pipe 37 are connected to each other at two points in the middle.
and a refrigerant bypass that bypasses the evaporator/absorber 2 by connecting the second absorption liquid bypass pipes 61 and 62 and the fifth refrigerant transfer pipe 26 and the sixth refrigerant transfer pipe 27 with an on-off valve 53 interposed therebetween. a first heat exchange fluid transfer tube 38 for transferring the heat exchange fluid into the heat exchange tube 11 of the evaporator 1 and a first heat exchange fluid transfer tube 38 for transferring the heat exchange fluid into each heat exchange tube 13, 16 of the absorber 3 and condenser 6; a second heat exchange fluid transfer pipe 39, a refrigerant circulation pipe 28 having a refrigerant pump 73 interposed therebetween to circulate and move the refrigerant in the evaporator 1, Heat exchange is performed between the absorbent liquid transfer pipe 36 and between the third concentrated absorbent liquid transfer pipe 33 and the second dilute absorbent liquid transfer pipe 37, and the heat of the concentrated absorbent liquid is recovered to the dilute absorbent liquid. It consists of heat exchangers 7 and 8 for.
【0011】次に、上記構成における作用について説明
する。
■暖房運転時(暖房サイクル作動時)
暖房運転時には、開閉弁44,45,51,52,53
が閉状態(図中、黒く塗り潰した箇所)にされるととも
に、残りの開閉弁が開状態にされて、吸収液が吸収器3
と再生器4との間、および蒸発兼吸収器2と再生兼凝縮
器5との間で独立して循環させられる。Next, the operation of the above configuration will be explained. ■During heating operation (during heating cycle operation) During heating operation, on-off valves 44, 45, 51, 52, 53
is closed (blacked out area in the diagram), and the remaining on-off valves are opened, allowing the absorption liquid to flow into the absorber 3.
and the regenerator 4, and between the evaporator/absorber 2 and the regenerator/condenser 5.
【0012】すなわち、再生器4で蒸発分離された冷媒
は再生兼凝縮器5および凝縮器6で2重に凝縮された後
、第3および第4冷媒移送管24,25を介して蒸発器
1および蒸発兼吸収器2に移送される。That is, the refrigerant evaporated and separated in the regenerator 4 is doubly condensed in the regenerator/condenser 5 and the condenser 6, and then transferred to the evaporator 1 via the third and fourth refrigerant transfer pipes 24 and 25. and transferred to the evaporator/absorber 2.
【0013】蒸発器1では熱交換流体である低温の熱源
、例えば低温の河川水により、冷媒が蒸発され、この蒸
発された冷媒が蒸発兼吸収器2内に移送され、ここで吸
収液に吸収されて発熱し、この発熱により伝熱管12内
を通過する冷媒を蒸発させる。そして、この伝熱管12
から出た冷媒が吸収器3内に移送され、ここで本来の吸
収作用が行われ、その伝熱管13内を通過する熱交換流
体である温水を加熱する。また、ここで加熱された温水
は、凝縮器6内の伝熱管16を通過する際に、凝縮熱を
奪いさらに加熱される。例えば、40℃の温水は47℃
に加熱される。なお、河川水は例えば12℃から7℃に
冷却される。In the evaporator 1, the refrigerant is evaporated by a low-temperature heat source that is a heat exchange fluid, such as low-temperature river water, and the evaporated refrigerant is transferred to the evaporator/absorber 2, where it is absorbed by an absorption liquid. This heat generation causes the refrigerant passing through the heat transfer tubes 12 to evaporate. And this heat exchanger tube 12
The refrigerant discharged from the absorber 3 is transferred to the absorber 3, where the original absorption action takes place and heats the hot water, which is the heat exchange fluid, passing through the heat exchanger tubes 13. Moreover, when the hot water heated here passes through the heat transfer tube 16 in the condenser 6, it absorbs condensation heat and is further heated. For example, 40℃ hot water is 47℃
is heated to. Note that the river water is cooled, for example, from 12°C to 7°C.
【0014】このように、吸収を2段に行うようにした
ので、低温の熱源、例えば河川水を利用して暖房を行う
ことができ、また再生を2重効用式にしたのと相まって
、駆動熱源熱量が1.0に対し、出力温水熱量が1.5
となる。[0014] Since absorption is performed in two stages in this way, heating can be performed using a low-temperature heat source, such as river water. Heat source heat amount is 1.0, output hot water heat amount is 1.5
becomes.
【0015】一方、吸収器3で吸収液を吸収して希釈さ
れた稀吸収液は、第1稀吸収液移送管36を介して再生
器4に移送されて加熱再生され、また蒸発兼吸収器2で
同様に生じた稀吸収液は第2稀吸収液移送管37を介し
て再生兼凝縮器5に移送され、ここで再生器4からの冷
媒蒸気の持つ熱により加熱されて再生が行われる。On the other hand, the diluted absorption liquid that has been diluted by absorbing the absorption liquid in the absorber 3 is transferred to the regenerator 4 via the first diluted absorption liquid transfer pipe 36 to be heated and regenerated. The diluted absorption liquid similarly generated in step 2 is transferred to the regeneration/condenser 5 via the second diluted absorption liquid transfer pipe 37, where it is heated by the heat of the refrigerant vapor from the regenerator 4 and regenerated. .
【0016】勿論、再生兼凝縮器5で蒸発された冷媒は
、連通管21を介して凝縮器6内に移送されてここで凝
縮される。
■冷房運転時(冷房サイクル作動時)
冷房運転時には、上述した暖房運転時とは異なり、開閉
弁44,45,51,52,53だけが開状態にされる
とともに、残りの開閉弁が閉状態にされ、そして吸収液
が吸収器3だけに移送される。Of course, the refrigerant evaporated in the regeneration/condenser 5 is transferred to the condenser 6 via the communication pipe 21 and condensed there. ■During cooling operation (during cooling cycle operation) During cooling operation, unlike during heating operation described above, only the on-off valves 44, 45, 51, 52, and 53 are opened, and the remaining on-off valves are closed. and the absorption liquid is transferred only to the absorber 3.
【0017】すなわち、再生器4で蒸発された冷媒は再
生兼凝縮器5および凝縮器6を経て凝縮され、蒸発器1
に移送される。そして、ここで伝熱管11内を通過する
熱交換流体である冷水を冷却する。一方、蒸発器1で蒸
発された冷媒は、冷媒バイパス管63を介して吸収器3
に直接移送され、吸収液に吸収される。ここで生じた吸
収液は第1稀吸収液移送管36、第1吸収液バイパス管
61、第2稀吸収液移送管37、第2吸収液バイパス管
62および第1稀吸収液移送管36を介して再生器4内
に移送される。再生器4内で蒸発された冷媒は、上述し
たように再生兼凝縮器5内に移送され、他方再生器4内
の濃吸収液は第1濃吸収液移送管31および第2濃吸収
液移送管32を介して再生兼凝縮器5内に移送され、そ
の後第3濃吸収液移管33を介して吸収器3に移送され
る。That is, the refrigerant evaporated in the regenerator 4 passes through the regenerator/condenser 5 and the condenser 6, and is condensed.
will be transferred to. Then, the cold water that is the heat exchange fluid passing through the heat exchanger tube 11 is cooled. On the other hand, the refrigerant evaporated in the evaporator 1 is transferred to the absorber 3 via the refrigerant bypass pipe 63.
and absorbed into the absorption liquid. The absorption liquid generated here passes through the first dilute absorption liquid transfer pipe 36, the first absorption liquid bypass pipe 61, the second dilute absorption liquid transfer pipe 37, the second absorption liquid bypass pipe 62, and the first dilute absorption liquid transfer pipe 36. It is transferred into the regenerator 4 through the regenerator 4. The refrigerant evaporated in the regenerator 4 is transferred to the regenerator/condenser 5 as described above, while the concentrated absorption liquid in the regenerator 4 is transferred to the first concentrated absorption liquid transfer pipe 31 and the second concentrated absorption liquid transfer pipe. It is transferred to the regenerator/condenser 5 via the pipe 32 and then transferred to the absorber 3 via the third concentrated absorption liquid transfer line 33.
【0018】なお、河川水などの冷却水は、第2熱交換
流体供給管39を介して吸収器3および凝縮器6内を冷
却している。Note that the cooling water such as river water cools the inside of the absorber 3 and the condenser 6 via the second heat exchange fluid supply pipe 39.
【0019】[0019]
【発明の効果】以上のように本発明の構成によると、暖
房運転を行う際には、吸収器と蒸発器との間に蒸発兼吸
収器および再生兼凝縮器を装備し、吸収液を循環させる
ようにしているので、吸収を2段に行わせることができ
、したがって蒸発器の熱源流体として低温の熱源、例え
ば河川水を利用して暖房を行うことができるので、熱効
率を改善でき非常に経済的である。As described above, according to the configuration of the present invention, when performing heating operation, an evaporator/absorber and a regenerator/condenser are installed between the absorber and the evaporator, and the absorption liquid is circulated. As a result, absorption can be carried out in two stages, and therefore, heating can be performed using a low-temperature heat source, such as river water, as the heat source fluid for the evaporator, which can greatly improve thermal efficiency. Economical.
【図1】図1は本発明の一実施例における吸収式熱源装
置の概略構成図である。FIG. 1 is a schematic diagram of an absorption heat source device according to an embodiment of the present invention.
1 蒸発器
2 蒸発兼吸収器3
吸収器
4 再生器
5 再生兼凝縮器6
凝縮器
11〜13 伝熱管
15,16 伝熱管
21 連通管
22〜27 冷媒移送管
31〜34 濃吸収液移送管
36,37 吸収液移送管
41〜49 開閉弁
51〜53 開閉弁
61〜63 バイパス管1 Evaporator 2 Evaporator and absorber 3
Absorber 4 Regenerator 5 Regenerator and condenser 6
Condensers 11-13 Heat transfer tubes 15, 16 Heat transfer tubes 21 Communication tubes 22-27 Refrigerant transfer tubes 31-34 Concentrated absorption liquid transfer tubes 36, 37 Absorption liquid transfer tubes 41-49 On-off valves 51-53 On-off valves 61-63 Bypass tube
Claims (1)
吸収器と、吸収器と、再生器と、再生兼凝縮器と、凝縮
器と、この凝縮器内と上記再生兼凝縮器内とを連通させ
る連通管と、上記再生器で蒸発された冷媒を上記再生兼
凝縮器内の伝熱管内に移送する冷媒移送管と、上記再生
兼凝縮器内の伝熱管からの冷媒を上記凝縮器に移送する
冷媒移送管と、上記凝縮器からの冷媒を上記蒸発器内お
よび蒸発兼吸収器の伝熱管内に移送する冷媒移送管と、
上記再生器で分離された濃吸収液を上記吸収器内および
上記再生兼凝縮器内に移送する濃吸収液移送管と、上記
再生兼凝縮器からの濃吸収液を上記吸収器および上記蒸
発兼吸収器内に移送する濃吸収液移送管と、上記吸収器
で冷媒を吸収して希釈された稀吸収液を上記再生器に移
送する稀吸収液移送管と、上記蒸発兼吸収器で冷媒を吸
収して希釈された稀吸収液を上記再生兼凝縮器に移送す
る稀吸収液移送管と、熱交換流体を上記吸収器および上
記凝縮器内の各伝熱管内に移送する熱交換流体移送管と
から構成し、かつ暖房サイクル作動時には、上記再生器
と吸収器との間で吸収液を循環させるようになすととも
に、上記再生兼凝縮器と蒸発兼吸収器との間で吸収液を
循環させるようになし、また冷房サイクル作動時には、
上記蒸発器で蒸発された冷媒を上記吸収器に直接移送す
るとともに、再生器で分離された濃吸収液を上記再生兼
凝縮器を介して上記吸収器内に移送させるようにしたこ
とを特徴とする吸収式熱源装置。Claims 1: An evaporator to which a heat exchange fluid is supplied, an evaporator/absorber, an absorber, a regenerator, a regenerator/condenser, a condenser, and the inside of the condenser and the regenerator/condenser. a refrigerant transfer pipe that transfers the refrigerant evaporated in the regenerator to the heat transfer tube in the regenerator and condenser, and a refrigerant transfer tube that transfers the refrigerant from the heat transfer tube in the regenerator and condenser to the a refrigerant transfer pipe that transfers the refrigerant to the condenser; a refrigerant transfer pipe that transfers the refrigerant from the condenser into the evaporator and the heat transfer tube of the evaporator and absorber;
A concentrated absorption liquid transfer pipe for transferring the concentrated absorption liquid separated by the regenerator into the absorber and the regeneration/condenser, and a concentrated absorption liquid transfer pipe for transferring the concentrated absorption liquid from the regeneration/condenser to the absorber and the evaporation/condenser. A concentrated absorption liquid transfer pipe that transfers the refrigerant into the absorber, a dilute absorption liquid transfer pipe that transfers the diluted diluted absorption liquid by absorbing the refrigerant in the absorber to the regenerator, and a dilute absorption liquid transfer pipe that transfers the refrigerant to the regenerator. A dilute absorption liquid transfer tube for transferring the absorbed and diluted diluted absorption liquid to the regeneration/condenser, and a heat exchange fluid transfer tube for transferring the heat exchange fluid to each heat transfer tube in the absorber and the condenser. and when the heating cycle is activated, the absorption liquid is circulated between the regenerator and the absorber, and the absorption liquid is circulated between the regeneration/condenser and the evaporator/absorber. There is no such thing, and when the cooling cycle is activated,
The refrigerant evaporated by the evaporator is directly transferred to the absorber, and the concentrated absorption liquid separated by the regenerator is transferred to the absorber via the regenerator/condenser. absorption type heat source device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3026597A JP2543258B2 (en) | 1991-02-21 | 1991-02-21 | Absorption heat source device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3026597A JP2543258B2 (en) | 1991-02-21 | 1991-02-21 | Absorption heat source device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04268175A true JPH04268175A (en) | 1992-09-24 |
JP2543258B2 JP2543258B2 (en) | 1996-10-16 |
Family
ID=12197941
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3026597A Expired - Lifetime JP2543258B2 (en) | 1991-02-21 | 1991-02-21 | Absorption heat source device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2543258B2 (en) |
-
1991
- 1991-02-21 JP JP3026597A patent/JP2543258B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2543258B2 (en) | 1996-10-16 |
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