JP2533932B2 - Air-cooled absorption type water heater - Google Patents
Air-cooled absorption type water heaterInfo
- Publication number
- JP2533932B2 JP2533932B2 JP1087048A JP8704889A JP2533932B2 JP 2533932 B2 JP2533932 B2 JP 2533932B2 JP 1087048 A JP1087048 A JP 1087048A JP 8704889 A JP8704889 A JP 8704889A JP 2533932 B2 JP2533932 B2 JP 2533932B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- heat
- container
- cooling
- 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 - Lifetime
Links
- 238000010521 absorption reaction Methods 0.000 title claims description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 25
- 238000001816 cooling Methods 0.000 claims description 133
- 239000003507 refrigerant Substances 0.000 claims description 96
- 238000010438 heat treatment Methods 0.000 claims description 80
- 239000006096 absorbing agent Substances 0.000 claims description 44
- 239000007921 spray Substances 0.000 claims description 38
- 239000007788 liquid Substances 0.000 claims description 9
- 238000007865 diluting Methods 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 2
- 241000271897 Viperidae Species 0.000 claims 1
- 239000000243 solution Substances 0.000 description 65
- 238000010586 diagram Methods 0.000 description 23
- 230000000694 effects Effects 0.000 description 6
- 239000000470 constituent Substances 0.000 description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Central Heating Systems (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、空冷吸収式冷温水機に係り、特に、夏の冷
房、冬の直接暖房、冬のヒートポンプ暖房の3つのサイ
クルに切替え使用するのに好適な管路切替弁を有する空
冷吸収式冷温水機に関するものである。Description: TECHNICAL FIELD The present invention relates to an air-cooled absorption type chiller-heater, and in particular, it is switched between three cycles of cooling in summer, direct heating in winter, and heat pump heating in winter. The present invention relates to an air-cooled absorption type cold / hot water machine having a pipeline switching valve suitable for.
[従来の技術] 従来の空冷吸収式冷温水機は、例えば、特開昭62−21
8771号公報に記載されているように、暖房時は、再生器
を往復する溶液管路を締め切り、かつ、凝縮器へ往く冷
媒蒸気系を締め切り、再生器からの加熱蒸気を温水器へ
流し、室内ユニットの熱媒体を加熱暖房するサイクルで
あった。[Prior Art] A conventional air-cooled absorption type chiller-heater is disclosed in, for example, Japanese Patent Laid-Open No. 62-21.
As described in 8771 publication, during heating, the solution pipe line that reciprocates the regenerator is shut off, and the refrigerant vapor system going to the condenser is shut off, and the heated steam from the regenerator is flown to the water heater, It was a cycle of heating and heating the heat medium of the indoor unit.
[発明が解決しようとする課題] 上記従来技術の空冷吸収式冷温水機における暖房は、
いわゆる直接暖房によるもので、温水器を設け、負荷側
である室内ユニット、例えば室内ファンコイルユニット
を循環する温水と熱交換させていたが、省エネルギーに
ついて十分配慮されていなかった。[Problems to be Solved by the Invention] Heating in the air-cooled absorption type chiller-heater of the above-mentioned conventional technology is
This is so-called direct heating, in which a water heater is provided and heat is exchanged with hot water circulating through the indoor unit on the load side, for example, an indoor fan coil unit, but energy saving has not been sufficiently taken into consideration.
仮に、ヒートポンプサイクルによる省エネルギー運転
を行うとすると、ヒートポンプでは外気が0℃以下のと
きの運転が不可能であり、直接暖房も欠くことができな
い。If energy-saving operation is performed by a heat pump cycle, the heat pump cannot operate when the outside air temperature is 0 ° C. or less, and direct heating is indispensable.
本発明は、上記従来技術における課題を解決するため
になされたもので、主たる構成要素を新たに追加するこ
となく、切替弁の操作によって、冷房、直接暖房、ヒー
トポンプ式暖房の3つのサイクルが切替えられ、これに
よって、冷房運転の安定化、ヒートポンプサイクルによ
る暖房運転の省エネ化、外気温0℃以下での直接暖房運
転の各運転が選択できる空冷吸収式冷温水機を提供する
ことを、その目的とするものである。The present invention has been made to solve the above-mentioned problems in the conventional art, and three cycles of cooling, direct heating, and heat pump heating are switched by operating a switching valve without newly adding a main component. Accordingly, it is an object of the present invention to provide an air-cooled absorption chiller-heater capable of stabilizing the cooling operation, saving energy in the heating operation by the heat pump cycle, and selecting the direct heating operation at an outside temperature of 0 ° C or less. It is what
[課題を解決するための手段] 上記目的を達成するために、本発明に係る空冷吸収式
冷温水機の基本となる構成は、稀溶液を加熱して濃縮し
冷媒蒸気を分離させる再生器と、この再生器で発生した
冷媒蒸気を液化させる空冷凝縮器と、その冷媒液を負荷
側の熱媒体と熱交換させて冷媒を蒸発させる蒸発器と、
この蒸発器で生じた冷媒蒸気を、前記再生器から送給さ
れた濃溶液に吸収させる空冷吸収器と、これら各機器を
作動的に接続する溶液配管系および冷媒配管系を備えて
なる空冷吸収式冷温水機において、負荷側へ熱媒体を供
給する熱媒体循環系に組み込み、冷房時に蒸発器として
機能する熱媒体熱交換器と、この熱媒体熱交換器に冷媒
導管を介して接続し、冷房時に空冷吸収器として機能す
る空冷容器と、負荷側から戻る熱媒体を循環させる熱媒
体容器と、前記熱媒体循環系に設け、前記熱媒体容器を
バイパスする管路および該バイパス管路の切替弁と、前
記空冷容器に接続し、冷媒スプレーポンプを具備した冷
媒スプレー配管と、前記熱媒体熱交換器と前記再生器と
を往復しうるように接続した溶液循環系と、冷房時に前
記空冷容器から溶液ポンプを経て前記再生器へ通じ、ヒ
ートポンプ式暖房時に前記熱媒体熱交換器から溶液ポン
プを経て前記再生器へ通じるように、前記空冷容器と溶
液ポンプとの間に設けた稀溶液配管系の切替弁と、冷房
時に前記再生器から溶液熱交換器を経て前記空冷容器へ
通じ、ヒートポンプ式暖房時に前記再生器から溶液熱交
換器を経て前記熱媒体熱交換器へ通じるように、前記空
冷容器の溶液スプレー部に通じる濃溶液配管系の前記空
冷容器へ入る直前のスプレー管に設けた濃溶液配管系の
切替弁とを備え、前記各切替弁の切替えによって、前記
熱媒体熱交換器を冷房時に蒸発器、ヒートポンプ式暖房
時に吸収器として、前記空冷容器を冷房時に空冷吸収
器、ヒートポンプ式暖房時に空冷蒸発器として、冷房時
の熱媒体容器をヒートポンプ式暖房時に凝縮器として、
それぞれ機能せしめるようにヒートポンプサイクルを構
成したものである。[Means for Solving the Problems] In order to achieve the above object, a basic configuration of an air-cooled absorption type chiller-heater according to the present invention is a regenerator that heats and concentrates a dilute solution to separate a refrigerant vapor. , An air-cooled condenser for liquefying the refrigerant vapor generated in this regenerator, and an evaporator for evaporating the refrigerant by exchanging heat between the refrigerant liquid and the heat medium on the load side,
An air-cooled absorber that includes a refrigerant vapor generated in this evaporator, which absorbs the concentrated solution sent from the regenerator, and a solution piping system and a refrigerant piping system that operatively connect these devices. In the hot and cold water heater, the heat medium circulation system that supplies the heat medium to the load side is incorporated, and the heat medium heat exchanger that functions as an evaporator during cooling is connected to this heat medium heat exchanger via a refrigerant conduit, An air-cooling container that functions as an air-cooling absorber during cooling, a heat medium container that circulates a heat medium that returns from the load side, a pipe line that is provided in the heat medium circulation system and that bypasses the heat medium container, and a switching of the bypass pipe line A valve, a refrigerant spray pipe connected to the air cooling container and equipped with a refrigerant spray pump, a solution circulation system connected to the heat medium heat exchanger and the regenerator in a reciprocating manner, and the air cooling container during cooling. Melt from Switching of the dilute solution piping system provided between the air-cooled container and the solution pump so as to communicate with the regenerator through the pump and communicate with the regenerator through the solution pump from the heat medium heat exchanger during heat pump type heating A valve, and leads from the regenerator through the solution heat exchanger to the air-cooled container during cooling, so as to communicate with the heat medium heat exchanger through the solution heat exchanger from the regenerator during heat pump type heating, With a switching valve of the concentrated solution piping system provided in the spray pipe immediately before entering the air-cooled container of the concentrated solution piping system leading to the solution spray unit, by switching the switching valves, the heat medium heat exchanger is cooled. Evaporator, as an absorber during heat pump heating, the air-cooled container as an air-cooling absorber during cooling, as an air-cooling evaporator during heat pump heating, and as a heat medium container during cooling during heat pump heating As a condenser,
The heat pump cycle is configured so that each can function.
加えて、上記記載のものにおいて、冷房時に再生器か
ら分離した蒸気を空冷凝縮器へ流す管路の途中に切替弁
を設け、その一方を、熱媒体容器に係るヒートポンプサ
イクルの凝縮器に通ずる管路に接続するとともに、暖房
時に、前記ヒートポンプサイクルの凝縮器から凝縮冷媒
液を再生器へ戻す管路と、冷房時に空冷吸収器でありヒ
ートポンプ式暖房時に空冷蒸発器として機能する容器に
戻す管路とを切替える切替弁を設け、また、冷房時の空
冷吸収器と再生器とを往復する溶液管路にそれぞれ締切
り弁を設け、前記ヒートポンプサイクルの凝縮器と再生
器とを結ぶ系にのみ冷媒を循環させて暖房するサイクル
を構成したものである。In addition, in the above description, a switching valve is provided in the middle of the pipeline for flowing the steam separated from the regenerator during cooling to the air-cooled condenser, and one of them is connected to the condenser of the heat pump cycle related to the heat medium container. A conduit for returning condensed condensed liquid from the condenser of the heat pump cycle to the regenerator during heating, and a conduit for returning to the container functioning as an air-cooling evaporator during heat-pump heating and an air-cooling absorber during cooling. A switching valve for switching between and is provided, and a shutoff valve is provided in each of the solution pipes that reciprocate between the air-cooled absorber and the regenerator during cooling, and the refrigerant is supplied only to the system connecting the condenser and the regenerator of the heat pump cycle. It is a cycle that circulates and heats.
[作用] 上記の基本的な構成における作用を、実施例で後述す
る第1図ないし第3図の符号を用いて説明する。[Operation] The operation of the above-described basic configuration will be described with reference to the reference numerals of FIGS. 1 to 3 described later in the embodiment.
第1図は、空冷吸収式冷温水器の冷房サイクルを示
す。FIG. 1 shows a cooling cycle of an air-cooled absorption type chiller / heater.
熱媒体熱交換器(冷房時の蒸発器)1で蒸発した冷媒
は、空冷容器(冷房時の空冷吸収器)2の吸収液に吸収
され、溶液ポンプ7によって溶液熱交換器5を経て再生
器4へ送られる。再生器4で加熱濃縮された溶液は、熱
交換器5を経て空冷容器(空冷吸収器)2へ戻る。The refrigerant evaporated in the heat medium heat exchanger (evaporator during cooling) 1 is absorbed by the absorbing liquid in the air-cooled container (air-cooled absorber during cooling) 2, and is regenerated by the solution pump 7 via the solution heat exchanger 5. Sent to 4. The solution heated and concentrated in the regenerator 4 returns to the air-cooled container (air-cooled absorber) 2 via the heat exchanger 5.
再生器4で加熱分離された冷媒は、空冷凝縮器3で冷
却され凝縮して蒸発器1へ戻る。再び冷媒は熱媒体循環
系の熱媒と熱交換して蒸発し、負荷側の室内ファンコイ
ルユニット6によって室内を冷房する。The refrigerant that has been heated and separated by the regenerator 4 is cooled and condensed by the air-cooled condenser 3 and returns to the evaporator 1. The refrigerant again exchanges heat with the heat medium in the heat medium circulation system to evaporate and cools the room by the indoor fan coil unit 6 on the load side.
第2図は、直接暖房のサイクルを示す。 FIG. 2 shows a direct heating cycle.
再生器4で加熱された冷媒蒸気は、切替弁12を介して
熱媒体容器(温水機)16へ送られ、ここで室内ファンコ
イルユニット6からの熱媒を加熱し、冷媒は凝縮して再
生器4へ戻る。このとき、溶液ポンプ7、冷媒スプレー
ポンプ8は停止し、溶液締切り弁13,14は全閉し、再生
器4と空冷凝縮器3,空冷容器(空冷吸収器)2,熱媒体熱
交換器(蒸発器)1とは遮断されている。The refrigerant vapor heated in the regenerator 4 is sent to the heat medium container (water heater) 16 via the switching valve 12, where the heat medium from the indoor fan coil unit 6 is heated, and the refrigerant is condensed and regenerated. Return to container 4. At this time, the solution pump 7 and the refrigerant spray pump 8 are stopped, the solution cutoff valves 13 and 14 are fully closed, and the regenerator 4, the air-cooled condenser 3, the air-cooled container (air-cooled absorber) 2, the heat medium heat exchanger ( It is cut off from the evaporator 1.
本発明では、このような冷房,暖房サイクルを構成す
る空冷吸収式冷温水機に、第3図のようなヒートポンプ
サイクルを構成するものである。In the present invention, a heat pump cycle as shown in FIG. 3 is configured in the air-cooling absorption type chiller-heater that constitutes such a cooling and heating cycle.
すなわち、切替弁10,11を切り替え、空冷容器(冷房
時の空冷吸収器)2を空冷蒸発器として利用し、熱媒体
熱交換器(冷房時の蒸発器)1を吸収器として利用す
る。また、第1図の空冷凝縮器3は切替弁12で閉鎖し、
熱媒体容器(冷房時の温水器)16をヒートポンプサイク
ルの凝縮器として利用する。ここで凝縮した冷媒は切替
弁15によって空冷容器(第3図の蒸発器)2に戻る。こ
のようにして熱媒体容器(凝縮器)16と熱媒体熱交換器
(吸収器)1によって加熱された熱媒は、室内ファンコ
イルユニット6によって室内を暖房する。That is, the switching valves 10 and 11 are switched, the air cooling container (air cooling absorber during cooling) 2 is used as an air cooling evaporator, and the heat medium heat exchanger (evaporator during cooling) 1 is used as an absorber. Further, the air-cooled condenser 3 of FIG. 1 is closed by the switching valve 12,
The heat medium container (water heater for cooling) 16 is used as a condenser of the heat pump cycle. The refrigerant condensed here is returned to the air-cooled container (evaporator in FIG. 3) 2 by the switching valve 15. The heat medium thus heated by the heat medium container (condenser) 16 and the heat medium heat exchanger (absorber) 1 heats the room by the indoor fan coil unit 6.
[実施例] 以下、本発明の各実施例を第1図ないし第12図を参照
して説明する。[Embodiment] Each embodiment of the present invention will be described below with reference to FIGS. 1 to 12.
まず、本発明の基本的な構成(第1の発明)をもつ実
施例を第1図ないし第3図を参照して説明する。First, an embodiment having a basic configuration (first invention) of the present invention will be described with reference to FIGS.
第1図は、本発明の一実施例に係る空冷吸収式冷温水
機の冷房サイクル系統図、第2図は、第1図の装置の直
接暖房サイクル系統図、第3図は、第1図の装置のヒー
トポンプサイクル系統図である。各図中、同等部は同一
符号で示す。また矢印は溶液または冷媒の流れの方向を
示し、切替弁の黒く塗りつぶした側は閉を示す。FIG. 1 is a cooling cycle system diagram of an air-cooled absorption type chiller-heater according to an embodiment of the present invention, FIG. 2 is a direct heating cycle system diagram of the apparatus of FIG. 1, and FIG. 3 is FIG. It is a heat pump cycle system diagram of the apparatus of. In each figure, the same parts are designated by the same reference numerals. The arrow indicates the direction of the flow of the solution or the refrigerant, and the black side of the switching valve indicates closed.
図において、1は熱媒体熱交換器で、冷房時に蒸発
器、ヒートポンプ式暖房時に吸収器として機能する。2
は空冷容器で、前記熱媒体熱交換器1と導管37を介して
接続し、冷房時に空冷吸収器、ヒートポンプ式暖房時に
空冷蒸発器として機能する。3は空冷凝縮器、4は再生
器、4aは、外部熱源に通じる加熱炉を示す。5は溶液熱
交換器、6は、負荷側である室内ユニットに係る室内フ
ァンコイルユニット、7は溶液ポンプ、8は、冷媒スプ
レー配管17に設けた冷媒スプレーポンプ、9は、熱媒体
循環系に設けた冷温水ポンプである。In the figure, reference numeral 1 is a heat medium heat exchanger, which functions as an evaporator during cooling and as an absorber during heat pump heating. Two
Is an air-cooled container, which is connected to the heat medium heat exchanger 1 through a conduit 37 and functions as an air-cooled absorber during cooling and as an air-cooled evaporator during heat pump heating. 3 is an air-cooled condenser, 4 is a regenerator, and 4a is a heating furnace communicating with an external heat source. 5 is a solution heat exchanger, 6 is an indoor fan coil unit related to the indoor unit on the load side, 7 is a solution pump, 8 is a refrigerant spray pump provided in the refrigerant spray pipe 17, and 9 is a heat medium circulation system. It is a cold / hot water pump provided.
10は濃溶液配管系の切替弁で、この切替弁10は、再生
器4から熱交換器5を経て空冷容器(空冷吸収器)2の
溶液スプレー部へ通じる濃溶液配管18Bの、前記空冷容
器(空冷吸収器)2へ入る直前のスプレー管18Cに設け
られている。その切替弁10の他方は熱媒体熱交換器(蒸
発器)1へ通じる管路19Bに接続している。Reference numeral 10 is a switching valve of the concentrated solution piping system. The switching valve 10 is the air cooling container of the concentrated solution piping 18B leading from the regenerator 4 to the solution spray section of the air cooling container (air cooling absorber) 2 through the heat exchanger 5. (Air-cooled absorber) It is installed in the spray pipe 18C immediately before entering the (2). The other side of the switching valve 10 is connected to a pipe line 19B leading to the heat medium heat exchanger (evaporator) 1.
11は稀溶液配管系の切替弁で、この切替弁11は、空冷
容器(空冷吸収器)2から溶液ポンプ7を経て再生器4
へ通じる稀溶液配管18Aの前記空冷容器(空冷吸収器)
2と前記溶液ポンプ7との間に設けられている。その切
替弁11の他方は熱媒体熱交換器(蒸発器)1へ通じる管
路19Aに接続している。Reference numeral 11 is a switching valve of a dilute solution piping system, and this switching valve 11 is a regenerator 4 from an air cooling container (air cooling absorber) 2 via a solution pump 7.
The air-cooled container (air-cooled absorber) of the diluted solution pipe 18A leading to
2 and the solution pump 7. The other side of the switching valve 11 is connected to a pipe line 19A leading to the heat medium heat exchanger (evaporator) 1.
13は、再生器4から出る濃溶液配管18Bに設けた溶液
締切り弁、14は、再生器4へ入る稀溶液配管18Aに設け
た溶液締切り弁である。Reference numeral 13 is a solution cutoff valve provided in the concentrated solution pipe 18B coming out of the regenerator 4, and 14 is a solution cutoff valve provided in the dilute solution pipe 18A entering the regenerator 4.
また、12は切替弁で、この切替弁12は、再生器4で加
熱分離された蒸気を空冷凝縮器へ流す冷媒蒸気配管20に
設けられている。その切替弁12の他方は熱媒体容器(温
水器)16へ通じる冷媒蒸気配管21に接続している。Further, 12 is a switching valve, and this switching valve 12 is provided in a refrigerant vapor pipe 20 for flowing the vapor heated and separated in the regenerator 4 to the air-cooled condenser. The other of the switching valves 12 is connected to a refrigerant vapor pipe 21 leading to a heat medium container (water heater) 16.
さらに、15は切替弁で、この切替弁15は、熱媒体容器
16から再生器4へ通じる冷媒管路35と、熱媒体容器16か
ら空冷容器2へ通じる冷媒管路36とを切替えるものであ
る。Furthermore, 15 is a switching valve, and this switching valve 15 is a heat medium container.
The refrigerant pipe 35 communicating from 16 to the regenerator 4 and the refrigerant pipe 36 communicating from the heat medium container 16 to the air cooling container 2 are switched.
16は、熱媒体循環系の熱媒戻り管路24に設けられた熱
媒体容器で、冷房時に温水器、ヒートポンプ式暖房時に
凝縮器として機能する。Reference numeral 16 denotes a heat medium container provided in the heat medium return pipe 24 of the heat medium circulation system, which functions as a water heater during cooling and a condenser during heat pump heating.
22は切替弁で、この切替弁22は熱媒体循環系の熱媒戻
り管路24に設けられ、その他方は熱媒バイパス管路25に
接続している。また、23は切替弁で、この切替弁23は熱
媒体循環系の熱媒体供給管路26に設けられ、その他方は
熱媒バイパス管路27に接続している。A switching valve 22 is provided in the heating medium return pipe 24 of the heating medium circulation system, and the other is connected to the heating medium bypass pipe 25. Further, 23 is a switching valve, and this switching valve 23 is provided in the heat medium supply pipe 26 of the heat medium circulation system, and the other is connected to the heat medium bypass pipe 27.
本実施例の空冷吸収式冷温水器の作用を説明する。 The operation of the air-cooled absorption type chiller-heater of this embodiment will be described.
ここで、吸収剤の溶液は臭化チリウム水溶液、冷媒は
水、熱媒体循環系の熱媒は水である。Here, the solution of the absorbent is a thylium bromide aqueous solution, the refrigerant is water, and the heat medium of the heat medium circulation system is water.
第1図に示す夏季の冷房時には、切替弁10は管路19B
側、切替弁11は管路19A側をそれぞれ閉じ、切替弁12は
冷媒蒸気配管21側を閉じている。また、溶液締切り弁1
3,14は全開、さらに、切替弁15は冷媒管路35,36側を閉
じている。熱媒体循環系では、切替弁22,23は熱媒バイ
パス管路25,27側を開いている。溶液ポンプ7は運転
し、冷媒スプレーポンプ8は停止する。At the time of cooling in the summer shown in FIG. 1, the switching valve 10 is provided with the conduit 19B.
Side, the switching valve 11 closes the pipeline 19A side, and the switching valve 12 closes the refrigerant vapor pipe 21 side. Also, the solution shutoff valve 1
3, 14 are fully opened, and the switching valve 15 is closed on the refrigerant pipe lines 35, 36 side. In the heat medium circulation system, the switching valves 22 and 23 open the heat medium bypass pipe lines 25 and 27 side. The solution pump 7 operates and the refrigerant spray pump 8 stops.
第1図の冷房サイクルでは、熱媒体熱交換器(蒸発
器)1で蒸発した冷媒は、導管37を経て空冷容器(空冷
吸収器)2に送られ、スプレー管18Cによって撤布され
る溶液(吸収液)に吸収され、その稀溶液は溶液ポンプ
7により稀溶液配管18A、溶液熱交換器5を経て再生器
4へ送られる。再生器4で加熱濃縮された溶液は、濃溶
液配管18B、溶液熱交換器5を経て、スプレー管18Cから
空冷容器(空冷吸収器)2へ戻る。In the cooling cycle of FIG. 1, the refrigerant evaporated in the heat medium heat exchanger (evaporator) 1 is sent to the air-cooled container (air-cooled absorber) 2 via the conduit 37 and is removed by the spray pipe 18C ( The absorbing solution) absorbs the diluted solution, and the diluted solution is sent to the regenerator 4 by the solution pump 7 via the diluted solution pipe 18A and the solution heat exchanger 5. The solution heated and concentrated in the regenerator 4 returns to the air-cooled container (air-cooled absorber) 2 from the spray pipe 18C via the concentrated solution pipe 18B and the solution heat exchanger 5.
一方、再生器4で加熱分離された冷媒は、冷媒蒸気配
管20を経て空冷凝縮器3へ入り、ここで空冷されて凝縮
し、凝縮液は管路28を経て熱媒体熱交換器(蒸発器)1
へ戻る。ここで冷媒は熱媒体循環系の熱媒と熱交換して
再び蒸発する。On the other hand, the refrigerant that has been heated and separated in the regenerator 4 enters the air-cooled condenser 3 through the refrigerant vapor pipe 20, is air-cooled and condensed there, and the condensate passes through the pipe line 28 and the heat medium heat exchanger (evaporator). ) 1
Return to. Here, the refrigerant exchanges heat with the heat medium in the heat medium circulation system and evaporates again.
熱媒(水)は熱媒バイパス管路25から熱媒体熱交換器
(蒸発器)1へ入り、前記冷媒によりフラッシュ冷却さ
れ、熱媒バイパス管路27を経て熱媒供給管路26により室
内ファンコイルユニット6に送られ室内を冷房する。The heat medium (water) enters the heat medium heat exchanger (evaporator) 1 from the heat medium bypass pipe 25, is flash-cooled by the refrigerant, and passes through the heat medium bypass pipe 27 and the heat medium supply pipe 26 to produce an indoor fan. It is sent to the coil unit 6 to cool the room.
次に、第2図に示す冬季の直接暖房時には、切替弁1
0,11は全開、切替弁12は空冷凝縮器3側を閉じ、溶液締
切弁13,14は全閉、切替弁15は冷媒管路36側を閉じてい
る。熱媒体循環系では、切替弁22,23は熱媒バイパス管
路25,27側を閉じている。Next, during direct heating in winter as shown in Fig. 2, the switching valve 1
0 and 11 are fully opened, the switching valve 12 is closed on the air-cooled condenser 3 side, the solution shutoff valves 13 and 14 are fully closed, and the switching valve 15 is closed on the refrigerant pipe line 36 side. In the heat medium circulation system, the switching valves 22 and 23 close the heat medium bypass pipe lines 25 and 27.
溶液ポンプ7、冷媒スプレーポンプ8は停止し、前記
のように溶液締切り弁13,14が全閉しているので、再生
器4と空冷凝縮器3,空冷容器(空冷吸収器)2,熱媒体熱
交換器(蒸発器)1とは遮断されている。Since the solution pump 7 and the refrigerant spray pump 8 are stopped and the solution shutoff valves 13 and 14 are fully closed as described above, the regenerator 4, the air-cooled condenser 3, the air-cooled container (air-cooled absorber) 2, the heat medium It is cut off from the heat exchanger (evaporator) 1.
再生器4で加熱された冷媒蒸気は、切替弁12を介して
冷媒蒸気配管21を経て熱媒体容器(温水器)16へ送られ
る。ここで、冷媒蒸気は、室内ファンコイルユニット6
から熱媒戻り管路24を経て戻ってきた熱媒(水)を加熱
し、冷媒みずからは凝縮して冷媒管路35を経て再生器4
へ戻る。一方、加熱された熱媒は熱媒供給管路26を経て
室内ファンコイルユニット6に送られ室内を暖房する。The refrigerant vapor heated by the regenerator 4 is sent to the heat medium container (water heater) 16 via the switching valve 12 and the refrigerant vapor pipe 21. Here, the refrigerant vapor is the indoor fan coil unit 6
The heat medium (water) that has returned from the heat exchanger via the heat medium return pipe 24 is heated, and condensed from the refrigerant itself through the refrigerant pipe 35 to regenerator 4.
Return to. On the other hand, the heated heat medium is sent to the indoor fan coil unit 6 via the heat medium supply pipe line 26 to heat the room.
次に、第3図に示すヒートポンプ式暖房時には、切替
弁10,11は空冷容器2側を閉じ、切替弁12は空冷凝縮器
3側を閉じ、溶液締切り弁13,14は全閉、また切替弁15
は冷媒管路35側を閉じる。熱媒体循環系では、切替弁2
2,23は熱媒バイパス管路25,27側を閉じている。溶液ポ
ンプ7および冷媒スプレーポンプ8は運転する。Next, at the time of heat pump heating shown in FIG. 3, the switching valves 10 and 11 close the air cooling container 2 side, the switching valve 12 closes the air cooling condenser 3 side, the solution shutoff valves 13 and 14 are fully closed, and switching is performed again. Valve 15
Closes the refrigerant line 35 side. In the heat medium circulation system, switching valve 2
2 and 23 close the heat medium bypass pipe lines 25 and 27. The solution pump 7 and the refrigerant spray pump 8 are operated.
第3図に示すヒートポンプ式暖房時には、空冷容器
(冷房時の空冷吸収器)2を空冷蒸発器として機能さ
せ、熱媒体熱交換器(冷房時の蒸発器)1を吸収器とし
て機能させる。冷房時の空冷凝縮器3は切替弁12で閉鎖
し、熱媒体容器(冷房時の温水器)16をヒートポンプサ
イクルの凝縮器として機能させる。At the time of heat pump type heating shown in FIG. 3, the air cooling container (air cooling absorber during cooling) 2 functions as an air cooling evaporator, and the heat medium heat exchanger (evaporator during cooling) 1 functions as an absorber. The air-cooled condenser 3 during cooling is closed by a switching valve 12, and the heat medium container (water heater during cooling) 16 functions as a condenser of the heat pump cycle.
空冷容器(空冷蒸発器)2で蒸発した冷媒は、導管37
を経て熱媒体熱交換器(吸収器)1に送られ管路19Bに
よって供給され撤布される溶液に吸収され、その稀溶液
は管路19Aから切替弁11、溶液ポンプ7により稀溶液配
管18A、溶液熱交換器5を経て再生器4へ送られる。再
生器4で加熱濃縮された溶液は、濃溶液配管18B、溶液
熱交換器5を経て、切替弁10を介して管路19Bによって
熱媒体熱交換器(吸収器)1へ戻る。The refrigerant evaporated in the air-cooled container (air-cooled evaporator) 2 is supplied to the conduit 37.
Is transferred to the heat medium heat exchanger (absorber) 1 and is absorbed by the solution supplied and removed by the conduit 19B, and the diluted solution is transferred from the conduit 19A to the diluting solution pipe 18A by the switching valve 11 and the solution pump 7. , Via the solution heat exchanger 5 to the regenerator 4. The solution heated and concentrated in the regenerator 4 returns to the heat medium heat exchanger (absorber) 1 via the concentrated solution pipe 18B and the solution heat exchanger 5 and the conduit 19B via the switching valve 10.
一方、再生器4で加熱分離された冷媒は、切替弁12を
介して冷媒蒸気配管21を経て熱媒体容器(凝縮器)16へ
入り、ここで熱媒戻り管路24を経て戻ってきた熱媒を加
熱し、冷媒みずからは凝縮液化し、冷媒管路36によって
空冷容器(空冷蒸発器)2へ戻る。On the other hand, the refrigerant that has been heated and separated by the regenerator 4 enters the heat medium container (condenser) 16 through the switching valve 12 and the refrigerant vapor pipe 21, and returns to the heat medium return pipe 24 where the heat returned. The medium is heated, condensed and liquefied from the refrigerant itself, and returned to the air-cooled container (air-cooled evaporator) 2 through the refrigerant pipe 36.
熱媒体循環系の熱媒(水)は、熱媒体容器(凝縮器)
16において冷媒蒸気で加熱され、熱媒体熱交換器(吸収
器)1において吸収溶液で加熱され、熱媒供給管路26を
経て室内ファンコイルユニット6に送られ室内を暖房す
る。The heat medium (water) in the heat medium circulation system is the heat medium container (condenser).
It is heated by the refrigerant vapor in 16 and is heated by the absorbing solution in the heat medium heat exchanger (absorber) 1 and is sent to the indoor fan coil unit 6 via the heat medium supply pipeline 26 to heat the room.
このサイクルにおいては、空冷容器(空冷蒸発器)2
の冷媒を再循環させるため、冷媒スプレー配管17の冷媒
スプレーポンプ8を運転する。In this cycle, the air-cooled container (air-cooled evaporator) 2
In order to recirculate the above refrigerant, the refrigerant spray pump 8 of the refrigerant spray pipe 17 is operated.
本実施例によれば、空冷吸収式冷凍機において、主た
る構成要素を新たに追加することなく、切替弁の操作に
よって、冷房,直接暖房,ヒートポンプ式暖房の3つの
サイクルが切替えられる。これによって、空冷吸収式冷
凍機、ヒートポンプサイクルの省エネ化、直接暖房時の
外気温0℃以下での運転が、選択運転できる。According to this embodiment, in the air-cooled absorption refrigerator, three cycles of cooling, direct heating, and heat pump heating can be switched by operating the switching valve without newly adding main constituent elements. As a result, it is possible to selectively operate the air-cooled absorption type refrigerator and the heat pump cycle for energy saving and the operation at the outside air temperature of 0 ° C. or less during direct heating.
次に、本発明の他の実施例(第2の発明)を第4図な
いし第6図を参照して説明する。Next, another embodiment (second invention) of the present invention will be described with reference to FIGS. 4 to 6.
第4図は、本発明の他の実施例に係る空冷吸収式冷温
水機の冷房サイクル系統図、第5図は、第4図の装置の
直接暖房サイクル系統図、第6図は、第4図の装置のヒ
ートポンプサイクル系統図である。第4,5,6図中、先の
第1,2,3図と同一符号のものは同等部分であるから、そ
の説明を省略する。FIG. 4 is a cooling cycle system diagram of an air-cooling absorption type chiller / heater according to another embodiment of the present invention, FIG. 5 is a direct heating cycle system diagram of the apparatus of FIG. 4, and FIG. It is a heat pump cycle system diagram of the apparatus of the figure. In FIGS. 4, 5 and 6, the same reference numerals as those in FIGS. 1, 2 and 3 above are the same parts, and thus the description thereof will be omitted.
第4,5,6図の実施例が、先の第1,2,3図の実施例と相違
するところは、第4図の冷房時において、熱媒体熱交換
器(蒸発器)1をシェルアンドチューブ方式とし、管内
外で熱交換させて、蒸発潜熱によって熱媒戻り管路24の
熱媒を冷却することである。したがって、先の第2図の
実施例の直接暖房や第3図の実施例のヒートポンプ式暖
房のサイクルにおける熱媒体循環系における切替弁22,2
3は、第5図の実施例の直接暖房や第6図の実施例のヒ
ートポンプ式暖房のサイクルでは不要となる。The embodiment shown in FIGS. 4, 5 and 6 is different from the embodiment shown in FIGS. 1, 2 and 3 above when the heat medium heat exchanger (evaporator) 1 is used as a shell during cooling in FIG. This is an AND-tube system, in which heat is exchanged inside and outside the tube, and the heat medium in the heat medium return pipe 24 is cooled by latent heat of vaporization. Therefore, the switching valves 22 and 2 in the heat medium circulation system in the cycle of the direct heating of the embodiment shown in FIG. 2 and the heat pump type heating of the embodiment shown in FIG.
3 becomes unnecessary in the cycle of the direct heating of the embodiment shown in FIG. 5 and the heat pump type heating of the embodiment shown in FIG.
すなわち、第2の発明では、熱媒体循環系に切替弁、
熱媒バイパス管路を備えていないものである。熱媒体容
器(冷房時に温水器、ヒートポンプ式暖房時に凝縮器)
16および熱媒体熱交換器(冷房時に蒸発器、ヒートポン
プ式暖房時に吸収器)1Aは、いずれもシェルアンドチュ
ーブ式熱交換器が採用されている。That is, in the second invention, a switching valve is provided in the heat medium circulation system,
It does not have a heat medium bypass line. Heat medium container (water heater for cooling, condenser for heat pump heating)
The shell-and-tube heat exchanger is adopted for both 16 and the heat medium heat exchanger (evaporator during cooling, absorber during heat pump heating) 1A.
ここで、第4図に示す冷房時の負荷の小さい場合に
は、熱媒体熱交換器(蒸発器)1Aで蒸発しきれなかった
冷媒は空冷容器(空冷吸収器)2へ冷媒液として流れ再
循環する。Here, when the load during cooling shown in Fig. 4 is small, the refrigerant that could not be completely evaporated in the heat medium heat exchanger (evaporator) 1A flows to the air cooling container (air cooling absorber) 2 as a refrigerant liquid and is re-cooled. Circulate.
第4,5,6図の実施例によれば、先の実施例と同様の効
果が期待される。According to the embodiments of FIGS. 4, 5 and 6, the same effect as that of the previous embodiment is expected.
次に、本発明のさらに他の実施例(第2の発明の変形
例)を第7図ないし第9図を参照して説明する。Next, still another embodiment of the present invention (a modification of the second invention) will be described with reference to FIGS. 7 to 9.
第7図は、本発明のさらに他の実施例に係る空冷吸収
式冷温水機の冷房サイクル系統図、第8図は、第7図の
装置の直接暖房サイクル系統図、第9図は、第7図の装
置のヒートポンプサイクル系統図である。第7,8,9図
中、先の第1,2,3図あるいは第4,5,6図と同一符号のもの
は同等部分であるから、その説明を省略する。FIG. 7 is a cooling cycle system diagram of an air-cooling absorption type chiller-heater according to still another embodiment of the present invention, FIG. 8 is a direct heating cycle system diagram of the apparatus of FIG. 7, and FIG. It is a heat pump cycle system diagram of the apparatus of FIG. In FIGS. 7, 8, and 9, the same reference numerals as those in FIGS. 1, 2, and 3 or FIGS.
第7,8,9図の実施例が、第4,5,6図の実施例と相違する
ところは、熱媒体容器(冷房時に温水器、ヒートポンプ
式暖房時に凝縮器)16Aがシェルアンドチューブ式熱交
換器でないことである。The embodiment of FIGS. 7, 8 and 9 differs from the embodiment of FIGS. 4, 5 and 6 in that the heat medium container (water heater during cooling, condenser during heat pump heating) 16A is a shell and tube type. It is not a heat exchanger.
すなわち、第8図に示す直接暖房時の熱媒体容器(温
水器)16A、第9図に示すヒートポンプ式暖房時の熱媒
体容器(凝縮器)16Aでは、熱媒体循環系が熱媒戻り管
路24を流れる熱媒水(温水)によって、再生器4から切
替弁12、冷媒蒸気配管21を経て流入する冷媒蒸気が直接
冷却されて凝縮する。一方、熱媒は加熱されて熱媒供給
管路26から室内ファンコイルユニット6へ流れ室内を暖
房する。That is, in the heat medium container (water heater) 16A for direct heating shown in FIG. 8 and the heat medium container (condenser) 16A for heat pump type heating shown in FIG. 9, the heat medium circulation system is the heat medium return pipe line. The refrigerant vapor flowing from the regenerator 4 through the switching valve 12 and the refrigerant vapor pipe 21 is directly cooled and condensed by the heat transfer water (warm water) flowing in 24. On the other hand, the heat medium is heated and flows from the heat medium supply pipe line 26 to the indoor fan coil unit 6 to heat the inside of the room.
凝縮した冷媒液は、第8図の直接暖房では、切替弁1
5、冷媒管路35を経て再生器4へ戻り、第9図のヒート
ポンプ式暖房では、切替弁15、冷媒管路36を経て空冷容
器(空冷蒸発器)2へ戻る。In the direct heating shown in FIG.
5. Returning to the regenerator 4 via the refrigerant pipe 35, and in the heat pump heating of FIG. 9, returning to the air cooling container (air cooling evaporator) 2 via the switching valve 15 and the refrigerant pipe 36.
第7,8,9図の実施例によれば、先の各実施例と同様の
効果が期待されるほか、熱媒体容器(冷房時,直接暖房
時に温水器、ヒートポンプ式暖房時に凝縮器)16Aを簡
単な構造とするという本実施例特有の効果がある。According to the embodiments shown in FIGS. 7, 8 and 9, the same effects as those of the previous embodiments are expected, and the heat medium container (water heater during cooling and direct heating, condenser during heat pump heating) 16A There is an effect peculiar to the present embodiment that it has a simple structure.
次に、本発明のさらに他の実施例(第3の発明)を第
10図ないし第12図を参照して説明する。Next, another embodiment (third invention) of the present invention will be described.
This will be described with reference to FIGS. 10 to 12.
第10図は、本発明のさらに他の実施例に係る空冷吸収
式冷温水器の冷房サイクル系統図、第11図は、第10図の
装置の直接暖房サイクル系統図、第12図は、第10図の装
置のヒートポンプサイクル系統図である。第10,11,12図
中、先の第1,2,3図と同一符号のものは同等部分である
から、その説明を省略する。FIG. 10 is a cooling cycle system diagram of an air-cooled absorption type chiller / heater according to still another embodiment of the present invention, FIG. 11 is a direct heating cycle system diagram of the device of FIG. 10, and FIG. FIG. 10 is a heat pump cycle system diagram of the apparatus in FIG. In FIGS. 10, 11, and 12, the same reference numerals as those in FIGS. 1, 2, and 3 above denote the same parts, and thus the description thereof will be omitted.
第10,11,12図の実施例が、先の各実施例と相違すると
ころは、第10図に示す冷房時に蒸発器として機能する熱
媒体熱交換器(蒸発器)1のスプレー循環流路に係る管
路29,30と、第12図に示すヒートポンプ式暖房時に空冷
蒸発器として機能する空冷容器(冷房時の空冷吸収器)
2のスプレー循環流路に係る管路31,32とを切換えるた
めの切替弁33,34を設けたことである。The embodiment of FIGS. 10, 11 and 12 differs from the previous embodiments in that the spray circulation passage of the heat medium heat exchanger (evaporator) 1 functioning as an evaporator during cooling shown in FIG. 29, 30 related to and the air-cooling container (air-cooling absorber during cooling) that functions as an air-cooling evaporator during heat pump heating shown in FIG.
The changeover valves 33 and 34 for changing over to the pipe lines 31 and 32 related to the second spray circulation flow path are provided.
第10図に示す冷房時には、切替弁33,34は、空冷容器
2へ通じる管路31,32側を閉じている。これによって、
冷房時の負荷の少ないときでも、熱媒体熱交換器(蒸発
器)1で蒸発しきれなかった冷媒液は、冷媒スプレーポ
ンプ8によって管路29、切替弁33,34、管路30を経て再
循環スプレーされる。したがって、先の第7図の実施例
のように空冷吸収器へ冷媒液のまま送られて冷房効率を
落すことはない。At the time of cooling shown in FIG. 10, the switching valves 33 and 34 close the pipe lines 31 and 32 that communicate with the air-cooled container 2. by this,
Even when the load during cooling is small, the refrigerant liquid that could not be completely evaporated in the heat medium heat exchanger (evaporator) 1 is recycled by the refrigerant spray pump 8 via the pipe 29, the switching valves 33, 34, and the pipe 30. Circulating spray. Therefore, unlike the embodiment shown in FIG. 7, the cooling liquid is not sent to the air-cooled absorber as it is, and the cooling efficiency is not lowered.
第11図に示す直接暖房時には、切替弁33,34は全開で
あるが、先の第2図の実施例同様、溶液締切り弁13,14
が全閉、切替弁12の空冷凝縮器3側、切替弁15の空冷容
器2側が閉じており、再生器4と空冷凝縮器3,空冷容器
2,熱媒体熱交換器(蒸発器)1とは遮断されている。At the time of direct heating shown in FIG. 11, the switching valves 33, 34 are fully opened, but the solution shutoff valves 13, 14 are the same as in the previous embodiment of FIG.
Is fully closed, the air-cooling condenser 3 side of the switching valve 12 and the air-cooling container 2 side of the switching valve 15 are closed, and the regenerator 4, the air-cooling condenser 3, and the air-cooling container are closed.
2, It is cut off from the heat medium heat exchanger (evaporator) 1.
したがって、先の第2図の実施例と、同様の作用効果
が期待される。Therefore, the same effect as that of the embodiment shown in FIG. 2 is expected.
第12図に示すヒートポンプ式暖房時には、切替弁33,3
4は、管路29,30側を閉じており、切替弁10,11は空冷容
器2側を閉じている。During heat pump type heating shown in Fig. 12, switching valves 33, 3
Reference numeral 4 closes the pipelines 29 and 30 side, and switching valves 10 and 11 close the air cooling container 2 side.
したがって、先の第3図の実施例と同様、空冷容器
(空冷蒸発器)2の冷媒は、冷媒スプレーポンプ8によ
り、管路31、切替弁33、切替弁34、管路32によって再循
環される。Therefore, as in the previous embodiment of FIG. 3, the refrigerant in the air-cooled container (air-cooled evaporator) 2 is recirculated by the refrigerant spray pump 8 through the pipe 31, the switching valve 33, the switching valve 34, and the pipe 32. It
このように、第10,11,12図の各実施例によれば、先の
各実施例と同様の効果が期待される。Thus, according to each of the embodiments shown in FIGS. 10, 11, and 12, the same effect as that of each of the previous embodiments is expected.
[発明の効果] 以上述べたように、本発明によれば、主たる構成要素
を新たに追加することなく、切替弁の操作によって、冷
房、直接暖房、ヒートポンプ式暖房の3つのサイクルが
切替えられ、これによって、冷房運転の安定化、ヒート
ポンプサイクルによる暖房運転の省エネ化、外気温0℃
以下での直接暖房運転の各運転を選択しうる空冷吸収式
冷温水機を提供することができる。[Effects of the Invention] As described above, according to the present invention, three cycles of cooling, direct heating, and heat pump heating can be switched by operating the switching valve without newly adding main constituent elements. As a result, the cooling operation is stabilized, the heating operation is saved by the heat pump cycle, and the outside temperature is 0 ° C.
It is possible to provide an air-cooling absorption type chiller-heater capable of selecting each of the following direct heating operations.
第1図は、本発明の一実施例に係る空冷吸収式冷温水機
の冷房サイクル系統図、第2図は、第1図の装置の直接
暖房サイクル系統図、第3図は、第1図の装置のヒート
ポンプサイクル系統図、第4図は、本発明の他の実施例
に係る空冷吸収式冷温水機の冷房サイクル系統図、第5
図は、第4図の装置の直接暖房サイクル系統図、第6図
は、第4図の装置のヒートポンプサイクル系統図、第7
図は、本発明のさらに他の実施例に係る空冷吸収式冷温
水機の冷房サイクル系統図、第8図は、第7図の装置の
直接暖房サイクル系統図、第9図は、第7図の装置のヒ
ートポンプサイクル系統図、第10図は、本発明のさらに
他の実施例に係る空冷吸収式冷温水機の冷房サイクル系
統図、第11図は、第10図の装置の直接暖房サイクル系統
図、第12図は、第10図の装置のヒートポンプサイクル系
統図である。 1,1A……熱媒体熱交換器、2……空冷容器、3……空冷
凝縮器、4……再生器、5……溶液熱交換器、6……室
内ファンコイルユニット、7……溶液ポンプ、8……冷
媒スプレーポンプ、10,11,12,15……切替弁、13,14……
溶液締切り弁、16,16A……熱媒体容器、17……冷媒スプ
レー配管、18A……稀溶液配管、18B……濃溶液配管、18
C……スプレー管、19A,19B……管路、20,21……冷媒蒸
気配管、22,23……切替弁、24……熱媒戻り管路、26…
…熱媒供給管路、25,27……熱媒バイパス管路、29,30,3
1,32……管路、33,34……切替弁、35,36……冷媒管路、
37……導管。FIG. 1 is a cooling cycle system diagram of an air-cooled absorption type chiller-heater according to an embodiment of the present invention, FIG. 2 is a direct heating cycle system diagram of the apparatus of FIG. 1, and FIG. 3 is FIG. 5 is a heat pump cycle system diagram of the apparatus of FIG. 4, and FIG. 4 is a cooling cycle system diagram of an air-cooled absorption type chiller-heater according to another embodiment of the present invention.
FIG. 6 is a direct heating cycle system diagram of the apparatus of FIG. 4, FIG. 6 is a heat pump cycle system diagram of the apparatus of FIG. 4, and FIG.
FIG. 8 is a cooling cycle system diagram of an air-cooled absorption type chiller-heater according to still another embodiment of the present invention, FIG. 8 is a direct heating cycle system diagram of the apparatus of FIG. 7, and FIG. 9 is FIG. 10 is a heat pump cycle system diagram of the apparatus, FIG. 10 is a cooling cycle system diagram of an air-cooled absorption type chiller / heater according to still another embodiment of the present invention, FIG. 11 is a direct heating cycle system of the apparatus of FIG. FIG. 12 is a heat pump cycle system diagram of the apparatus of FIG. 1,1A: Heat medium heat exchanger, 2 ... Air-cooled container, 3 ... Air-cooled condenser, 4 ... Regenerator, 5 ... Solution heat exchanger, 6 ... Indoor fan coil unit, 7 ... Solution Pump, 8 …… Refrigerant spray pump, 10,11,12,15 …… Switching valve, 13,14 ……
Solution shut-off valve, 16, 16A ... Heat medium container, 17 ... Refrigerant spray piping, 18A ... Dilute solution piping, 18B ... Concentrated solution piping, 18
C ... Spray pipe, 19A, 19B ... Pipe line, 20,21 ... Refrigerant vapor pipe, 22,23 ... Switching valve, 24 ... Heat medium return pipe line, 26 ...
… Heat medium supply line, 25,27 …… Heat medium bypass line, 29,30,3
1,32 ... pipe, 33,34 ... switching valve, 35,36 ... refrigerant pipeline,
37 ... conduit.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 黒沢 茂吉 東京都豊島区要町2丁目26番地 (72)発明者 永岡 義一 東京都世田谷区上祖師谷5―22―4 上 祖師谷ハイツ302号 (72)発明者 閑納 真一 大阪府羽曳野市高鷲4丁目9―4―303 (72)発明者 竹本 貞寿 愛知県名古屋市千種区豊年町11―8 (72)発明者 吉井 俊朗 茨城県土浦市神立町603番地 株式会社 日立製作所土浦工場内 (72)発明者 清水 民男 茨城県土浦市神立町603番地 株式会社 日立製作所土浦工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shigeyoshi Kurosawa 2-26, Kanamemachi, Toshima-ku, Tokyo (72) Inventor Yoshikazu Nagaoka 5-22-4 Kamisoshiya, Setagaya-ku, Tokyo Kamisoshiya Heights 302 (72) Inventor Shinichi Kanno 4-9-4-303 Takawashi, Habikino-shi, Osaka (72) Inventor Sadaju Takemoto 11-8, Toyonencho, Chikusa-ku, Nagoya-shi, Aichi (72) Toshiro Yoshii, 603 Kandachi-cho, Tsuchiura-shi, Ibaraki Address, Hitachi Tsuchiura Plant, Ltd. (72) Inventor, Tamio Shimizu, 603, Kamidate-cho, Tsuchiura-shi, Ibaraki Hitachi Ltd., Tsuchiura Plant
Claims (6)
せる再生器と、この再生器で発生した冷媒蒸気を液化さ
せる空冷凝縮器と、その冷媒液を負荷側の熱媒体と熱交
換させて冷媒を蒸発させる蒸発器と、この蒸発器で生じ
た冷媒蒸気を、前記再生器から送給された濃溶液に吸収
させる空冷吸収器と、これら各機器を作動的に接続する
溶液配管系および冷媒配管系を備えてなる空冷吸収式冷
温水機において、 負荷側へ熱媒体を供給する熱媒体循環系に組み込み、冷
房時に蒸発器として機能する熱媒体熱交換器と、 この熱媒体熱交換器に冷媒導管を介して接続し、冷房時
に空冷吸収器として機能する空冷容器と、 負荷側から戻る熱媒体を循環させる熱媒体容器と、 前記熱媒体循環系に設け、前記熱媒体容器をバイパスす
る管路および該バイパス管路の切替弁と、 前記空冷容器に接続し、冷媒スプレーポンプを具備した
冷媒スプレー配管と、 前記熱媒体熱交換器と前記再生器とを往復しうるように
接続した溶液循環系と、 冷房時に前記空冷容器から溶液ポンプを経て前記再生器
へ通じ、ヒートポンプ式暖房時に前記熱媒体熱交換器か
ら溶液ポンプを経て前記再生器へ通じるように、前記空
冷容器と溶液ポンプとの間に設けた稀溶液配管系の切替
弁と、 冷房時に前記再生器から溶液熱交換器を経て前記空冷容
器へ通じ、ヒートポンプ式暖房時に前記再生器から溶液
熱交換器を経て前記熱媒体熱交換器へ通じるように、前
記空冷容器の溶液スプレー部に通じる濃溶液配管系の前
記空冷容器へ入る直前のスプレー管に設けた濃溶液配管
系の切替弁とを備え、 前記各切替弁の切替えによって、前記熱媒体熱交換器を
冷房時に蒸発器、ヒートポンプ式暖房時に吸収器とし
て、前記空冷容器を冷房時に空冷吸収器、ヒートポンプ
式暖房時に空冷蒸発器として、冷房時の熱媒体容器をヒ
ートポンプ式暖房時に凝縮器として、それぞれ機能せし
めるようにヒートポンプサイクルを構成したことを特徴
とする空冷吸収式冷温水機。1. A regenerator that heats and dilutes a dilute solution to separate refrigerant vapor, an air-cooled condenser that liquefies the refrigerant vapor generated in the regenerator, and heat exchange of the refrigerant liquid with a heat medium on the load side. An evaporator that evaporates the refrigerant, an air-cooled absorber that absorbs the refrigerant vapor generated in the evaporator into the concentrated solution sent from the regenerator, and a solution piping system that operatively connects these devices. In an air-cooled absorption chiller-heater equipped with a refrigerant piping system, a heat-medium heat exchanger that functions as an evaporator during cooling and is incorporated into the heat-medium circulation system that supplies the heat medium to the load side, and this heat-medium heat exchange Connected to the cooling system via a refrigerant conduit, an air cooling container that functions as an air cooling absorber during cooling, a heat medium container that circulates the heat medium that returns from the load side, and a heat medium circulation system that is provided and bypasses the heat medium container. Pipe and the viper A switching valve of a gas line, a refrigerant spray pipe that is connected to the air-cooled container and includes a refrigerant spray pump, and a solution circulation system that reciprocally connects the heat medium heat exchanger and the regenerator, Provided between the air-cooled container and the solution pump so as to communicate with the regenerator through the solution pump from the air-cooled container during cooling, and communicate with the regenerator through the solution pump from the heat medium heat exchanger during heat pump type heating. And a switching valve for the diluted solution piping system, which leads from the regenerator to the air-cooled container via the solution heat exchanger during cooling, and from the regenerator to the heat medium heat exchanger during heat pump heating As described above, a concentrated solution piping system switching valve provided in the spray pipe of the concentrated solution piping system leading to the solution spray section of the air-cooled container immediately before entering the air-cooled container is provided. The heat medium heat exchanger is an evaporator during cooling, an absorber during heat pump heating, the air cooling container is an air cooling absorber during cooling, an air cooling evaporator during heat pump heating, and the heat medium container during cooling is heat pump heating. An air-cooled absorption type chiller-heater characterized by having a heat pump cycle configured to function as a condenser at times.
せる再生器と、この再生器で発生した冷媒蒸気を液化さ
せる空冷凝縮器と、その冷媒液を負荷側の熱媒体と熱交
換させて冷媒を蒸発させる蒸発器と、この蒸発器で生じ
た冷媒蒸気を、前記再生器から送給された濃溶液に吸収
させる空冷吸収器と、これら各機器を作動的に接続する
溶液配管系および冷媒配管系を備えてなる空冷吸収式冷
温水機において、 負荷側へ熱媒体を供給する熱媒体循環系に組み込み、冷
房時に蒸発器として機能する熱媒体熱交換器と、 この熱媒体熱交換器に冷媒導管を介して接続し、冷房時
に空冷吸収器として機能する空冷容器と、 負荷側から戻る熱媒体を循環させる熱媒体容器と、 前記空冷容器に接続し、冷媒スプレーポンプを具備した
冷媒スプレー配管と、 前記熱媒体熱交換器と前記再生器とを往復しうるように
接続した溶液循環系と、 冷房時に前記空冷容器から溶液ポンプを経て前記再生器
へ通じ、ヒートポンプ式暖房時に前記熱媒体熱交換器か
ら溶液ポンプを経て前記再生器へ通じるように、前記空
冷容器と溶液ポンプとの間に設けた稀溶液配管系の切替
弁と、 冷房時に前記再生器から溶液熱交換器を経て前記空冷容
器へ通じ、ヒートポンプ式暖房時に前記再生器から溶液
熱交換器を経て前記熱媒体熱交換器へ通じるように、前
記空冷容器の溶液スプレー部に通じる濃溶液配管系の前
記空冷容器へ入る直前のスプレー管に設けた濃溶液配管
系の切替弁とを備え、 前記各切替弁の切替えによって、前記熱媒体熱交換器を
冷房時に蒸発器、ヒートポンプ式暖房時に吸収器とし
て、前記空冷容器を冷房時に空冷吸収器、ヒートポンプ
式暖房時に空冷蒸発器として、冷房時の熱媒体容器をヒ
ートポンプ式暖房時に凝縮器として、それぞれ機能せし
めるようにヒートポンプサイクルを構成したことを特徴
とする空冷吸収式冷温水機。2. A regenerator that heats and concentrates a dilute solution to separate refrigerant vapor, an air-cooled condenser that liquefies the refrigerant vapor generated in this regenerator, and heat exchange of the refrigerant liquid with a heat medium on the load side. An evaporator that evaporates the refrigerant, an air-cooled absorber that absorbs the refrigerant vapor generated in the evaporator into the concentrated solution sent from the regenerator, and a solution piping system that operatively connects these devices. In an air-cooled absorption chiller-heater equipped with a refrigerant piping system, a heat-medium heat exchanger that functions as an evaporator during cooling and is incorporated into the heat-medium circulation system that supplies the heat medium to the load side, and this heat-medium heat exchange Connected to the air conditioner via a refrigerant conduit, an air cooling container that functions as an air cooling absorber during cooling, a heat medium container that circulates a heat medium that returns from the load side, and a refrigerant that is connected to the air cooling container and that has a refrigerant spray pump. With spray piping, A solution circulation system in which the heat medium heat exchanger and the regenerator are connected so as to be able to reciprocate, and the air is passed from the air cooling container to the regenerator through the solution pump during cooling, and the heat medium heat exchanger during heat pump heating. From the regenerator through the solution heat pump to the regenerator via the solution pump, and a diluting solution pipe switching valve provided between the air-cooling container and the solution pump. The spray pipe immediately before entering the air-cooled container of the concentrated solution piping system that communicates with the solution spray section of the air-cooled container so that the regenerator passes through the solution heat exchanger and the heat-medium heat exchanger during heating. And a switching valve of a concentrated solution piping system provided in, by switching each switching valve, the heat medium heat exchanger is an evaporator during cooling, as an absorber during heat pump heating, the air-cooled container. An air-cooled absorption type cold / hot water characterized in that a heat pump cycle is configured to function as an air-cooled absorber during cooling, an air-cooled evaporator during heat pump heating, and a heat medium container during cooling as a condenser during heat pump heating. Machine.
せる再生器と、この再生器で発生した冷媒蒸気を液化さ
せる空冷凝縮器と、その冷媒液を負荷側の熱媒体と熱交
換させて冷媒を蒸発させる蒸発器と、この蒸発器で生じ
た冷媒蒸気を、前記再生器から送給された濃溶液に吸収
させる空冷吸収器と、これら各機器を作動的に接続する
溶液配管系および冷媒配管系を備えてなる空冷吸収式冷
温水機において、 負荷側へ熱媒体を供給する熱媒体循環系に組み込み、冷
房時に蒸発器として機能する熱媒体熱交換器と、 この熱媒体熱交換器に冷媒導管を介して接続し、冷房時
に空冷吸収器として機能する空冷容器と、 負荷側から戻る熱媒体を循環させる熱媒体容器と、 前記空冷容器に接続し、冷媒スプレーポンプを具備した
冷媒スプレー配管と、 前記熱媒体熱交換器と前記再生器とを往復しうるように
接続した溶液循環系と、 冷房時に前記空冷容器から溶液ポンプを経て前記再生器
へ通じ、ヒートポンプ式暖房時に前記熱媒体熱交換器か
ら溶液ポンプを経て前記再生器へ通じるように、前記空
冷容器と溶液ポンプとの間に設けた稀溶液配管系の切替
弁と、 冷房時に前記再生器から溶液熱交換器を経て前記空冷容
器へ通じ、ヒートポンプ式暖房時に前記再生器から溶液
熱交換器を経て前記熱媒体熱交換器へ通じるように、前
記空冷容器の溶液スプレー部に通じる濃溶液配管系の前
記空冷容器へ入る直前のスプレー管に設けた濃溶液配管
系の切替弁と、 前記熱媒体熱交換器に対するスプレー循環流路と、前記
空冷容器に対するスプレー循環流路とを切替える切替弁
とを備え、 前記各切替弁の切替えによって、前記熱媒体熱交換器を
冷房時に蒸発器、ヒートポンプ式暖房時に吸収器とし
て、前記空冷容器を冷房時に空冷吸収器、ヒートポンプ
式暖房時に空冷蒸発器として、冷房時の熱媒体容器をヒ
ートポンプ式暖房時に凝縮器として、それぞれ機能せし
めるようにヒートポンプサイクルを構成したことを特徴
とする空冷吸収式冷温水機。3. A regenerator that heats and dilutes a dilute solution to separate refrigerant vapor, an air-cooled condenser that liquefies the refrigerant vapor generated in this regenerator, and heat exchange of the refrigerant liquid with a heat medium on the load side. An evaporator that evaporates the refrigerant, an air-cooled absorber that absorbs the refrigerant vapor generated in the evaporator into the concentrated solution sent from the regenerator, and a solution piping system that operatively connects these devices. In an air-cooled absorption chiller-heater equipped with a refrigerant piping system, a heat-medium heat exchanger that functions as an evaporator during cooling and is incorporated into the heat-medium circulation system that supplies the heat medium to the load side, and this heat-medium heat exchange Connected to the air conditioner via a refrigerant conduit, an air cooling container that functions as an air cooling absorber during cooling, a heat medium container that circulates a heat medium that returns from the load side, and a refrigerant that is connected to the air cooling container and that has a refrigerant spray pump. With spray piping, A solution circulation system in which the heat medium heat exchanger and the regenerator are connected so as to be able to reciprocate, and the air is passed from the air cooling container to the regenerator through the solution pump during cooling, and the heat medium heat exchanger during heat pump heating. From the regenerator through the solution heat pump to the regenerator via the solution pump, and a diluting solution pipe switching valve provided between the air-cooling container and the solution pump. The spray pipe immediately before entering the air-cooled container of the concentrated solution piping system that communicates with the solution spray section of the air-cooled container so that the regenerator passes through the solution heat exchanger and the heat-medium heat exchanger during heating. A switching valve for the concentrated solution piping system provided in, a spray circulation channel for the heat medium heat exchanger, and a switching valve for switching the spray circulation channel for the air-cooled container, each switching By switching, the heat medium heat exchanger is an evaporator during cooling, as an absorber during heat pump heating, the air cooling container is an air cooling absorber during cooling, an air cooling evaporator during heat pump heating, and the heat medium container during cooling is Heat-pump type An air-cooled absorption type chiller-heater that has a heat pump cycle configured to function as a condenser during heating.
もののいずれかにおいて、 冷房時に再生器から分離した蒸気を空冷凝縮器へ流す管
路の途中に切替弁を設け、その一方を、熱媒体容器に係
るヒートポンプサイクルの凝縮器に通ずる管路に接続す
るとともに、 暖房時に、前記ヒートポンプサイクルの凝縮器から凝縮
冷媒液を再生器へ戻す管路と、冷房時に空冷吸収器であ
りヒートポンプ式暖房時に空冷蒸発器として機能する容
器に戻す管路とを切替える切替弁を設け、 また、冷房時の空冷吸収器と再生器とを往復する溶液管
路にそれぞれ締切り弁を設け、 前記ヒートポンプサイクルの凝縮器と再生器とを結ぶ系
にのみ冷媒を循環させて暖房するサイクルを構成するこ
とを特徴とする空冷吸収式冷温水機。4. A switching valve according to any one of claims 1 to 3, wherein a switching valve is provided in the middle of a pipeline for flowing the steam separated from the regenerator to the air-cooled condenser during cooling. , A pipe for returning the condensed refrigerant liquid from the condenser of the heat pump cycle to the regenerator at the time of heating, as well as being connected to the pipe leading to the condenser of the heat pump cycle related to the heat medium container, and an air cooling absorber at the time of cooling A switching valve that switches between a pipe returning to a container functioning as an air-cooling evaporator during heating is provided, and a shut-off valve is provided in each solution pipe that reciprocates between the air-cooling absorber and the regenerator during cooling, and the heat pump cycle An air-cooled absorption chiller-heater characterized by comprising a cycle in which a refrigerant is circulated only in a system connecting a condenser and a regenerator to heat the same.
もののいずれかにおいて、 冷房時に蒸発器として機能する熱媒体熱交換器と、負荷
側の室内ユニットから戻る熱媒体を循環させる熱媒体容
器とは、いずれもシエルアンドチューブ式熱交換器より
なることを特徴とする空冷吸収式冷温水機。5. The heat medium heat exchanger according to any one of claims 1 to 3, which functions as an evaporator during cooling, and heat for circulating a heat medium returned from an indoor unit on the load side. The medium container is an air-cooled absorption type chiller-heater characterized by comprising a shell-and-tube heat exchanger.
もののいずれかにおいて、負荷側の室内ユニツトから戻
る熱媒体を循環させる熱媒体容器を、ヒートポンプ式暖
房時に、切替弁を経て再生器から流入する冷媒蒸気が直
接冷却され凝縮する凝縮器として機能せしめることを特
徴とする空冷吸収式冷温水機。6. The heat medium container according to claim 1, wherein a heat medium container for circulating a heat medium returned from the indoor unit on the load side is circulated through a switching valve at the time of heating with a heat pump. An air-cooled absorption type chiller-heater characterized in that it functions as a condenser that directly cools and condenses the refrigerant vapor flowing from the reactor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1087048A JP2533932B2 (en) | 1989-04-07 | 1989-04-07 | Air-cooled absorption type water heater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1087048A JP2533932B2 (en) | 1989-04-07 | 1989-04-07 | Air-cooled absorption type water heater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02267477A JPH02267477A (en) | 1990-11-01 |
JP2533932B2 true JP2533932B2 (en) | 1996-09-11 |
Family
ID=13904056
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1087048A Expired - Lifetime JP2533932B2 (en) | 1989-04-07 | 1989-04-07 | Air-cooled absorption type water heater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2533932B2 (en) |
-
1989
- 1989-04-07 JP JP1087048A patent/JP2533932B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH02267477A (en) | 1990-11-01 |
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