JPH0364787B2 - - Google Patents
Info
- Publication number
- JPH0364787B2 JPH0364787B2 JP56202750A JP20275081A JPH0364787B2 JP H0364787 B2 JPH0364787 B2 JP H0364787B2 JP 56202750 A JP56202750 A JP 56202750A JP 20275081 A JP20275081 A JP 20275081A JP H0364787 B2 JPH0364787 B2 JP H0364787B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat exchanger
- pump
- condenser
- heating
- 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
- 238000001816 cooling Methods 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 14
- 230000006835 compression Effects 0.000 claims description 11
- 238000007906 compression Methods 0.000 claims description 11
- 239000006096 absorbing agent Substances 0.000 claims description 10
- 238000010521 absorption reaction Methods 0.000 claims description 8
- 238000005338 heat storage Methods 0.000 claims description 4
- 239000003507 refrigerant Substances 0.000 description 18
- 239000007789 gas Substances 0.000 description 10
- 230000005855 radiation Effects 0.000 description 6
- 238000004378 air conditioning Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- IPLONMMJNGTUAI-UHFFFAOYSA-M lithium;bromide;hydrate Chemical compound [Li+].O.[Br-] IPLONMMJNGTUAI-UHFFFAOYSA-M 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Air Filters, Heat-Exchange Apparatuses, And Housings Of Air-Conditioning Units (AREA)
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は太陽熱や排熱等を熱源として作動する
吸収式サイクルに、圧縮式ヒートポンプサイクル
を組み合わせた冷暖房装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heating and cooling system that combines a compression heat pump cycle with an absorption cycle that operates using solar heat, waste heat, or the like as a heat source.
従来、太陽熱等を利用する冷暖房装置として、
臭化リチウム−水吸収冷凍機がよく知られている
が、これは太陽熱集熱器に水等の熱媒体を循環さ
せ顕熱として熱を取り出し、冷房期にはその熱を
吸収式冷凍機のガス発生器に供給し、この熱によ
り冷媒を蒸発させて冷房を行なう為、発生器の要
求する温度よりさらに10℃以上高い加熱温水が必
要となり、熱損失も増加するばかりでなく、温水
循環ポンプ等補助動力が余分に必要である。 Traditionally, air conditioning equipment that utilizes solar heat, etc.
Lithium bromide-water absorption refrigerators are well known, and they circulate a heat medium such as water through a solar collector to extract heat as sensible heat, and during the cooling season, this heat is transferred to an absorption refrigerator. This heat is supplied to the gas generator and used to evaporate the refrigerant for cooling, which requires heating hot water that is at least 10°C higher than the temperature required by the generator, which not only increases heat loss but also requires a hot water circulation pump. Additional auxiliary power is required.
この問題を解決する一方法として、冷媒として
フロン系冷媒を用い、直接太陽熱集熱を吸収式冷
凍機の発生器とするものがあるがそれだけでは不
十分なので、圧縮式ヒートポンプサイクルと組合
せ、暖房時には、集熱器で集めた熱を水等を介し
て圧縮式ヒートポンプで汲み上げ、加温して暖房
するものがある。 One way to solve this problem is to use a fluorocarbon-based refrigerant as the refrigerant and directly collect solar heat as a generator for an absorption refrigerator, but since this alone is not sufficient, it is combined with a compression heat pump cycle and used for heating. There are some systems that use a compression heat pump to pump up the heat collected in a heat collector through water, etc. to heat the room.
しかし、この方法では太陽日射等の熱源がない
時は暖房できないし、これを解決する為温水を蓄
熱するとすると、相当大きな蓄熱槽が必要となり
不経済である。 However, with this method, heating is not possible when there is no heat source such as solar radiation, and if hot water is stored as a solution to this problem, a considerably large heat storage tank is required, which is uneconomical.
本発明は冷房および暖房時のかかる欠点を改善
し、効率よく暖房さらには冷房を行なわせるよう
にしたものである。 The present invention improves these drawbacks during cooling and heating, and enables efficient heating and cooling.
以下、本発明の詳細について、その一実施例を
示す図面とともに説明する。 Hereinafter, details of the present invention will be explained with reference to drawings showing one embodiment thereof.
最初に、冷房時の動作について説明する。太陽
日射等熱源が十分ある時には溶液ポンプ3により
送られた冷媒を多量に溶かした濃溶液は、溶液熱
交換器2を通り、集熱器兼ガス発生器1に入り加
熱されて冷媒ガスを発生させ、液は稀溶液とな
る。発生した冷媒ガスは通路7を通るが、冷房時
には弁6を閉じる為、弁8を経て凝縮器9に入り
ここで放熱し液化する。凝縮器9で液化した冷媒
は膨張弁10で減圧され蒸発し易くなつて、熱交
換器11で吸熱し蒸発する。この時、室内空間等
を冷却する。蒸発した冷媒は、弁12を経て吸収
器13に入り、発生器1より溶液熱交換器2で濃
溶液と熱交換し絞り弁4を通つて吸収器13に戻
つてきた稀溶液に吸収され、濃溶液となつて再び
溶液ポンプ3で発生器1に送られ、前記サイクル
を繰り返す。又、太陽日射等、熱源が不十分で、
十分な冷房出力が得られない時は圧縮機24を運
転し、室内熱交換器23で冷房出力を補助する。
この場合、圧縮機24より吐出された冷媒は四方
弁28を経て、水冷式熱交換器20あるいは空冷
式熱交換器26で放熱凝縮されて膨張弁22で減
圧され、室内熱交換器23に入る。熱交換器23
に入つた冷媒は吸熱蒸発しこのとき室内空間を冷
却する。熱交換器23を出た冷媒は四方弁28を
経て圧縮機24に入り再び前記サイクルを繰り返
す。さらに太陽日射等、熱源が全く得られない時
には圧縮式冷凍サイクルでのみ冷房を行う。この
様に太陽熱などの熱源を有効に利用し、冷房負荷
にマツチした効率の良い冷房運転が出来る。 First, the operation during cooling will be explained. When there is a sufficient heat source such as solar radiation, a concentrated solution containing a large amount of refrigerant sent by the solution pump 3 passes through the solution heat exchanger 2 and enters the heat collector/gas generator 1 where it is heated and generates refrigerant gas. The solution becomes a dilute solution. The generated refrigerant gas passes through the passage 7, but since the valve 6 is closed during cooling, it enters the condenser 9 via the valve 8, where it radiates heat and becomes liquefied. The refrigerant liquefied in the condenser 9 is depressurized in the expansion valve 10 and becomes easily evaporated, and then absorbs heat in the heat exchanger 11 and evaporates. At this time, the indoor space etc. is cooled. The evaporated refrigerant enters the absorber 13 through the valve 12, exchanges heat with the concentrated solution from the generator 1 in the solution heat exchanger 2, and is absorbed by the dilute solution that returns to the absorber 13 through the throttle valve 4. The concentrated solution is sent again to the generator 1 by the solution pump 3, and the cycle is repeated. In addition, heat sources such as solar radiation are insufficient,
When sufficient cooling output cannot be obtained, the compressor 24 is operated and the indoor heat exchanger 23 assists the cooling output.
In this case, the refrigerant discharged from the compressor 24 passes through the four-way valve 28, is heat-radiated and condensed in the water-cooled heat exchanger 20 or the air-cooled heat exchanger 26, is depressurized in the expansion valve 22, and enters the indoor heat exchanger 23. . Heat exchanger 23
The refrigerant that enters the room absorbs heat and evaporates, cooling the indoor space. The refrigerant leaving the heat exchanger 23 enters the compressor 24 via the four-way valve 28 and repeats the cycle again. Furthermore, when no heat source is available, such as solar radiation, cooling is performed only with a compression refrigeration cycle. In this way, heat sources such as solar heat can be used effectively to provide efficient cooling operation that matches the cooling load.
次に暖房時の動作について説明する。太陽日射
等熱源が十分得られる時、濃溶液はポンプ3によ
り溶液熱交換器2を経て集熱発生器1に送られこ
こで冷媒ガスを発生して稀溶液となつて熱交換器
2を経て吸収器13に流入する。一方、発生器1
で発生した冷媒ガスは弁8及び弁12を閉じ弁6
を開くと、通路7及び弁6、通路5を通つて吸収
器13に入る。吸収器13にて冷媒ガスと稀溶液
は混合し溶液し濃溶液となるが、その際集熱発生
器1で冷媒ガスを発生させるのに要した熱量にほ
ぼ等しい熱量を放出する。この時、冷水入口14
より冷却水を流入すると、この水は吸収器13内
で加熱され、出口15より温水となつて流出す
る。ここで、前記圧縮式ヒートポンプサイクルの
水冷式熱交換器20に、出口15より得られた温
水をポンプ16で流入した圧縮機24を運転する
と、吸収器13より放出した熱は温水を介して、
ヒートポンプサイクルの冷媒蒸気に汲み上げられ
る。熱交換器20で吸熱した冷媒は、四方弁28
を経て圧縮機24に入り、ここで加圧加温されて
室内熱交換器23に至る。高温度の冷媒は、熱交
換器23で放熱凝縮して暖房を行なう。この場
合、圧縮式ヒートポンプサイクルの熱源として高
温の熱を利用できるので凝縮器と蒸発器の温度差
を小さく(つまり圧縮比を小さく)出来るので非
常に効率のよい暖房ができる。 Next, the operation during heating will be explained. When a sufficient heat source such as solar radiation is available, the concentrated solution is sent to the heat collector generator 1 via the solution heat exchanger 2 by the pump 3, where a refrigerant gas is generated and becomes a dilute solution, which passes through the heat exchanger 2. It flows into the absorber 13. On the other hand, generator 1
The refrigerant gas generated in
When opened, it enters the absorber 13 through passage 7 and valve 6, passage 5. In the absorber 13, the refrigerant gas and the dilute solution are mixed and dissolved to form a concentrated solution, and at this time, an amount of heat approximately equal to the amount of heat required to generate the refrigerant gas in the heat collecting generator 1 is released. At this time, cold water inlet 14
When more cooling water flows in, this water is heated in the absorber 13 and flows out from the outlet 15 as hot water. Here, when the compressor 24 in which the hot water obtained from the outlet 15 is flowed into the water-cooled heat exchanger 20 of the compression heat pump cycle by the pump 16 is operated, the heat released from the absorber 13 passes through the hot water.
It is pumped into the refrigerant vapor of the heat pump cycle. The refrigerant that has absorbed heat in the heat exchanger 20 is transferred to the four-way valve 28.
The heat enters the compressor 24, where it is pressurized and heated, and reaches the indoor heat exchanger 23. The high temperature refrigerant radiates heat and condenses in the heat exchanger 23 to perform heating. In this case, since high-temperature heat can be used as a heat source for the compression heat pump cycle, the temperature difference between the condenser and evaporator can be reduced (that is, the compression ratio can be reduced), resulting in extremely efficient heating.
又、太陽日射等熱源の得られない時は、吸収式
サイクル側を停止し、熱媒体配管17,18の先
に例えば設置されている蓄熱槽に温水がある場合
は熱交換器20より熱を汲み上げ、温水のない時
あるいは外気温が高く温水を利用するより得な時
は、室外空気熱交換器26で外気より熱を汲み上
げ前記と同様にして暖房を行なう。 In addition, when a heat source such as solar radiation is not available, the absorption type cycle side is stopped, and if there is hot water in a heat storage tank installed at the end of the heat medium pipes 17 and 18, heat is transferred from the heat exchanger 20. When hot water is not available, or when the outside temperature is high and it is more advantageous to use hot water, the outdoor air heat exchanger 26 pumps heat from the outside air and performs heating in the same manner as described above.
第2図は空冷式熱交換器26の代りにガスや石
油による燃焼熱交換器29を備えた例を示す。ま
た第3図は空冷式熱交換器26、燃焼熱交換器2
9の両方を備えた例である。なお、その他は第1
図と同一構成である。 FIG. 2 shows an example in which a gas or oil combustion heat exchanger 29 is provided instead of the air-cooled heat exchanger 26. Figure 3 also shows an air-cooled heat exchanger 26 and a combustion heat exchanger 2.
This is an example that includes both of the above. In addition, the other
It has the same configuration as the figure.
以上のように本発明は吸収式ヒートポンプサイ
クルに圧縮式ヒートポンプサイクルを組み合わせ
前記圧縮式ヒートポンプ側に少なくとも2個の暖
房時の蒸発器となる熱交換器を設けることによつ
て従来のように必要以上に大きな蓄熱槽を備える
必要はなく、又、温水温度や外気温によつて適正
な運転モードを選べ、省エネルギでかつ快適な空
調を行なうことが出来る。 As described above, the present invention combines an absorption heat pump cycle with a compression heat pump cycle, and by providing at least two heat exchangers that serve as evaporators during heating on the compression heat pump side, the present invention eliminates the need for conventional heat pumps. There is no need to equip the system with a large heat storage tank, and an appropriate operation mode can be selected depending on the hot water temperature and outside air temperature, allowing for energy-saving and comfortable air conditioning.
第1図は本発明の実施例を示す冷暖房装置の構
成図、第2図および第3図は本発明の異なる実施
例の一部構成図である。
1……集熱発生器、3……溶液ポンプ、11…
…室内熱交換器、13……吸収器、16……水ポ
ンプ、20……水冷熱交換器、23……室内熱交
換器、24……圧縮機、26……空気熱交換器、
29……ガス(石油)熱交換器。
FIG. 1 is a block diagram of a heating and cooling system showing an embodiment of the present invention, and FIGS. 2 and 3 are partial block diagrams of different embodiments of the present invention. 1... Heat collection generator, 3... Solution pump, 11...
... Indoor heat exchanger, 13 ... Absorber, 16 ... Water pump, 20 ... Water-cooled heat exchanger, 23 ... Indoor heat exchanger, 24 ... Compressor, 26 ... Air heat exchanger,
29...Gas (oil) heat exchanger.
Claims (1)
器及びポンプを構成要素とし、前記凝縮器と前記
蒸発器の直列回路をバイパス制御する通路を設け
た吸収式ヒートポンプサイクルと、少なくとも圧
縮機、四方弁、凝縮器、熱交換器、膨張弁及び蒸
発器を構成要素とする圧縮式ヒートポンプサイク
ルを具備し、前記吸収式ヒートポンプサイクルの
吸収器と前記圧縮式ヒートポンプサイクルの熱交
換器を水などの熱媒体配管で連結して組み合せ、
前記熱媒体配管中に蓄熱槽等に連なる熱媒体配管
を設け、前記熱媒体配管中に前記熱媒体の移動を
制御するポンプを設けたことを特徴とする冷暖房
装置。 2 凝縮器に熱交換器を並列接続したことを特徴
とする特許請求請求の範囲第1項記載の冷暖房装
置。[Claims] 1. An absorption heat pump cycle comprising at least a generator, a condenser, an evaporator, an absorber, and a pump, and a passage for bypass-controlling a series circuit of the condenser and the evaporator. , comprising a compression heat pump cycle having at least a compressor, a four-way valve, a condenser, a heat exchanger, an expansion valve, and an evaporator as components, and heat exchange between the absorber of the absorption heat pump cycle and the compression heat pump cycle. The devices are connected and combined using heat medium piping such as water,
A heating and cooling device characterized in that a heat medium pipe connected to a heat storage tank or the like is provided in the heat medium pipe, and a pump for controlling movement of the heat medium is provided in the heat medium pipe. 2. The heating and cooling device according to claim 1, characterized in that a heat exchanger is connected in parallel to the condenser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20275081A JPS58104474A (en) | 1981-12-15 | 1981-12-15 | Air conditioner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20275081A JPS58104474A (en) | 1981-12-15 | 1981-12-15 | Air conditioner |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58104474A JPS58104474A (en) | 1983-06-21 |
JPH0364787B2 true JPH0364787B2 (en) | 1991-10-08 |
Family
ID=16462538
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20275081A Granted JPS58104474A (en) | 1981-12-15 | 1981-12-15 | Air conditioner |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58104474A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5118137A (en) * | 1974-08-06 | 1976-02-13 | Kajima Corp | |
JPS5563364A (en) * | 1978-11-08 | 1980-05-13 | Kogyo Gijutsuin | High temperature heat pump system |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56155224U (en) * | 1980-04-18 | 1981-11-19 |
-
1981
- 1981-12-15 JP JP20275081A patent/JPS58104474A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5118137A (en) * | 1974-08-06 | 1976-02-13 | Kajima Corp | |
JPS5563364A (en) * | 1978-11-08 | 1980-05-13 | Kogyo Gijutsuin | High temperature heat pump system |
Also Published As
Publication number | Publication date |
---|---|
JPS58104474A (en) | 1983-06-21 |
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