JPH05215440A - Absorption type heat pump device - Google Patents
Absorption type heat pump deviceInfo
- Publication number
- JPH05215440A JPH05215440A JP359492A JP359492A JPH05215440A JP H05215440 A JPH05215440 A JP H05215440A JP 359492 A JP359492 A JP 359492A JP 359492 A JP359492 A JP 359492A JP H05215440 A JPH05215440 A JP H05215440A
- Authority
- JP
- Japan
- Prior art keywords
- heat pump
- absorber
- pump device
- condenser
- cooling water
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、熱を利用して冷熱を得
る吸収式ヒートポンプ装置で、冷却手段として水を用い
る吸収式ヒートポンプ装置の改良に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption heat pump device for obtaining cold heat by utilizing heat, and to an improvement of the absorption heat pump device using water as cooling means.
【0002】[0002]
【従来の技術】従来の吸収式ヒートポンプ装置の構成を
図5に示す。溶液ポンプ1により加圧された冷媒濃度の
高い濃溶液は、吸収器2で吸収熱を回収して昇温する。
さらに、溶液熱交換器3で発生器4から流出してくる冷
媒濃度の低い希溶液の顕熱を受けて昇温する。その後、
発生器4で外部より加熱される。吸収器2、溶液熱交換
器3、発生器4で昇温された濃溶液は、冷媒蒸気を発生
し、気液2相状態で精溜器5へ流入する。精溜器5は気
液を分離し、冷媒蒸気を凝縮器6へ、冷媒の少なくなっ
た希溶液を溶液熱交換器3へ流出させる。ここで、冷媒
蒸気には冷媒だけではなく溶媒の蒸気も含んでいること
から、精溜器5は、この溶媒蒸気を液化させ純度の高い
冷媒蒸気を凝縮器6に供給している。精溜の原理は温度
を下げ沸点の高い溶媒を液化させるもので、この時生ず
る熱は、精溜器5の上部から流入する分岐濃溶液に回収
される。精溜器5を出た希溶液はその顕熱を溶液熱交換
器3で濃溶液に与え降温し吸収器2へ戻る。一方、精溜
器5で生じた純度の高い冷媒蒸気は凝縮器6へ流出し、
外部へ熱を捨てて液化する。その後膨張弁7で減圧され
低温となって蒸発器8へ入り、外部より熱を受け蒸発
し、吸収器2へ戻る。吸収器2では溶液熱交換器3から
戻る希溶液に冷媒蒸気を吸収させ、その際生じる吸収熱
の一部を濃溶液に与え、残りは外部へ捨てる。2. Description of the Related Art The structure of a conventional absorption heat pump device is shown in FIG. The concentrated solution having a high refrigerant concentration, which is pressurized by the solution pump 1, recovers the absorbed heat in the absorber 2 and rises in temperature.
Further, the solution heat exchanger 3 receives the sensible heat of the dilute solution having a low refrigerant concentration flowing out from the generator 4, and raises the temperature. afterwards,
It is heated from the outside by the generator 4. The concentrated solution heated in the absorber 2, the solution heat exchanger 3, and the generator 4 generates a refrigerant vapor and flows into the rectifier 5 in a gas-liquid two-phase state. The rectifier 5 separates the gas and the liquid, and causes the refrigerant vapor to flow to the condenser 6 and the dilute solution with less refrigerant to flow to the solution heat exchanger 3. Here, since the refrigerant vapor contains not only the refrigerant but also the solvent vapor, the rectifier 5 liquefies the solvent vapor and supplies the refrigerant vapor with high purity to the condenser 6. The principle of rectification is to lower the temperature and liquefy the solvent having a high boiling point, and the heat generated at this time is recovered in the branched concentrated solution flowing from the upper part of the rectifier 5. The dilute solution discharged from the rectifier 5 gives its sensible heat to the concentrated solution by the solution heat exchanger 3 and is cooled to return to the absorber 2. On the other hand, the high-purity refrigerant vapor generated in the rectifier 5 flows out to the condenser 6,
It liquefies by discharging heat to the outside. After that, the pressure is reduced by the expansion valve 7 and the temperature becomes low to enter the evaporator 8, which receives heat from the outside to evaporate and returns to the absorber 2. In the absorber 2, the dilute solution returning from the solution heat exchanger 3 absorbs the refrigerant vapor, and part of the heat of absorption generated at that time is given to the concentrated solution, and the rest is discarded to the outside.
【0003】吸収式ヒートポンプで冷房または冷凍を行
う場合は、蒸発器8の冷熱を利用し、暖房または給湯に
利用する場合は、凝縮器6および吸収器2の排熱を利用
する。この時、冷却水は最初に吸収器と熱交換し、その
後凝縮器と熱交換するように流れている。When the absorption heat pump is used for cooling or freezing, the cold heat of the evaporator 8 is used, and when it is used for heating or hot water supply, the exhaust heat of the condenser 6 and the absorber 2 is used. At this time, the cooling water flows so as to exchange heat with the absorber first and then with the condenser.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、このよ
うな従来の吸収式ヒートポンプでは、吸収器を冷却した
後の比較的高温の冷却水で凝縮器を冷却するため、凝縮
圧力が大きくなり、能力および効率が低下する課題が生
じている。However, in such a conventional absorption heat pump, since the condenser is cooled by cooling water having a relatively high temperature after cooling the absorber, the condensing pressure becomes large and the capacity and There is a problem of reduced efficiency.
【0005】本発明は、上記課題にもとづき、能力が大
きく効率の高い吸収式ヒートポンプ装置を提供すること
を目的とする。An object of the present invention is to provide an absorption heat pump device having a large capacity and a high efficiency based on the above problems.
【0006】[0006]
【課題を解決するための手段】本発明は上記目的を達成
するために、吸収熱の一部と凝縮熱の一部または全部を
同一の冷却水と熱交換するように吸収器と凝縮器を一体
化するものである。SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides an absorber and a condenser so that a part of the absorption heat and a part or all of the condensation heat are exchanged with the same cooling water. It is a unity.
【0007】[0007]
【作用】上記のような構成もしくは手段によって、得ら
れる作用は次の通りである。The operation obtained by the above-mentioned structure or means is as follows.
【0008】吸収器と凝縮器を同時に最も低い温度の冷
却水と熱交換させることが可能であることから、吸収器
の温度を上げることなく、凝縮器の圧力を低減すること
ができ、能力および効率の向上が図れる。Since it is possible to heat-exchange the absorber and the condenser with the cooling water of the lowest temperature at the same time, the pressure of the condenser can be reduced without increasing the temperature of the absorber, and the capacity and The efficiency can be improved.
【0009】[0009]
【実施例】図1は本発明による一実施例であり、吸収式
ヒートポンプ装置の吸収器、凝縮器の断面を示すもので
ある。吸収器、凝縮器の一体化部は、積層式の熱交換器
よりなっており、吸収液流路11、冷却水流路12、凝
縮冷媒流路13、冷却水流路12の順に積層されてい
る。したがって、すべての冷却水流路12は、吸収液流
路11と凝縮冷媒流路13との間に位置することにな
る。図2は冷却水流路12の構成を示すものであり、一
方のヘッダー15から流入した冷却水は斜線部で示す流
路12に沿って熱交換器のほぼ全面を流れ、他方のヘッ
ダー15から流出する。流路12はエッチングにより形
成されている。斜線部ヘッダー16および17は、おの
おの吸収液および凝縮冷媒のヘッダーに対応している。
ヘッダー15は、吸収液のヘッダー16および凝縮冷媒
のヘッダー17と異なる位置としていることから、各流
体は混合することなく流れる。図3は吸収液流路11の
構成を示すものであり、一方のヘッダー16から流入し
た希溶液と冷媒蒸気の2相流は流路13に沿って熱交換
器のほぼ全面を流れ、他方のヘッダー16から流出す
る。凝縮冷媒流路13は、本実施例では吸収液流路11
の対象形で作成したものを使用している。このような流
路11から13を多数積層することにより、吸収器、凝
縮器の一体化が可能となる。各流体間の熱交換は、熱交
換器のほぼ全面で行われることから伝熱面積も大きく、
多量の熱をコンパクトに処理することが可能となる。実
際に使用した場合の結果では、吸収器温度を変えること
なく凝縮温度を5℃下げることができ、能力および効率
を10%以上に高めることができた。このときの冷却水
出口温度は従来例と同じであり、放熱器を変える必要も
なかった。なお、以上の説明では、エッチングにより流
路を形成した例について説明したが、プレス等により形
成された積層式熱交換器も同様な効果を得ることができ
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an embodiment of the present invention and shows a cross section of an absorber and a condenser of an absorption heat pump device. The integrated portion of the absorber and the condenser is composed of a laminated heat exchanger, and the absorption liquid channel 11, the cooling water channel 12, the condensed refrigerant channel 13, and the cooling water channel 12 are laminated in this order. Therefore, all the cooling water channels 12 are located between the absorbing liquid channel 11 and the condensed refrigerant channel 13. FIG. 2 shows the configuration of the cooling water flow passage 12, in which the cooling water flowing from one header 15 flows along the flow passage 12 indicated by the shaded portion over almost the entire surface of the heat exchanger and flows out from the other header 15. To do. The flow path 12 is formed by etching. The shaded headers 16 and 17 correspond to the headers of the absorbing liquid and the condensed refrigerant, respectively.
Since the header 15 is located at a position different from the header 16 of the absorbing liquid and the header 17 of the condensed refrigerant, the fluids flow without being mixed. FIG. 3 shows the structure of the absorbent liquid flow path 11. The two-phase flow of the dilute solution and the refrigerant vapor flowing from one header 16 flows along the flow path 13 over almost the entire surface of the heat exchanger, and the other It flows out of the header 16. The condensed refrigerant flow path 13 is the absorption liquid flow path 11 in this embodiment.
I used the one created in the target form. By stacking a large number of such flow paths 11 to 13, it becomes possible to integrate the absorber and the condenser. Since the heat exchange between the fluids is performed on almost the entire surface of the heat exchanger, the heat transfer area is large.
A large amount of heat can be processed compactly. As a result of actual use, the condensation temperature could be lowered by 5 ° C. without changing the absorber temperature, and the capacity and efficiency could be increased to 10% or more. The cooling water outlet temperature at this time was the same as that of the conventional example, and it was not necessary to change the radiator. In the above description, an example in which the flow path is formed by etching has been described, but a laminated heat exchanger formed by pressing or the like can also obtain similar effects.
【0010】以上のように本発明によって、能力および
効率が高い吸収式ヒートポンプ装置が提供される。As described above, the present invention provides an absorption heat pump device having high capacity and efficiency.
【0011】図4は本発明の他の実施例であり、吸収式
ヒートポンプ装置の吸収器、凝縮器の断面を示すもので
ある。吸収器、凝縮器の一体化部は、多重管の熱交換器
よりなっており、冷却水流路21の中に、吸収液流路2
2、凝縮冷媒流路23が位置している。したがって、冷
却水は、吸収液と凝縮冷媒双方と熱交換する。実際に使
用した場合の結果でも、実施例1で示した特性とほぼ同
等の値を確認している。FIG. 4 shows another embodiment of the present invention, showing a cross section of an absorber and a condenser of an absorption heat pump device. The integrated part of the absorber and the condenser is composed of a multi-tube heat exchanger, and the absorption liquid channel 2 is provided in the cooling water channel 21.
2. The condensed refrigerant flow path 23 is located. Therefore, the cooling water exchanges heat with both the absorbing liquid and the condensed refrigerant. Also in the result of actual use, it is confirmed that the value is almost equal to the characteristic shown in the first embodiment.
【0012】[0012]
【発明の効果】以上のように、本発明による吸収式ヒー
トポンプ装置は、吸収熱の一部と凝縮熱の一部または全
部を同一の冷却水と熱交換するように吸収器と凝縮器を
一体化することにより、能力および効率が高い吸収式ヒ
ートポンプ装置が可能となる。As described above, in the absorption heat pump device according to the present invention, the absorber and the condenser are integrated so that part of the absorbed heat and part or all of the condensed heat are exchanged with the same cooling water. As a result, an absorption heat pump device with high capacity and efficiency can be realized.
【図1】本発明の一実施例の吸収式ヒートポンプ装置の
吸収器、凝縮器の断面図FIG. 1 is a sectional view of an absorber and a condenser of an absorption heat pump device according to an embodiment of the present invention.
【図2】同冷却水流路の平面図FIG. 2 is a plan view of the cooling water channel.
【図3】同吸収液流路の平面図FIG. 3 is a plan view of the absorption liquid channel.
【図4】本発明の他の実施例の吸収式ヒートポンプ装置
の吸収器、凝縮器の断面図FIG. 4 is a sectional view of an absorber and a condenser of an absorption heat pump device according to another embodiment of the present invention.
【図5】従来の吸収式ヒートポンプ装置の構成図FIG. 5 is a configuration diagram of a conventional absorption heat pump device.
12,21 冷却水流路 11,22 吸収液流路 13,23 凝縮冷媒流路 12,21 Cooling water flow path 11,22 Absorbing liquid flow path 13,23 Condensing refrigerant flow path
Claims (3)
吸収式ヒートポンプにおいて、吸収熱を一部と凝縮熱の
一部または全部を同一の冷却水と熱交換するように吸収
器と凝縮器を一体化した吸収式ヒートポンプ装置。1. An absorption heat pump having an absorber, a generator, a condenser, and an evaporator, and an absorber so that part of the absorbed heat and part or all of the condensed heat are exchanged with the same cooling water. Absorption heat pump device with integrated condenser.
冷却水の順に流路を確保する積層式熱交換器で吸収器と
凝縮器の一体化を行う請求項1記載の吸収式ヒートポン
プ装置。2. An absorption liquid, a cooling water, a condensed refrigerant,
The absorption heat pump device according to claim 1, wherein the absorber and the condenser are integrated by a laminated heat exchanger that secures a flow path in the order of cooling water.
凝縮冷媒が流れる管を設置して吸収器と凝縮器の一体化
を行う請求項1記載の吸収式ヒートポンプ装置。3. The absorption heat pump device according to claim 1, wherein a pipe through which the absorbing liquid flows and a pipe through which the condensed refrigerant flows are installed in a pipe through which the cooling water flows to integrate the absorber and the condenser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP359492A JP2962020B2 (en) | 1992-01-13 | 1992-01-13 | Absorption type heat pump device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP359492A JP2962020B2 (en) | 1992-01-13 | 1992-01-13 | Absorption type heat pump device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05215440A true JPH05215440A (en) | 1993-08-24 |
JP2962020B2 JP2962020B2 (en) | 1999-10-12 |
Family
ID=11561802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP359492A Expired - Fee Related JP2962020B2 (en) | 1992-01-13 | 1992-01-13 | Absorption type heat pump device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2962020B2 (en) |
-
1992
- 1992-01-13 JP JP359492A patent/JP2962020B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2962020B2 (en) | 1999-10-12 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |