JPS6372461U - - Google Patents
Info
- Publication number
- JPS6372461U JPS6372461U JP16788886U JP16788886U JPS6372461U JP S6372461 U JPS6372461 U JP S6372461U JP 16788886 U JP16788886 U JP 16788886U JP 16788886 U JP16788886 U JP 16788886U JP S6372461 U JPS6372461 U JP S6372461U
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- low
- temperature
- refrigerant vapor
- dilute 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.)
- Granted
Links
- 238000010521 absorption reaction Methods 0.000 claims description 6
- 230000009977 dual effect Effects 0.000 claims description 6
- 239000006096 absorbing agent Substances 0.000 claims description 3
- 241000234435 Lilium Species 0.000 claims description 2
- 239000003507 refrigerant Substances 0.000 claims 7
- 238000010438 heat treatment Methods 0.000 claims 4
- 239000000498 cooling water Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000007921 spray Substances 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 2
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
第１図は本考案に係る直焚二重効用吸収冷凍機
の実施例の概略構成図、第２図は従来の直焚二重
効用吸収冷凍機の概略構成図である。
１０…高温再生器、１２…加熱源、１６…分離
器、２２…低温再生器、２６…凝縮器、３４…蒸
発器、３６…高温熱交換器、４２…低温熱交換器
、４４…吸収器、５４…循環ポンプ、６０…排ガ
ス熱交換器、６６…ベンチユリ。
FIG. 1 is a schematic diagram of an embodiment of a direct-fired dual-effect absorption refrigerator according to the present invention, and FIG. 2 is a schematic diagram of a conventional direct-fired dual-effect absorption refrigerator. 10... High temperature regenerator, 12... Heat source, 16... Separator, 22... Low temperature regenerator, 26... Condenser, 34... Evaporator, 36... High temperature heat exchanger, 42... Low temperature heat exchanger, 44... Absorber , 54... Circulation pump, 60... Exhaust gas heat exchanger, 66... Bench lily.
Claims (1)
再生器と、この高温再生器により加熱した希溶液
を冷媒蒸気と中間濃度溶液とに分離する分離器と
、この分離器からの中間濃度溶液が前記高温再生
器に流入する希溶液と熱交換する高温熱交換器と
、前記分離器から導かれた冷媒蒸気により前記高
温熱交換器から流入する中間濃度溶液を加熱し、
冷媒蒸気と濃溶液とに分離する低温再生器と、こ
の低温再生器からの冷媒蒸気を凝縮させる凝縮器
と、この凝縮器により凝縮した液体冷媒が散布さ
れて蒸発し、冷却用水を冷却する低圧の蒸発器と
、前記低温再生器から流入した前記濃溶液が前記
高温熱交換器に流入する希溶液と熱交換をして冷
却される低温熱交換器と、この低温熱交換器から
の前記濃溶液が散布され、前記蒸発器から流入し
た蒸気を吸収して希溶液となる吸収器と、この吸
収器において生じた希溶液を前記低温熱交換器・
前記高温熱交換器を介して前記高温再生器に圧送
する循環ポンプと、前記低温熱交換器に流入する
希溶液の一部を加熱した冷媒蒸気を発生させる前
記加熱源の煙道に設けた排ガス熱交換器とを有す
る二重効用吸収冷凍機において、前記高温熱交換
器にて熱交換した中間濃度溶液を低温再生器に導
く配管に、前記排ガス熱交換器で発生させた冷媒
蒸気を吸引する吸引装置を設けたことを特徴とす
る二重効用吸収冷凍機。 (2) 前記吸引装置は、ベンチユリであることを
特徴とする実用新案登録請求の範囲第１項に記載
の二重効用吸収冷凍機。 (3) 前記吸引装置は、エゼクタであることを特
徴とする実用新案登録請求の範囲第１項に記載の
二重効用吸収冷凍機。[Claims for Utility Model Registration] (1) A high-temperature regenerator equipped with a heating source for heating a dilute solution, and a separator that separates the dilute solution heated by the high-temperature regenerator into refrigerant vapor and an intermediate concentration solution. , a high temperature heat exchanger in which an intermediate concentration solution from the separator exchanges heat with a dilute solution flowing into the high temperature regenerator; and an intermediate concentration solution flowing from the high temperature heat exchanger with refrigerant vapor led from the separator. heat the
A low-temperature regenerator that separates refrigerant vapor and a concentrated solution, a condenser that condenses the refrigerant vapor from the low-temperature regenerator, and a low-pressure regenerator that sprays and evaporates the liquid refrigerant condensed by the condenser to cool the cooling water. a low-temperature heat exchanger in which the concentrated solution flowing from the low-temperature regenerator is cooled by exchanging heat with the dilute solution flowing into the high-temperature heat exchanger; An absorber in which a solution is sprayed and absorbs the vapor flowing from the evaporator to become a dilute solution, and a dilute solution generated in this absorber is transferred to the low temperature heat exchanger.
a circulation pump that pumps pressure to the high-temperature regenerator via the high-temperature heat exchanger; and an exhaust gas installed in the flue of the heating source that generates refrigerant vapor by heating a portion of the dilute solution flowing into the low-temperature heat exchanger. In a dual-effect absorption refrigerator having a heat exchanger, refrigerant vapor generated in the exhaust gas heat exchanger is sucked into piping that leads the intermediate concentration solution heat-exchanged in the high-temperature heat exchanger to a low-temperature regenerator. A dual-effect absorption refrigerator characterized by being equipped with a suction device. (2) The dual-effect absorption refrigerator according to claim 1, wherein the suction device is a bench lily. (3) The dual-effect absorption refrigerator according to claim 1, wherein the suction device is an ejector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16788886U JPH0429339Y2 (en) | 1986-10-31 | 1986-10-31 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16788886U JPH0429339Y2 (en) | 1986-10-31 | 1986-10-31 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6372461U true JPS6372461U (en) | 1988-05-14 |
| JPH0429339Y2 JPH0429339Y2 (en) | 1992-07-16 |
Family
ID=31100245
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16788886U Expired JPH0429339Y2 (en) | 1986-10-31 | 1986-10-31 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0429339Y2 (en) |
-
1986
- 1986-10-31 JP JP16788886U patent/JPH0429339Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0429339Y2 (en) | 1992-07-16 |
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