JPH0353539B2 - - Google Patents
Info
- Publication number
- JPH0353539B2 JPH0353539B2 JP20275181A JP20275181A JPH0353539B2 JP H0353539 B2 JPH0353539 B2 JP H0353539B2 JP 20275181 A JP20275181 A JP 20275181A JP 20275181 A JP20275181 A JP 20275181A JP H0353539 B2 JPH0353539 B2 JP H0353539B2
- Authority
- JP
- Japan
- Prior art keywords
- absorber
- heat exchanger
- condenser
- heat
- cooling
- 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
Links
- 239000006096 absorbing agent Substances 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000001816 cooling Methods 0.000 claims description 15
- 239000000498 cooling water Substances 0.000 claims description 9
- 238000010521 absorption reaction Methods 0.000 claims description 4
- 239000003507 refrigerant Substances 0.000 description 13
- 238000010586 diagram Methods 0.000 description 4
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- 239000002918 waste heat Substances 0.000 description 2
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は発生器、吸収器、凝縮器、蒸発器、ポ
ンプを有する冷房装置における廃熱利用に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to waste heat utilization in a cooling system having a generator, absorber, condenser, evaporator and pump.
従来の冷房装置、例えば吸収式冷凍機では、吸
収器より濃溶液がポンプにより発生器に送られ
る。そして発生器で加熱され、冷媒蒸気が発生す
る。冷媒蒸気は凝縮器へ送られ、そこで冷却され
液化する。その際、冷媒蒸気は熱を放出する。液
化された冷媒は蒸発器に送られ、熱を奪い気化さ
れ吸収器に戻る。一方、発生器で冷媒蒸気を放出
した稀溶液は吸収器に戻され、蒸発器よりの冷媒
を吸収する。その際に吸収熱が発生する。従来の
冷房装置においては、凝縮器、吸収器で発生した
熱は水などを介して、冷却塔などで捨てられてい
た。 In conventional cooling systems, such as absorption refrigerators, a concentrated solution is pumped from an absorber to a generator. It is then heated in a generator to generate refrigerant vapor. The refrigerant vapor is sent to a condenser where it is cooled and liquefied. In doing so, the refrigerant vapor releases heat. The liquefied refrigerant is sent to the evaporator, where it absorbs heat and is vaporized before returning to the absorber. On the other hand, the dilute solution, which has released refrigerant vapor in the generator, is returned to the absorber and absorbs the refrigerant from the evaporator. At this time, absorbed heat is generated. In conventional cooling systems, the heat generated in the condenser and absorber is disposed of in a cooling tower or the like via water.
本発明は上記の凝縮器や吸収器で生じる熱を冷
却塔などですべて捨てることなく、有効に利用し
得る装置を提供しようとするものである。 The present invention aims to provide an apparatus that can effectively utilize the heat generated in the above-mentioned condenser and absorber without discarding it in a cooling tower or the like.
以下本発明の実施例を吸収式冷凍サイクルを用
いた添付図面により説明する。第1図は、吸収
器、凝縮器で生じた熱を吸収器から発生器へ送ら
れる濃溶液に与え、予熱することを示したサイク
ル図である。吸収器1には、冷媒(例えばフロン
22等)と溶媒(例えばジメチルホルムアミド
等)から成る溶液が満たされている。 Embodiments of the present invention will be described below with reference to the attached drawings, which use an absorption refrigeration cycle. FIG. 1 is a cycle diagram showing that heat generated in the absorber and condenser is applied to a concentrated solution sent from the absorber to the generator to preheat it. The absorber 1 is filled with a solution consisting of a refrigerant (eg, Freon 22, etc.) and a solvent (eg, dimethylformamide, etc.).
溶液は管路2を通り、ポンプ3により発生器1
1に送られ加熱され、冷媒蒸気を発生する。冷媒
蒸気は凝縮器14で凝縮され、管路15、絞り弁
16を通り、蒸発器17で周囲より熱を奪い気化
され、吸収器に戻る。一方、発生器11で冷媒の
蒸気を放出した溶液は、管路18、絞り弁4を通
り吸収器1に戻る。ここで、吸収器1では溶液が
冷媒を吸収するときには発熱反応を起こす。その
ため、吸収器1を冷却する必要がある。また凝縮
器14で冷媒を凝縮させるために、凝縮器14を
冷却する必要がある。なお、ここでは冷却には水
を用いることにする。吸収器1の冷却では、冷却
水は管路5を経て、吸収器1に設けた第1の熱交
換器25により吸収器1を冷却し、管路12を通
り、管路10へ流れる。また凝縮器14の冷却で
は、冷却水は管路9を経て、凝縮器14に設けた
第2の熱交換器26により凝縮器14を冷却し、
管路13を通り、管路10へ流れる。管路10を
通る冷却水は管路2を通る濃溶液と第3熱交換器
7で熱交換し、管路6、冷却塔8で放熱し、ポン
プ19を通り、管路5,9へ流れる。ここで、管
路10を通る冷却水は、吸収器1、凝縮器14で
の発熱が、それらの内部に有する熱交換器25,
26で熱交換されるため、管路2を通る濃溶液よ
りも高温となる。そのため、濃溶液は発生器11
に入る前に第3の熱交換器7で予熱される。 The solution passes through line 2 and is pumped to generator 1 by pump 3.
1, where it is heated and generates refrigerant vapor. The refrigerant vapor is condensed in a condenser 14, passes through a pipe 15 and a throttle valve 16, takes heat from the surroundings in an evaporator 17, is vaporized, and returns to the absorber. On the other hand, the solution from which the refrigerant vapor has been released in the generator 11 returns to the absorber 1 through the pipe 18 and the throttle valve 4. Here, in the absorber 1, an exothermic reaction occurs when the solution absorbs the refrigerant. Therefore, it is necessary to cool the absorber 1. Furthermore, in order to condense the refrigerant in the condenser 14, it is necessary to cool the condenser 14. Note that water will be used for cooling here. To cool the absorber 1 , the cooling water passes through the pipe 5 , cools the absorber 1 by a first heat exchanger 25 provided in the absorber 1 , passes through the pipe 12 , and flows into the pipe 10 . In addition, in cooling the condenser 14, the cooling water passes through the pipe 9 and cools the condenser 14 by a second heat exchanger 26 provided in the condenser 14.
It passes through conduit 13 and flows into conduit 10. The cooling water passing through the pipe 10 exchanges heat with the concentrated solution passing through the pipe 2 in the third heat exchanger 7, radiates heat in the pipe 6 and the cooling tower 8, passes through the pump 19, and flows to the pipes 5 and 9. . Here, the cooling water passing through the pipe line 10 is heated by the absorber 1 and the condenser 14, and the heat exchanger 25 and
26, the temperature is higher than that of the concentrated solution passing through the pipe 2. Therefore, the concentrated solution is
It is preheated in a third heat exchanger 7 before entering the air.
第2図は冷房装置と給湯装置を併用したとき、
吸収器・凝縮器で生じた熱を給湯水の加熱用とし
て使うためのシステム図である。第1図と同様、
吸収器1、凝縮器14よりの冷却水は第3の熱交
換器を内蔵した貯湯タンク20内で給湯水と熱交
換される。給湯水は所定の温度に達していないも
のは補助加熱器22で加熱され弁23を通り出湯
される。出湯されないものは給湯水用管路21を
通り貯湯タンク20に戻される。24は弁であ
る。なお、1〜19は第1図の同一のものであ
り、動作も同じであるので説明を省略する。 Figure 2 shows when the air conditioner and water heater are used together.
It is a system diagram for using the heat generated by the absorber/condenser to heat hot water. Similar to Figure 1,
Cooling water from the absorber 1 and condenser 14 is heat exchanged with hot water in a hot water storage tank 20 containing a third heat exchanger. If the hot water has not reached a predetermined temperature, it is heated by an auxiliary heater 22 and discharged through a valve 23. Hot water that is not tapped is returned to the hot water storage tank 20 through a hot water supply pipe 21. 24 is a valve. Incidentally, numerals 1 to 19 are the same as those in FIG. 1, and their operations are the same, so their explanation will be omitted.
以上のように、本発明は吸収ヒートポンプサイ
クル中の吸収器と発生器を結ぶ管路と冷却水回路
間に設けた第3の熱交換器により、発生器に入る
冷媒が予熱される、あるいは冷却水回路と給湯水
用管路間に設けられた第3の熱交換器により、従
来冷却塔等で捨てられていた廃熱で給湯水の予熱
が行われることを特徴とするものである。それに
よつて熱の有効利用を計り前記冷却塔や発生器の
容量を小さくするとともに補助熱源の使用量を削
減するものである。 As described above, the present invention enables the refrigerant entering the generator to be preheated or cooled by the third heat exchanger installed between the cooling water circuit and the pipe connecting the absorber and generator in the absorption heat pump cycle. The third heat exchanger provided between the water circuit and the hot water supply pipe is characterized in that the hot water supply water is preheated using waste heat that was conventionally discarded in a cooling tower or the like. This allows effective use of heat, reduces the capacity of the cooling tower and generator, and reduces the amount of auxiliary heat sources used.
第1図は本発明の実施例の冷房装置の説明図、
第2図は本発明の異なる実施例の冷房装置の説明
図である。
1……吸収器、3,19……ポンプ、4,16
……絞り弁、7……第3の熱交換器、8……冷却
塔、11……発生器、14……凝縮器、17……
蒸発器、20……第3の熱交換器を内蔵した貯湯
タンク、21……給湯水用管路、22……補助加
熱器、23,24……弁、25……第1の熱交換
器、26……第2の熱交換器。
FIG. 1 is an explanatory diagram of a cooling device according to an embodiment of the present invention;
FIG. 2 is an explanatory diagram of a cooling device according to a different embodiment of the present invention. 1...Absorber, 3,19...Pump, 4,16
... Throttle valve, 7 ... Third heat exchanger, 8 ... Cooling tower, 11 ... Generator, 14 ... Condenser, 17 ...
Evaporator, 20...Hot water storage tank incorporating third heat exchanger, 21...Hot water supply pipe, 22...Auxiliary heater, 23, 24...Valve, 25...First heat exchanger , 26... second heat exchanger.
Claims (1)
および前記吸収器に設けた第1の熱交換器と前記
凝縮器に設けた第2の熱交換器を構成要素とする
吸収式冷凍機と、前記両熱交換器、循環ポンプ、
冷却塔よりなる冷却水回路と、前記吸収器と前記
発生器を結ぶ管路と、上記冷却水回路間に設けた
第3の熱交換器を有する冷房装置。 2 冷却水回路と給湯水用管路間に設けられた第
3の熱交換器を有する特許請求の範囲第1項記載
の冷房装置。[Claims] 1. Generator, absorber, condenser, evaporator, pump,
and an absorption refrigerator comprising a first heat exchanger provided in the absorber and a second heat exchanger provided in the condenser, both heat exchangers, a circulation pump,
A cooling device comprising a cooling water circuit including a cooling tower, a pipe line connecting the absorber and the generator, and a third heat exchanger provided between the cooling water circuit. 2. The air conditioner according to claim 1, comprising a third heat exchanger provided between the cooling water circuit and the hot water supply pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20275181A JPS58104472A (en) | 1981-12-15 | 1981-12-15 | Air-cooling device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20275181A JPS58104472A (en) | 1981-12-15 | 1981-12-15 | Air-cooling device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58104472A JPS58104472A (en) | 1983-06-21 |
JPH0353539B2 true JPH0353539B2 (en) | 1991-08-15 |
Family
ID=16462556
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20275181A Granted JPS58104472A (en) | 1981-12-15 | 1981-12-15 | Air-cooling device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58104472A (en) |
-
1981
- 1981-12-15 JP JP20275181A patent/JPS58104472A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS58104472A (en) | 1983-06-21 |
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