JPS6148065B2 - - Google Patents
Info
- Publication number
- JPS6148065B2 JPS6148065B2 JP7536279A JP7536279A JPS6148065B2 JP S6148065 B2 JPS6148065 B2 JP S6148065B2 JP 7536279 A JP7536279 A JP 7536279A JP 7536279 A JP7536279 A JP 7536279A JP S6148065 B2 JPS6148065 B2 JP S6148065B2
- Authority
- JP
- Japan
- Prior art keywords
- generator
- exhaust gas
- temperature
- refrigerant
- hot 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.)
- Expired
Links
- 238000010521 absorption reaction Methods 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000003507 refrigerant Substances 0.000 claims description 23
- 239000006096 absorbing agent Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000000498 cooling water Substances 0.000 claims description 3
- 238000005057 refrigeration Methods 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 17
- 238000004378 air conditioning Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Description
【発明の詳細な説明】
本発明は排ガス吸収冷凍機に関するもので、排
ガス真空ボイラーを組合わせることにより排ガス
の有する熱エネルギーを吸収冷凍機と排ガス真空
ボイラーで回収して大きな冷凍能力を得ることを
目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an exhaust gas absorption refrigerator, and by combining an exhaust gas vacuum boiler, the absorption refrigerator and the exhaust gas vacuum boiler are used to recover the thermal energy of the exhaust gas, thereby obtaining a large refrigerating capacity. purpose.
工場などより排出される排ガスを吸収冷凍機で
2段階に熱回収する場合には、排ガス回収用発生
器を2個配置する方法がある。 When heat is recovered in two stages from exhaust gas discharged from a factory or the like using an absorption refrigerator, there is a method of arranging two exhaust gas recovery generators.
しかしながら、一度熱回収された排ガスは温度
が下がり、次に熱回収する発生器は多くの伝熱面
が必要となり形状が大きくなると共に吸収液量が
増し、コスト的にも高くなるという欠点があつ
た。 However, once the heat is recovered, the temperature of the exhaust gas decreases, and the generator that then recovers the heat requires many heat transfer surfaces, resulting in a larger shape and an increase in the amount of absorption liquid, which has the disadvantage of increasing costs. Ta.
本発明は上記の欠点を解消するためになされた
もので以下図に示す実施例について説明する。1
は排ガスを利用して製造された温水を熱源として
稀吸収液より冷媒を加熱分離する温水用発生器、
2は排ガスを熱源として一次中間吸収液から冷媒
を加熱分離する高温発生器、3は前記高温発生器
2で分離された冷媒蒸気を熱源として二次中間吸
収液を再熱し冷媒を更に加熱分離する低温発生
器、4及び5は前記温水用発生器1と前記高温発
生器2、低温発生器3から夫々流入する冷媒を冷
却器6,7で冷却して凝縮する凝縮器、8は前記
両凝縮器4,5からの液冷媒を散布し気化させる
際の潜熱を利用して冷水器9から冷房用の冷水を
得るようにした蒸発器、10は前記各発生器1,
2,3で順次冷媒を加熱分離して濃縮された濃吸
収液を散布して器内の冷媒蒸気を吸収することに
より前記蒸発器8の内部を低圧に維持し連続した
冷水の供給を行なえるようにした吸収器、11及
び12は低温熱交換器と高温熱交換器で、これら
は冷媒蒸気配管13、冷媒液流下管14,15、
冷媒ポンプ16を有する冷媒循環路17、吸収液
ポンプ18を有する稀吸収液管路19、中間吸収
液ポンプ20を有する一次中間吸収液管路21、
二次中間吸収液管路22及び濃吸収液管路23に
より配管接続して吸収冷凍サイクルを構成してい
る。 The present invention has been made to solve the above-mentioned drawbacks, and an embodiment shown in the drawings will be described below. 1
is a hot water generator that uses hot water produced using exhaust gas as a heat source to heat and separate refrigerant from dilute absorption liquid.
2 is a high-temperature generator that heats and separates the refrigerant from the primary intermediate absorption liquid using exhaust gas as a heat source, and 3 uses the refrigerant vapor separated by the high-temperature generator 2 as a heat source to reheat the secondary intermediate absorption liquid and further heat and separate the refrigerant. low temperature generators; 4 and 5 are condensers that cool and condense the refrigerant flowing from the hot water generator 1, high temperature generator 2, and low temperature generator 3, respectively, in coolers 6 and 7; 8 is a condenser for both of the above condensers; An evaporator that obtains cold water for air conditioning from a water cooler 9 by utilizing the latent heat when the liquid refrigerant from the containers 4 and 5 is dispersed and vaporized;
By successively heating and separating the refrigerant in steps 2 and 3 and dispersing the concentrated concentrated absorption liquid to absorb the refrigerant vapor inside the vessel, the inside of the evaporator 8 can be maintained at a low pressure and a continuous supply of cold water can be performed. The absorbers 11 and 12 are a low-temperature heat exchanger and a high-temperature heat exchanger, and these include a refrigerant vapor pipe 13, a refrigerant liquid downflow pipe 14, 15,
A refrigerant circulation path 17 having a refrigerant pump 16, a dilute absorption liquid line 19 having an absorption liquid pump 18, a primary intermediate absorption liquid line 21 having an intermediate absorption liquid pump 20,
A secondary intermediate absorption liquid pipe line 22 and a concentrated absorption liquid pipe line 23 are connected to form an absorption refrigeration cycle.
而して24は前記高温発生器2を加熱した後の
排ガス路25に設けた排ガス空真ボイラーで該ボ
イラーで製造された温水は温水循環ポンプ26を
有した温水回路27を通り前記温水発生器1に供
給れる。 Reference numeral 24 denotes an exhaust gas vacuum boiler installed in the exhaust gas path 25 after heating the high temperature generator 2, and hot water produced by the boiler passes through a hot water circuit 27 having a hot water circulation pump 26 to the hot water generator. 1.
次に動作について説明する。 Next, the operation will be explained.
まず排ガスは高温発生器2で熱回収され温度が
下がり次に排ガス真空ボイラー24に入いり熱回
収される。排ガス真空ボイラー24から取出され
た温水により温水用発生器1が加熱されて稀吸収
液から冷媒を分離すると共に排ガス及び冷媒蒸気
により高温発生器2と低温発生器3を加熱して一
次、二次中間吸収液から夫々冷媒を分離する。こ
れらの冷媒は凝縮器4,5で液化した後蒸発器8
に散布されて気化する。 First, the exhaust gas is heat-recovered by the high-temperature generator 2, and its temperature is lowered.Then, the exhaust gas enters the exhaust-gas vacuum boiler 24, where the heat is recovered. The hot water generator 1 is heated by the hot water taken out from the exhaust gas vacuum boiler 24 to separate the refrigerant from the dilute absorption liquid, and the high temperature generator 2 and the low temperature generator 3 are heated by the exhaust gas and refrigerant vapor to generate primary and secondary Each refrigerant is separated from the intermediate absorption liquid. These refrigerants are liquefied in condensers 4 and 5 and then transferred to an evaporator 8.
is dispersed and vaporized.
この時の気化熱により冷水器9から冷水が得ら
れる。一方前記各発生器1,2,3で順次冷媒を
分離して濃縮された濃吸収液は吸収器10に散布
されて気化冷媒を吸収して稀吸収液となる。 Cold water is obtained from the water cooler 9 by the heat of vaporization at this time. On the other hand, the refrigerant is sequentially separated and concentrated in the generators 1, 2, and 3, and the concentrated absorption liquid is distributed to the absorber 10 to absorb the vaporized refrigerant and become a dilute absorption liquid.
尚冷却水は吸収器10と温水用発生器1の凝縮
器4に先ず流れその後低温発生器3に隣接した凝
縮器5に流れる。 Note that the cooling water first flows to the absorber 10 and the condenser 4 of the hot water generator 1, and then to the condenser 5 adjacent to the low temperature generator 3.
本発明による排ガス吸収冷凍機は上述の如く排
ガスを加熱源とする高温発生器、該発生器で分離
された冷媒蒸気を加熱源とする低温発生器、凝縮
器、蒸発器、吸収器、低温熱交換器及び高温熱交
換器を配管接続して冷凍サイクルを構成すると共
に前記吸収器から高温発生器に至る溶液循環系路
に排ガス真空ボイラーで加熱された温水を熱源と
する温水用発生器を設けてなるものであるから、
排ガスのもつ熱エネルギーを有効に回収出来排ガ
ス吸収冷凍機において大きな冷凍能力が得られ
る。 As described above, the exhaust gas absorption refrigerator according to the present invention includes a high-temperature generator that uses exhaust gas as a heating source, a low-temperature generator that uses refrigerant vapor separated by the generator as a heating source, a condenser, an evaporator, an absorber, and a low-temperature heat generator. A refrigeration cycle is constructed by connecting the exchanger and the high-temperature heat exchanger with piping, and a hot water generator whose heat source is hot water heated by an exhaust gas vacuum boiler is provided in the solution circulation path from the absorber to the high-temperature generator. Because it is,
Thermal energy contained in exhaust gas can be effectively recovered and a large refrigerating capacity can be obtained in the exhaust gas absorption refrigerator.
尚排ガス真空ボイラーからは給湯暖房又は再熱
用温水の供給も可能である。 It is also possible to supply hot water for hot water heating or reheating from the exhaust gas vacuum boiler.
図面は本発明による排ガス吸収冷凍機の回路構
成図である。
1……温水用発生器、2……高温発生器、3…
…低温発生器、10……吸収器、24……排ガス
真空ボイラー、27……温水回路。
The drawing is a circuit diagram of an exhaust gas absorption refrigerator according to the present invention. 1...Hot water generator, 2...High temperature generator, 3...
...Low temperature generator, 10...Absorber, 24...Exhaust gas vacuum boiler, 27...Hot water circuit.
Claims (1)
で分離された冷媒蒸気を加熱源とする低温発生
器、凝縮器、蒸発器、吸収器。低温熱交換器及び
高温熱交換器を配管接続して冷凍サイクルを構成
すると共に前記吸収器から高温発生器に至る溶液
循環系路に排ガス真空ボイラーで加熱された温水
を熱源とする温水用発生器を設けてなることを特
徴とする排ガス吸収冷凍機。 2 第1項に記載の凝縮器が低温発生器および高
温発生器からの冷媒を冷却しつつ液化する凝縮器
とこの凝縮器に流入する冷却水よりも低温の冷却
水により温水用発生器からの冷媒を液化する凝縮
器とで構成されている排ガス吸収冷凍機。[Claims] 1. A high-temperature generator using exhaust gas as a heating source, a low-temperature generator using refrigerant vapor separated by the generator as a heating source, a condenser, an evaporator, and an absorber. A refrigeration cycle is constructed by connecting a low-temperature heat exchanger and a high-temperature heat exchanger with piping, and a hot water generator uses hot water heated by an exhaust gas vacuum boiler as a heat source in a solution circulation path from the absorber to a high-temperature generator. An exhaust gas absorption refrigerating machine characterized by being provided with. 2. The condenser described in paragraph 1 liquefies the refrigerant while cooling it from the low-temperature generator and the high-temperature generator, and the refrigerant from the hot water generator is cooled by cooling water at a lower temperature than the cooling water flowing into the condenser. An exhaust gas absorption refrigerator consists of a condenser that liquefies the refrigerant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7536279A JPS56962A (en) | 1979-06-14 | 1979-06-14 | Exhaust gas absorption refrigerating machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7536279A JPS56962A (en) | 1979-06-14 | 1979-06-14 | Exhaust gas absorption refrigerating machine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56962A JPS56962A (en) | 1981-01-08 |
JPS6148065B2 true JPS6148065B2 (en) | 1986-10-22 |
Family
ID=13574025
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7536279A Granted JPS56962A (en) | 1979-06-14 | 1979-06-14 | Exhaust gas absorption refrigerating machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56962A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0390645U (en) * | 1989-12-28 | 1991-09-17 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62272068A (en) * | 1987-02-06 | 1987-11-26 | 株式会社荏原製作所 | Absorption refrigerator |
-
1979
- 1979-06-14 JP JP7536279A patent/JPS56962A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0390645U (en) * | 1989-12-28 | 1991-09-17 |
Also Published As
Publication number | Publication date |
---|---|
JPS56962A (en) | 1981-01-08 |
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