JPS6210348B2 - - Google Patents
Info
- Publication number
- JPS6210348B2 JPS6210348B2 JP1942081A JP1942081A JPS6210348B2 JP S6210348 B2 JPS6210348 B2 JP S6210348B2 JP 1942081 A JP1942081 A JP 1942081A JP 1942081 A JP1942081 A JP 1942081A JP S6210348 B2 JPS6210348 B2 JP S6210348B2
- Authority
- JP
- Japan
- Prior art keywords
- generator
- evaporator
- condenser
- absorption refrigerator
- ejector
- 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 20
- 239000006096 absorbing agent Substances 0.000 claims description 9
- 238000001704 evaporation Methods 0.000 claims 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 13
- 238000005057 refrigeration Methods 0.000 description 12
- 238000010586 diagram Methods 0.000 description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000003507 refrigerant Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は、蒸発器から冷媒蒸気を溶液に吸収
し、凝縮器へ溶液から冷媒蒸気を放出する吸収冷
凍機に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption refrigerator that absorbs refrigerant vapor from an evaporator into a solution and releases the refrigerant vapor from the solution to a condenser.
まず、このような吸収冷凍機の従来のものを図
面により説明する。 First, a conventional absorption refrigerator of this type will be explained with reference to the drawings.
第1図はアンモニア水溶液を使用する従来の一
重効用式吸収冷凍機を示すものであり、吸収器
1、発生器2、凝縮器3および蒸発器4が閉管路
内に配設されている。前記吸収器1には水などの
冷却源が流通する管路5が導通しており、この吸
収器1と前記発生器2とは相互に逆方向に流通す
る一対の管路6,7により接続されている。この
うち、一方の管路6にはポンプ8が介装されてお
り、吸収器1内のアンモニア水溶液を発生器2に
供給するようになつている。また、前記両管路
6,7に分けてエコノマイザ9が配設されてお
り、管路7内のアンモニア水溶液の熱を管路7内
のアンモニア水溶液へ伝達するようになつてい
る。 FIG. 1 shows a conventional single-effect absorption refrigerator using an aqueous ammonia solution, in which an absorber 1, a generator 2, a condenser 3, and an evaporator 4 are arranged in a closed pipe. The absorber 1 is connected to a pipe 5 through which a cooling source such as water flows, and the absorber 1 and the generator 2 are connected by a pair of pipes 6 and 7 that flow in opposite directions. has been done. A pump 8 is interposed in one of the pipe lines 6 to supply the ammonia aqueous solution in the absorber 1 to the generator 2. Further, an economizer 9 is arranged separately between the two pipes 6 and 7, and is configured to transfer the heat of the ammonia aqueous solution in the pipe 7 to the ammonia aqueous solution in the pipe 7.
前記発生器2には加熱源が流通する管路10が
導通しており、また、内部にはエリミネータ11
が配設されている。そして、この発生器2と前記
凝縮器3とは管路12により接続されている。こ
の凝縮器3には冷却源が流通する管路13が導通
しており、この凝縮器3と前記蒸発器4とは膨張
弁14の介装された管路15により接続されてい
る。さらに、この蒸発器4には被冷却源が流通す
る管路16が導通しており、この蒸発器4と前記
吸収器1とは管路17により接続されている。 A conduit 10 through which a heating source flows is connected to the generator 2, and an eliminator 11 is provided inside the generator 2.
is installed. The generator 2 and the condenser 3 are connected by a pipe 12. A condenser 3 is connected to a conduit 13 through which a cooling source flows, and the condenser 3 and the evaporator 4 are connected by a conduit 15 in which an expansion valve 14 is interposed. Furthermore, a pipe line 16 through which a source to be cooled flows is connected to the evaporator 4, and the evaporator 4 and the absorber 1 are connected by a pipe line 17.
前述した構成によれば、吸収器1からポンプ8
により汲み上げられたアンモニアの濃溶液はエコ
ノマイザ9を介して発生器2内へ達し、ここで加
熱源の流通している管路10からの熱により冷媒
のアンモニアはエリミネータ11を介して蒸発す
る。一方、アンモニアの蒸発した発生器2内の溶
液は稀溶液となり、前記エコノマイザ9で前記濃
溶液に熱を付与し、回収器1へ還流する。 According to the above-described configuration, from the absorber 1 to the pump 8
The concentrated ammonia solution pumped up reaches the generator 2 via the economizer 9, where the refrigerant ammonia is evaporated via the eliminator 11 by the heat from the pipe 10 through which the heating source flows. On the other hand, the solution in the generator 2 in which ammonia has evaporated becomes a dilute solution, which is heated by the economizer 9 and refluxed to the collector 1.
前述の蒸発したアンモニアは管路12を介して
凝縮器3に達し、ここで冷却源の流通している管
路13に熱を奪われ液化する。この液化したアン
モニアは管路15に介装された膨張弁14内で断
熱膨張し、ついで蒸発器4内で管路16内を流通
する被冷却源から蒸発潜熱を奪つて該被冷却源を
冷却する。そして、この気化したアンモニアは管
路17を介して吸収器1へ戻り、ここで管路7か
らの稀溶液とともにアンモニア濃溶液を形成して
1サイクルを完了する。 The evaporated ammonia mentioned above reaches the condenser 3 via the pipe line 12, where it is liquefied by being removed with heat by the pipe line 13 through which the cooling source flows. This liquefied ammonia expands adiabatically within the expansion valve 14 installed in the pipe line 15, and then takes away the latent heat of vaporization from the cooled source flowing through the pipe line 16 in the evaporator 4 to cool the cooled source. do. The vaporized ammonia then returns to the absorber 1 via the line 17, where it forms a concentrated ammonia solution together with the dilute solution from the line 7, completing one cycle.
このような従来の一重効用式吸引冷凍機のモリ
エル線図が第2図に示されている。第2図におい
て、i2―inは管路10内の熱源によつて与えら
れる圧縮仕事を示し、また、圧力Pnは管路13
内の冷却源の温度によつて定まる凝縮圧力であ
る。そして、冷凍効果はi2―i1′で示されている。
この図からわかるように、従来のこの種の吸収冷
凍機の系内最大圧力は冷却源の温度により決定さ
れる凝縮器の圧力(Pn)である。この圧力(P
n)を発生器2内の加熱源の温度に見合う圧力
(P2)にして加熱源の有効エネルギの損失をなくす
ようにすると、冷凍効果はi2―i1となり、この値
は前記のi2―i1′より小さく冷凍効果が悪化する欠
点があつた。 A Mollier diagram of such a conventional single-effect suction refrigerator is shown in FIG. In FIG. 2, i 2 -i n indicates the compression work provided by the heat source in the line 10, and the pressure P n is the pressure applied by the heat source in the line 13.
This is the condensing pressure determined by the temperature of the cooling source within. And the freezing effect is shown as i 2 −i 1 ′.
As can be seen from this figure, the maximum pressure in the system of this type of conventional absorption refrigerator is the condenser pressure (P n ) determined by the temperature of the cooling source. This pressure (P
n ) to a pressure (P 2 ) corresponding to the temperature of the heating source in the generator 2 to eliminate the loss of effective energy of the heating source, the refrigeration effect becomes i 2 −i 1 , and this value is equal to the above i 2 - i 1 ', the drawback was that the refrigeration effect deteriorated.
このような冷凍効果を改良するものとして第3
図に示す多重効用式吸収冷凍機が従来から知られ
ている。この種の吸収冷凍機は凝縮器3内にエリ
ミネータ19を介して低圧発生器18を隣接し、
この低圧発生器18内に発生器2からの管路12
を接続したものである。 The third method that improves this freezing effect is
A multi-effect absorption refrigerator shown in the figure is conventionally known. This type of absorption refrigerator has a low pressure generator 18 adjacent to the condenser 3 via an eliminator 19,
A line 12 from the generator 2 is inserted into this low pressure generator 18.
is connected.
前述した構成によれば、発生器2では管路10
内の加熱源に応じた圧力の蒸気を発生し、この蒸
気は管路12を介して低圧発生器18に達し、こ
こで低圧蒸気を発生する。そして、この蒸気は凝
縮器3内で凝縮して膨張弁14および蒸発器4を
通過し、冷凍効果を発揮する。 According to the configuration described above, in the generator 2, the pipe line 10
Steam is generated at a pressure depending on the heating source within, and this steam reaches a low pressure generator 18 via a line 12, where low pressure steam is generated. Then, this steam is condensed in the condenser 3, passes through the expansion valve 14 and the evaporator 4, and exhibits a refrigeration effect.
しかしながら、この種の従来の多重動用式吸収
冷凍機は低圧発生器18を設けたことで構成が複
雑化し、コストが高くなるという欠点があつた。 However, the provision of the low-pressure generator 18 in this type of conventional multi-operation type absorption refrigerating machine has the disadvantage of complicating the structure and increasing cost.
本発明は、前述した従来のものにおける欠点を
除去し、簡単な構成で、効率の良い冷凍効果の得
られる吸収冷凍機を提供することを目的としてな
されたもので、発生器と凝縮器とも接続する管路
にエゼクタを介装し、このエゼクタへ蒸発器から
の蒸気の一部を吸引するバイパス管路を配設した
ものである。 The present invention has been made for the purpose of eliminating the drawbacks of the conventional ones described above, and providing an absorption refrigerator that has a simple configuration and can obtain an efficient refrigeration effect, and is also connected to a generator and a condenser. In this system, an ejector is interposed in the conduit for the evaporator, and a bypass conduit is provided to suck some of the steam from the evaporator into the ejector.
以下、本発明を図面に示す実施例により説明す
る。なお、前述した従来のものと同一の構成につ
いては、図面中に同一の符号を付し、その説明は
省略する。 The present invention will be explained below with reference to embodiments shown in the drawings. Note that the same components as those of the conventional device described above are denoted by the same reference numerals in the drawings, and the explanation thereof will be omitted.
第4図において、発生器2および凝縮器3間を
接続する管路12にはエゼクタ20が介装されて
おり、このエゼクタ20はバイパス管路21を介
して蒸発器4と接続されている。 In FIG. 4, an ejector 20 is interposed in a pipe 12 connecting the generator 2 and the condenser 3, and the ejector 20 is connected to the evaporator 4 via a bypass pipe 21.
このような、吸収冷凍機のモリエル線図が第5
図に示されており、凝縮器3の圧力は管路13内
の冷却源温度によつて決まる圧力(Pn)であ
り、また発生器2の圧力は管路10の加熱源温度
によつて決まる圧力(P2)である。 The Mollier diagram of an absorption refrigerator like this is the fifth
The pressure in the condenser 3 is determined by the temperature of the cooling source in line 13 (P n ), and the pressure in the generator 2 is determined by the temperature of the heating source in line 10. is the determined pressure (P 2 ).
そして、前述した構成によれば、発生器2内で
発生した圧力(P2)の蒸気は管路12を介してエ
ゼクタ20へ導かれる。一方、このエゼクタ20
内へは蒸発器4からの発生蒸気の一部がバイパス
管路21を介して吸引されて圧縮され、この圧縮
された蒸気は前述した発生器2からの駆動蒸気に
混合される。つぎに、この混合蒸気は凝縮器3へ
導かれ液化し、液化後の冷媒は膨張弁14を介し
て蒸発器4へ導かれて冷凍効果を発揮する。 According to the above-described configuration, steam at a pressure (P 2 ) generated within the generator 2 is guided to the ejector 20 via the pipe line 12. On the other hand, this ejector 20
A portion of the generated steam from the evaporator 4 is drawn into the evaporator 4 through the bypass line 21 and compressed, and this compressed steam is mixed with the driving steam from the generator 2 described above. Next, this mixed vapor is led to the condenser 3 and liquefied, and the liquefied refrigerant is led to the evaporator 4 via the expansion valve 14 to exert a refrigeration effect.
ところで、この場合の冷凍効果は、第2図に示
した従来のi2―i1′に等しいi2―i1′(第5図)であ
るが、バイパス管路21からエゼクタ20内に吸
引する冷媒量だけ装置としての冷凍能力が増大す
る結果となる。 Incidentally, the refrigeration effect in this case is i 2 −i 1 ′ (FIG. 5), which is equal to the conventional i 2 − i 1 ′ shown in FIG. As a result, the refrigerating capacity of the device increases by the amount of refrigerant.
以上説明したように、本発明に係る吸収冷凍機
は、発生器と凝縮器とも接続する管路にエゼクタ
を介装し、このエゼクタへ蒸発器からの蒸気の一
部を吸引するバイパス管路を配設したので、冷凍
能力に寄与し得る冷凍量が増大し、簡単な構成に
もかかわらず効率の良い冷凍効果を得ることがで
きる。 As explained above, the absorption refrigerator according to the present invention includes an ejector interposed in the pipe line that connects the generator and the condenser, and a bypass pipe line that sucks a part of the steam from the evaporator into the ejector. Because of this arrangement, the amount of refrigeration that can contribute to the refrigeration capacity increases, and an efficient refrigeration effect can be obtained despite the simple configuration.
なお、本発明の吸収冷凍機は、実施例で説明し
たアンモニア・水式のみならず、水、臭化リチウ
ム式の吸収冷凍機にも適用できることはいうまで
もない。 It goes without saying that the absorption refrigerator of the present invention can be applied not only to the ammonia/water type absorption refrigerator described in the embodiment, but also to water and lithium bromide type absorption refrigerators.
第1図は従来の一重効用式吸収冷凍機の冷凍回
路図、第2図は第1図の吸収冷凍機のモリエル線
図、第3図は従来の多重効用式吸収冷凍機の冷凍
回路図、第4図は本発明に係る吸収冷凍機の実施
例を示す冷凍回路図、第5図は第4図の吸収冷凍
機のモリエル線図である。
1…吸収器、2…発生器、3…凝縮器、4…蒸
発器、9…エコノマイザ、11…エリミネータ、
20…エゼクタ、21…バイパス管路。
Figure 1 is a refrigeration circuit diagram of a conventional single-effect absorption refrigerator, Figure 2 is a Mollier diagram of the absorption refrigerator shown in Figure 1, and Figure 3 is a refrigeration circuit diagram of a conventional multiple-effect absorption refrigerator. FIG. 4 is a refrigeration circuit diagram showing an embodiment of the absorption refrigerator according to the present invention, and FIG. 5 is a Mollier diagram of the absorption refrigerator shown in FIG. 4. 1...Absorber, 2...Generator, 3...Condenser, 4...Evaporator, 9...Economizer, 11...Eliminator,
20...Ejector, 21...Bypass pipe line.
Claims (1)
路により接続し、発生器に加えた熱により蒸発器
で被冷却源を冷凍するようにした吸収冷凍機にお
いて、発生器と凝縮器とも接続する管路にエゼク
タを介装し、このエゼクタへ蒸発器から蒸気の一
部を吸引するバイパス管路を配設したことを特徴
とする吸収冷凍機。1 In an absorption refrigerator in which the absorber, generator, condenser, and evaporator are connected by a closed pipe line, and the source to be cooled is frozen by the evaporator using the heat added to the generator, the generator and condenser are also connected. 1. An absorption refrigerating machine characterized in that an ejector is interposed in a conduit for evaporating, and a bypass conduit for sucking a part of steam from an evaporator into the ejector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1942081A JPS57134669A (en) | 1981-02-12 | 1981-02-12 | Absorption refrigerating machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1942081A JPS57134669A (en) | 1981-02-12 | 1981-02-12 | Absorption refrigerating machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57134669A JPS57134669A (en) | 1982-08-19 |
| JPS6210348B2 true JPS6210348B2 (en) | 1987-03-05 |
Family
ID=11998762
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1942081A Granted JPS57134669A (en) | 1981-02-12 | 1981-02-12 | Absorption refrigerating machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57134669A (en) |
-
1981
- 1981-02-12 JP JP1942081A patent/JPS57134669A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57134669A (en) | 1982-08-19 |
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