JPS6125982B2 - - Google Patents
Info
- Publication number
- JPS6125982B2 JPS6125982B2 JP7650482A JP7650482A JPS6125982B2 JP S6125982 B2 JPS6125982 B2 JP S6125982B2 JP 7650482 A JP7650482 A JP 7650482A JP 7650482 A JP7650482 A JP 7650482A JP S6125982 B2 JPS6125982 B2 JP S6125982B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature regenerator
- solution
- refrigerant
- temperature
- low
- 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
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】
本発明は、二重効用吸収冷凍機に係り、負荷が
変動した場合に起り易い溶液系統への冷媒蒸気の
侵入を防止するようにした二重効用吸収冷凍機に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a double-effect absorption refrigerating machine, and more particularly, to a dual-effect absorption refrigerating machine that prevents refrigerant vapor from entering the solution system, which is likely to occur when the load fluctuates.
二重効用吸収冷凍機では、吸収溶液としてリチ
ウム塩水溶液、冷媒として水を用いるものが一般
的であり、冷水を得るために蒸発器にて蒸発した
蒸発冷媒を吸収器にて吸収溶液に吸収させ、この
冷媒を吸収した溶液(稀溶液)を高温再生器でバ
ーナ等の高温熱源で加熱して濃縮することにより
中間濃溶液を得、更に中間濃溶液を低温再生器で
前述の高温再生器で蒸発した高温の冷媒蒸気で再
度加熱して濃溶液を得ることにより吸収溶液及び
冷媒を再生し、これらを再度蒸発器及び吸収器に
て冷水を得るために使用されるように循環系を備
えている。なお、低温再生器から得られる冷媒蒸
気は凝縮器で凝縮されることは云うまでもない。 Dual-effect absorption refrigerators generally use a lithium salt aqueous solution as the absorption solution and water as the refrigerant.In order to obtain cold water, the evaporated refrigerant evaporated in the evaporator is absorbed into the absorption solution in the absorber. The solution (dilute solution) that has absorbed this refrigerant is heated and concentrated using a high-temperature heat source such as a burner in a high-temperature regenerator to obtain an intermediately concentrated solution, and then the intermediately concentrated solution is further regenerated in a low-temperature regenerator in the high-temperature regenerator described above. A circulation system is provided to regenerate the absorption solution and refrigerant by heating again with the evaporated hot refrigerant vapor to obtain a concentrated solution and to use these again in the evaporator and absorber to obtain chilled water. There is. It goes without saying that the refrigerant vapor obtained from the low-temperature regenerator is condensed in the condenser.
ところで、このような二重効用吸収冷凍機で
は、例えば高温再生器での加熱量が増加したため
それに伴なつて溶液の循環量が増大したり、逆に
加熱量が減少したために溶液の循環量が減少した
りすることが起るが、このような場合に、冷媒蒸
気が溶液経路中に混入してしまい、冷凍能力を低
下させる難点があつた。 By the way, in such a dual-effect absorption refrigerator, for example, as the amount of heating in the high-temperature regenerator increases, the amount of solution circulated increases, or conversely, as the amount of heating decreases, the amount of solution circulated increases. However, in such cases, refrigerant vapor gets mixed into the solution path, resulting in a reduction in refrigeration capacity.
そこで従来は、高温再生器から低温再生器へ至
る溶液経路中に、圧力差を保つためのキヤピラ
リ、オリフイス或いはモータバルブ等を設けてい
たが、このようなものでは或る程度の負荷変動に
対しては蒸気の侵入を防ぐことができるものの、
過度の負荷変動に対しては対処しきれずに、蒸気
の侵入を許してしまつたり、或いは必要以上に溶
液を高温再生器に溜めてしまつたりする欠点があ
つた。 Therefore, in the past, capillaries, orifices, motor valves, etc. were installed in the solution path from the high-temperature regenerator to the low-temperature regenerator to maintain the pressure difference. Although it is possible to prevent steam from entering,
This method has the drawback of not being able to deal with excessive load fluctuations, allowing steam to enter, or storing more solution in the high-temperature regenerator than necessary.
本発明は、このような従来の欠点を除去するこ
とを目的としてなされたものである。 The present invention has been made with the aim of eliminating such conventional drawbacks.
以下本発明に係る二重効用吸収冷凍機の一実施
例を、第1図及び第2図を参照して詳細に説明す
る。 An embodiment of the dual-effect absorption refrigerator according to the present invention will be described in detail below with reference to FIGS. 1 and 2.
第1図は、この発明の一実施例を示す系統図で
あり、まず構成を説明すると1はガスバーナ等の
高温熱源を使用し稀溶液を加熱して濃縮する高温
再生器、2は高温再生器1で加熱された溶液を中
間濃溶液と冷媒蒸気とに分離するための分離器、
3は前記高温再生器1からの冷媒蒸気を熱源とし
て、高温再生器1からの中間濃溶液を再加熱し更
に冷媒蒸気を分離させる低温再生器、4は低温再
生器3からの冷媒蒸気を凝縮し、低温再生器3で
加熱源として使われた冷媒を冷却するための凝縮
器、5は、凝縮器4からの冷媒を蒸発されその際
発生する潜熱を利用して、負荷の冷水を冷却する
蒸発器、6は蒸発器5からの冷媒蒸気を低温再生
器3で濃縮された濃溶液に吸収させるための吸収
器、7は吸収器6からの稀溶液を高温再生器へ流
入させるための溶液循環ポンプ、8は低温熱交換
器、9は高温熱交換器、10は形状記憶合金を使
つた流量調節器であり、これらは管略11ないし
20及び23,24によつて接続されて、冷凍サ
イクルを構成している。 FIG. 1 is a system diagram showing one embodiment of the present invention. First, the configuration will be explained. 1 is a high-temperature regenerator that heats and concentrates a dilute solution using a high-temperature heat source such as a gas burner, and 2 is a high-temperature regenerator. a separator for separating the solution heated in step 1 into an intermediate concentrated solution and a refrigerant vapor;
3 is a low-temperature regenerator that uses the refrigerant vapor from the high-temperature regenerator 1 as a heat source to reheat the intermediate concentrated solution from the high-temperature regenerator 1 and further separates the refrigerant vapor; 4 is a low-temperature regenerator that condenses the refrigerant vapor from the low-temperature regenerator 3; A condenser 5 for cooling the refrigerant used as a heating source in the low-temperature regenerator 3 uses the latent heat generated when the refrigerant from the condenser 4 is evaporated to cool the chilled water of the load. An evaporator, 6 an absorber for absorbing the refrigerant vapor from the evaporator 5 into the concentrated solution concentrated in the low temperature regenerator 3, and 7 a solution for flowing the dilute solution from the absorber 6 into the high temperature regenerator. A circulation pump, 8 a low-temperature heat exchanger, 9 a high-temperature heat exchanger, and 10 a flow regulator using a shape memory alloy, are connected by pipes 11 to 20 and 23, 24, constitutes a cycle.
次に作用を説明する。 Next, the action will be explained.
二重効用吸収冷凍機に於て、高温再生器1で濃
縮され分離器2で冷媒を分離した中間濃溶液は、
管路14を通り高温熱交換器9を経て、管路15
へ導かれ、ここで流量調節器10によつて流量が
制御され低温再生器3に流入する。 In the dual-effect absorption refrigerator, the intermediate concentrated solution is concentrated in the high-temperature regenerator 1 and the refrigerant is separated in the separator 2.
Passing through the pipe 14 and passing through the high temperature heat exchanger 9, the pipe 15
Here, the flow rate is controlled by the flow rate regulator 10 and flows into the low temperature regenerator 3.
次にこの流量調節器10について詳しく説明す
る。第2図に示した様に流量調節器10は、中間
濃溶液の管路15出口に設けた形状記憶合金を使
つたばね21の伸び縮みによつて移動する弁22
によつて構成されている。形状記憶合金はある臨
界温度以上になると元の形にもどろうとする性質
を持つているため、管路15を出る中間濃溶液の
温度によつてこのばね21が伸縮する。 Next, this flow regulator 10 will be explained in detail. As shown in FIG. 2, the flow rate regulator 10 includes a valve 22 that moves by the expansion and contraction of a spring 21 made of a shape memory alloy provided at the outlet of the intermediate concentrated solution pipe 15.
It is composed of. Since the shape memory alloy has the property of returning to its original shape when the temperature exceeds a certain critical temperature, the spring 21 expands and contracts depending on the temperature of the intermediate concentrated solution exiting the pipe 15.
例えば高温再生器1の加熱量が増加するとそれ
に伴なつて中間濃溶液の管路15出口温度が上昇
する。ここでばね21を形成する形状記憶合金に
高温で縮む様な形状を記憶させて加工しておくこ
とにより、温度上昇に伴なうばね10の縮みとと
もに弁22が開き、管路15出口すなわちノズル
出口の開口面積を大きくすることが出来る。ま
た、高温再生器1の加熱量が減少するとばね21
が伸び、それに伴なつてノズル出口の開口面積が
減少することになる。このことにより、負荷に対
する高温再生器1の加熱量の比例的又は段階的制
御における溶液の循環流量の変化に対処出来、高
温再生器1から低温再生器3への溶液を適正な流
量に維持することが可能となる。 For example, when the heating amount of the high-temperature regenerator 1 increases, the temperature at the outlet of the intermediate concentrated solution pipe 15 increases accordingly. Here, by processing the shape memory alloy that forms the spring 21 to memorize a shape that shrinks at high temperatures, the valve 22 opens as the spring 10 contracts as the temperature rises, and the outlet of the pipe 15, that is, the nozzle. The opening area of the outlet can be increased. Moreover, when the heating amount of the high temperature regenerator 1 decreases, the spring 21
increases, and the opening area of the nozzle outlet decreases accordingly. This makes it possible to cope with changes in the circulation flow rate of the solution in proportional or stepwise control of the heating amount of the high-temperature regenerator 1 to the load, and maintains the solution from the high-temperature regenerator 1 to the low-temperature regenerator 3 at an appropriate flow rate. becomes possible.
尚弁22は管路16側に設けても同様に機能す
ることは云うまでもない。 It goes without saying that the valve 22 functions similarly even if it is provided on the conduit 16 side.
以上説明してきたように、この発明によれば次
の様な効果が得られる。 As explained above, according to the present invention, the following effects can be obtained.
高温再生器1の加熱量が増加し、それに伴なつ
て溶液の循環量が増大した時、この流量調節器1
0の開口面積が広がり、必要以上に溶液を高温再
生器1及び分離器2内に溜めることなく、系内の
溶液のバランスが保たれ、正常な運転を継続する
ことが出来る。また、高温再生器1の加熱量が減
少し溶液の循環量が減少した場合、流量調整器1
0の開口面積が狭まり分離器2内に溶液を一定量
溜めることにより低温再生器3内に蒸気が混入す
ることを防ぎ、冷凍能力の低下等を防止すること
が出来る。 When the heating amount of the high temperature regenerator 1 increases and the circulation amount of the solution increases accordingly, this flow rate regulator 1
The opening area of 0 is expanded, the solution is not stored in the high temperature regenerator 1 and the separator 2 more than necessary, the balance of the solution in the system is maintained, and normal operation can be continued. In addition, when the heating amount of the high temperature regenerator 1 decreases and the circulation amount of the solution decreases, the flow rate regulator 1
By narrowing the opening area of 0 and storing a certain amount of solution in the separator 2, it is possible to prevent steam from entering the low-temperature regenerator 3 and to prevent a decrease in the refrigerating capacity.
更にモジユトロール弁よりも安価であり、オリ
フイスやキヤピラリーなどと比べて制御が安定し
ている。 Furthermore, it is cheaper than a modular control valve, and its control is more stable than an orifice or capillary.
第1図は、本発明に係る二重効用吸収冷凍機の
一実施例を示す系統図、第2図は本発明に使用さ
れる流量調節器の一例の概略的な構成を示した図
である。
1……高温再生器、2……分離器、3……低温
再生器、4……凝縮器、5……蒸発器、6……吸
収器、7……溶液循環ポンプ、8……低温熱交換
器、9……高温熱交換器、10……流量調節器、
21……形状記憶合金を使つたばね、22……
弁。
FIG. 1 is a system diagram showing an embodiment of a dual-effect absorption refrigerator according to the present invention, and FIG. 2 is a diagram showing a schematic configuration of an example of a flow rate regulator used in the present invention. . 1... High temperature regenerator, 2... Separator, 3... Low temperature regenerator, 4... Condenser, 5... Evaporator, 6... Absorber, 7... Solution circulation pump, 8... Low temperature heat exchanger, 9...high temperature heat exchanger, 10...flow regulator,
21... Spring using shape memory alloy, 22...
valve.
Claims (1)
高温再生器と、この高温再生器で濃縮された中間
濃溶液を前記高温再生器で生じた冷媒蒸気で加熱
する低温再生器と、この低温再生器で生じた冷媒
蒸気及び加熱源として使われた冷媒を凝縮する凝
縮器と、この凝縮器からの液体冷媒を蒸発させて
冷水を得る蒸発器と、この蒸発器で蒸発した冷媒
を前記低温再生器で濃縮された濃溶液に吸収させ
て稀溶液とする吸収器とを有し、これらが循環系
を形成するように配管接続されている二重効用吸
収冷凍機において、前記高温再生器から前記低温
再生器に至る中間濃溶液通路中に、通過する中間
濃溶液温度に応じて開口面積が変化するように少
なくとも弁機構の一部として形状記憶合金を用い
た流量調節器を設けたことを特徴とする二重効用
吸収冷凍機。1. A high-temperature regenerator that heats a dilute solution that has absorbed refrigerant with a high-temperature heat source, a low-temperature regenerator that heats an intermediate concentrated solution concentrated in this high-temperature regenerator with refrigerant vapor generated in the high-temperature regenerator, and this low-temperature regenerator. a condenser that condenses the refrigerant vapor generated in the refrigerant and the refrigerant used as a heating source; an evaporator that evaporates the liquid refrigerant from the condenser to obtain cold water; In a dual-effect absorption refrigerator, the double-effect absorption refrigerator has an absorber that absorbs the concentrated solution concentrated in the regenerator to form a dilute solution, and these are connected via piping to form a circulation system. A flow regulator using a shape memory alloy as at least a part of the valve mechanism is provided in the intermediate concentrated solution passage leading to the low temperature regenerator so that the opening area changes depending on the temperature of the intermediate concentrated solution passing through. A dual-effect absorption refrigerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7650482A JPS58195766A (en) | 1982-05-10 | 1982-05-10 | Double effect absorption chiller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7650482A JPS58195766A (en) | 1982-05-10 | 1982-05-10 | Double effect absorption chiller |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58195766A JPS58195766A (en) | 1983-11-15 |
| JPS6125982B2 true JPS6125982B2 (en) | 1986-06-18 |
Family
ID=13607062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7650482A Granted JPS58195766A (en) | 1982-05-10 | 1982-05-10 | Double effect absorption chiller |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58195766A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2770297B2 (en) * | 1993-10-18 | 1998-06-25 | 宏一 渡部 | Movable body opening / closing suppression device |
-
1982
- 1982-05-10 JP JP7650482A patent/JPS58195766A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58195766A (en) | 1983-11-15 |
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