JPS6159166A - Absorption refrigerator - Google Patents
Absorption refrigeratorInfo
- Publication number
- JPS6159166A JPS6159166A JP18017084A JP18017084A JPS6159166A JP S6159166 A JPS6159166 A JP S6159166A JP 18017084 A JP18017084 A JP 18017084A JP 18017084 A JP18017084 A JP 18017084A JP S6159166 A JPS6159166 A JP S6159166A
- Authority
- JP
- Japan
- Prior art keywords
- cooling water
- temperature
- load
- machine
- absorption
- 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.)
- Pending
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(イ)産業上の利用分野
本発明は負荷に応じて発生器の加熱量を調節するように
した吸収冷凍機の改良に関する。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to an improvement in an absorption refrigerator in which the amount of heating of a generator is adjusted according to the load.
(ロ)従来の技術
吸収冷凍機においては、発生器の加熱量を調節して冷凍
能力をコントロールすることにより、負荷に見合う冷水
を取出すことが一般に行われている。例えば負荷が半分
に減った時、発生器の加熱量を半分に減じて冷凍能力を
ほぼ半減させるのである。このことは、吸収冷凍機の熱
収支の観点に立って考えた場合、機内への入熱量すなわ
ち発生器および蒸発器での吸熱量を半減させることであ
り、吸収器および凝縮器での放熱量すなわち機外への出
熱量を半減させることにほかならない。それ故、負荷に
応じて発生器の加熱量を調節するようにした吸収冷凍機
においては、負荷に見合う冷水を安全かつ迅速に取出す
ために、例えば吸収冷凍機への入熱量が半減した時、吸
収冷凍機からの出熱量も迅速に半減させて熱収支を速や
かにバランスさせる必要がある。そして、出熱量(吸収
器および凝縮器の放熱量)を迅速に半減させる従来の技
術としては、負荷検出器の信号で冷却水用ポンプの稼働
台数を半減させる手段(例えば特公昭53−2216号
公報)がある。(B) Conventional technology In absorption refrigerators, it is generally done to extract cold water that matches the load by controlling the refrigerating capacity by adjusting the heating amount of the generator. For example, when the load is cut in half, the amount of heat generated by the generator is cut in half and the refrigeration capacity is cut in half. When considered from the perspective of the heat balance of the absorption chiller, this means that the amount of heat input into the machine, that is, the amount of heat absorbed by the generator and evaporator, is halved, and the amount of heat released by the absorber and condenser is halved. In other words, this means nothing more than halving the amount of heat output to the outside of the machine. Therefore, in an absorption refrigerator that adjusts the heating amount of the generator according to the load, in order to safely and quickly take out cold water that matches the load, for example, when the amount of heat input to the absorption refrigerator is halved, It is also necessary to quickly reduce the amount of heat output from the absorption chiller by half to quickly balance the heat balance. As a conventional technique for quickly reducing the amount of heat output (the amount of heat dissipated from the absorber and condenser) by half, there is a method for halving the number of operating cooling water pumps using a signal from a load detector (for example, Japanese Patent Publication No. 53-2216 There is a public notice).
(ハ)発明が解決しようとする問題点
上記のような従来の手段は、吸収冷凍機に流入する冷却
水の温度(以下、冷却水入口温度という)がほぼ定格値
に保たれている場合には有用であるものの、冷却水入口
温度が変化する場合には吸収冷凍機の運転を安全に続け
ることが困難となる問題点を有していた。例えば冷却水
入口温度が高くなった場合、それに伴って冷却水出口温
度(吸収冷凍機の凝縮器から流出する冷却水の温度)も
高くなるため、凝縮器や発生器内の温度および圧力が高
くなる。そして、これら機器内の部材の歪みや腐食が大
きくなるため(特に、二重効用吸収冷凍機においては、
高温発生器内の部材の歪みや高温の吸収液による部材の
腐食が大きくなるため)、保護装置が働いて運転が停止
されることになる。(C) Problems to be Solved by the Invention The conventional means as described above can only be used when the temperature of the cooling water flowing into the absorption chiller (hereinafter referred to as the cooling water inlet temperature) is maintained at approximately the rated value. Although this method is useful, it has the problem that it is difficult to continue operating the absorption refrigerator safely when the cooling water inlet temperature changes. For example, if the cooling water inlet temperature increases, the cooling water outlet temperature (the temperature of the cooling water flowing out from the condenser of an absorption chiller) also increases, resulting in higher temperatures and pressures inside the condenser and generator. Become. This also increases distortion and corrosion of the components inside these devices (especially in dual-effect absorption refrigerators).
(Due to the distortion of the parts inside the high temperature generator and the corrosion of the parts by the high temperature absorption liquid, the protection device is activated and the operation is stopped.)
また、逆に冷却水入口温度が低くなり過ぎた場合には、
冷水の凍結や吸収液の結晶などを生じるおそれがあるた
め、保護装置が働いて運転が停止されることになる。Conversely, if the cooling water inlet temperature becomes too low,
Since there is a risk of freezing of the cold water or crystallization of the absorption liquid, a protective device will be activated and the operation will be stopped.
本発明は、このような問題点に鑑み、運転を安全に継続
させつつ負荷に見合う冷水を取出すことのできる吸収冷
凍機の提供を目的としたものである。SUMMARY OF THE INVENTION In view of these problems, the present invention aims to provide an absorption refrigerating machine that can safely continue operation and extract chilled water suitable for the load.
に)問題点を解決するための手段
本発明は、上記の問題点を解決する手段として、負荷に
応じて発生器の加熱量を調節する吸収冷凍機において、
冷却水の流量を冷却水入口温度で補償しつつ負荷に応じ
て調節する構成としたものである。B) Means for Solving the Problems The present invention provides, as a means for solving the above problems, an absorption refrigerator that adjusts the heating amount of the generator according to the load.
The configuration is such that the flow rate of the cooling water is adjusted according to the load while compensating the flow rate of the cooling water using the cooling water inlet temperature.
(ホ)作用
本発明による手段においては、例えば負荷が全負荷の5
0%であるときに冷却水入口温度が定格値より低くなっ
ている場合、従来の手段のように冷却水流量が50%減
じられるのではなく、冷却水流量が50%以上減じられ
るように冷却水流量を調整して冷却水出口温度をほぼ定
格値に保ちつつ熱収支をバランスさせる働き(作用)を
もっているので、吸収器内に散布される吸収液の温度が
低下し過ぎて吸収液の結晶や冷水の凍結を生じるおそれ
は少なく、50%負荷に見合う冷水を安全に取出すこと
が可能となる。逆に、冷却水入口温度が定格値より高い
場合には冷却水流量の減量度合を50%以下に調整して
冷却水出口温度をほぼ定格値に保ちつつ熱収支をバラン
スさせるので、凝縮器や発生器内の温度および圧力が過
度に上昇して保護装置が作動するようなことは少なく、
50%負荷に見合う冷水を安全に取出すことが可能とな
る。(e) Effect In the means according to the present invention, the load is, for example, 5 of the total load.
0% and the cooling water inlet temperature is lower than the rated value, the cooling water flow rate is not reduced by 50% as in conventional means, but the cooling water flow rate is reduced by more than 50%. It has the function of balancing the heat balance by adjusting the water flow rate and keeping the cooling water outlet temperature at approximately the rated value, so if the temperature of the absorption liquid sprayed inside the absorber drops too much, the absorption liquid crystallizes. There is little risk that the cold water will freeze, and it is possible to safely take out the cold water that corresponds to the 50% load. Conversely, if the cooling water inlet temperature is higher than the rated value, the degree of reduction in the cooling water flow rate is adjusted to 50% or less to maintain the cooling water outlet temperature at approximately the rated value and balance the heat balance. It is unlikely that the temperature and pressure inside the generator will rise excessively and activate the protective device.
It becomes possible to safely extract cold water corresponding to 50% load.
(へ)実施例
図面は本発明による吸収冷凍機の一実施例を示した概略
構成説明図であり、(1)は高温発生器、(2)は低温
発生器、(3)は凝縮器、(4)は蒸発器、(5)は吸
収器、(6)、(7)は高温、低温溶液熱交換器、(8
)は冷媒液用のポンプ、(9)は吸収液用のポンプで、
これら機器は冷媒の流れる管(イ)、α乃、冷媒液の流
下する管(6)、冷媒液の還流する管(至)、α転成収
液の送られる管(ト)、αG、吸収液の流れる管αη、
al19.吸収液の流下する管へ転輸により接続されて
従来の二。(v) Embodiment The drawings are schematic configuration explanatory diagrams showing one embodiment of the absorption refrigerator according to the present invention, in which (1) is a high temperature generator, (2) is a low temperature generator, (3) is a condenser, (4) is an evaporator, (5) is an absorber, (6) and (7) are high temperature and low temperature solution heat exchangers, (8
) is a pump for refrigerant liquid, (9) is a pump for absorption liquid,
These devices include a pipe through which the refrigerant flows (a), α-no, a pipe through which the refrigerant liquid flows (6), a pipe through which the refrigerant liquid flows back (to), a pipe through which the α-conversion product is sent (g), αG, an absorption liquid. The flowing pipe αη,
al19. The conventional two is connected by diversion to the pipe through which the absorption liquid flows.
型動用の吸収冷凍機と同様の冷媒〔水〕と吸収液〔臭化
リチウム水溶液〕の循環路を形成している。It forms a circulation path for refrigerant (water) and absorption liquid (lithium bromide aqueous solution) similar to that of a type-driving absorption refrigerator.
(財)は高温発生器(1)の燃焼加熱室、(イ)、翰・
・・は燃焼ガスの流れる管、翰は低温発生器(2)の加
熱器、(財)は凝縮器(3)の冷却器、(2)は蒸発器
(4)の熱交換器、(ハ)は吸収器(5)の冷却器であ
り、また、(財)は冷却塔、[F]は吐出量可変の冷却
水用ポンプである。(Foundation) is the combustion heating chamber of the high temperature generator (1), (A),
... is the pipe through which the combustion gas flows, the wire is the heater of the low temperature generator (2), (F) is the cooler of the condenser (3), (2) is the heat exchanger of the evaporator (4), and (H) is the cooler of the condenser (3). ) is a cooler for the absorber (5), (F) is a cooling tower, and [F] is a cooling water pump with variable discharge amount.
翰は冷却塔(ロ)入口側と冷却器(ハ)出口側とを接続
した管、□は冷却水用ポンプ■吸込み側と冷却塔(財)
出口側とを接続した管、(1)は冷却器(イ)入口側と
冷却水用ポンプ(2)吐出側とを接続した管、61)は
冷却器(ハ)入口側と冷却器切出口側とを接続した管で
ある。The wire is the pipe connecting the cooling tower (b) inlet side and the cooler (c) outlet side, □ is the cooling water pump ■Suction side and cooling tower (goods)
(1) is the pipe that connects the cooler (A) inlet side and the cooling water pump (2) discharge side, 61) is the pipe that connects the cooler (C) inlet side and the cooler cutout. This is the tube that connects the sides.
また、(2)、鏝は熱交換器(ハ)と負荷側の熱交換ユ
ニット〔図示せず〕とを接続した管であり、(ロ)は燃
焼加熱室91)への燃料供給管である。In addition, (2), the trowel is a pipe that connects the heat exchanger (c) and the heat exchange unit [not shown] on the load side, and (b) is a fuel supply pipe to the combustion heating chamber 91). .
■は燃料供給管−に備えた燃料制御弁で、この燃料制御
弁の開度が熱交換器(2)出口側の管(至)に備えた温
度検出器(Sl)の信号で制御器(0を介して制御され
ることにより、従来の吸収冷凍機と同様に高温発生器(
1)の加熱量が負荷に応じて調節されるよ5ICなって
いる。■ is a fuel control valve installed in the fuel supply pipe, and the opening degree of this fuel control valve is determined by the signal from the temperature sensor (Sl) installed in the pipe on the outlet side of the heat exchanger (2). 0, the high temperature generator (
The amount of heating in step 1) is adjusted to 5 IC according to the load.
° また、制御器(Qは温度検出器(S、 )の信号を
受けて冷却水用ポンプCP)の吐出量を調節するように
もなっており、かつ、制御器(0には、ポンプCP)吐
出側の冷却水温度〔吸収冷凍機入口側の冷却水温度(冷
却水入口温度)〕を感知する温度検出器(S7)の信号
によりポンプCP)吐出量の調節度合を補償して調整す
るマイクロプロセッサ−や補償回路などの内蔵されてい
る調整器(5)が備えである。° It also adjusts the discharge amount of the controller (Q is the cooling water pump CP in response to the signal from the temperature sensor (S, ), and the controller (0 is the pump CP). ) The degree of adjustment of the discharge amount of the pump CP is compensated and adjusted based on the signal from the temperature detector (S7) that detects the cooling water temperature on the discharge side [cooling water temperature on the absorption chiller inlet side (cooling water inlet temperature)]. A built-in regulator (5) such as a microprocessor and a compensation circuit is provided.
次に、このように構成された吸収冷凍機(以下、本機と
いう)における冷却水流量の制御動作の一例を従来の吸
収冷凍機(以下、従来機という)のそれと比較しつつ説
明する。Next, an example of the control operation of the cooling water flow rate in the absorption chiller configured as described above (hereinafter referred to as the present machine) will be explained while comparing it with that of a conventional absorption chiller (hereinafter referred to as the conventional machine).
ここにおいて、負荷Y〔%〕、冷却水出入口温度の定格
値なそれぞれT、c、 T□、[:℃) 、冷却水出入
口温度をそれぞれT。’rzc’c)、本機の調整善因
による補償率を2,100%負荷時の冷却水流量〔ポン
プ[F]吐出量〕に対するY%負荷時のそれの度合なX
〔%〕で表わすものとすれば、本機にあっては
X=Y −Z ・・・・・・
■Z=CToc−Tic)/(Toc−Ti) −
−■となるように設計されている。そして、本機におい
て&家
To=Tj+(Toc−Tic) ・(Y/X) −”
・■が成り立ち、一方、従来機においてはX=Yの関係
式とT。= Ti+ (Toc−Tic) の関係式
が成り立つ。Here, the load Y [%], the rated value of the cooling water inlet/outlet temperature are T, c, T□, [:℃), respectively, and the cooling water inlet/outlet temperature is T, respectively. 'rzc'c), the compensation rate due to the adjustment factor of this machine is 2,100% compared to the cooling water flow rate [pump [F] discharge rate] at Y% load.
If expressed in [%], for this machine, X = Y - Z...
■Z=CToc-Tic)/(Toc-Ti) -
−■ It is designed to be. Then, in this machine &To=Tj+(Toc-Tic)・(Y/X)-"
・■ holds; on the other hand, in the conventional machine, the relational expression of X=Y and T. The relational expression = Ti+ (Toc-Tic) holds true.
今、100%負荷時の冷却水流量が本機および従来機と
もに同じで、かつ、T、c、 Ticがそれぞれ37.
5°C132°Cに設計されているものとし、100%
負荷CY=1001と50%負荷〔Y=50〕でのそれ
ぞれのT、〔冷却水入口温度〕に対する本機と従来機に
おけるX〔冷却水流量の度合〕およびTi C冷却水出
口温度〕を前記の関係式より求めて比較したものが下記
の表である。Now, the cooling water flow rate at 100% load is the same for both this machine and the conventional machine, and T, c, and Tic are each 37.
5°C132°C, 100%
The X [degree of cooling water flow rate] and TiC cooling water outlet temperature] of this machine and the conventional machine with respect to T and [cooling water inlet temperature] at load CY = 1001 and 50% load [Y = 50] are shown above. The following table shows the results obtained from the relational expression and compared.
上記の表から明らかなように、従来機においてはT、〔
冷却水入口温度〕が変化するとT。〔冷却水出口温度〕
も変化するのに対し、本機においてはT。が定格値CT
oc”:Jに保たれることが分かる。As is clear from the table above, in the conventional machine, T, [
T when the cooling water inlet temperature changes. [Cooling water outlet temperature]
T also changes, whereas in this machine T. is the rated value CT
oc”: It can be seen that it is maintained at J.
それ故、本機においては、定格運転時とほぼ同様の運転
に保たれ、安全な運転を続けることができるのである。Therefore, this machine maintains almost the same operation as the rated operation, and can continue to operate safely.
なお、本機においては、負荷とは別に、冷却水出口温度
によりポンプ■の吐出量を制御することによって冷却水
出口温度を定格値に保つ手段(例えば実開昭59−57
765号公報)を採用することも可能である。尤も、冷
却水入口温度の変化を冷却水出口温度の変化で検知する
この手段においては、熱収支がバランスするまでは冷却
水入口温度の変化を正確に把握できないため、多数の負
荷側熱交換ユニットに1台の吸収冷凍機で冷水を供給す
るような場合には不向きである。In addition, in this machine, in addition to the load, there is a means to maintain the cooling water outlet temperature at the rated value by controlling the discharge amount of the pump ■ according to the cooling water outlet temperature (for example, the
It is also possible to adopt the method disclosed in Japanese Patent Publication No. 765. However, with this method of detecting changes in the cooling water inlet temperature by changes in the cooling water outlet temperature, changes in the cooling water inlet temperature cannot be accurately determined until the heat balance is balanced. This method is not suitable for cases where a single absorption refrigerator is used to supply cold water.
なおまた、図に示した実施例においては、吐出量可変の
冷却水用ポンプψ)を用いた場合について説明したが、
吐出量可変のポンプに代えて冷却水の循環路に制御弁を
備え、この制御弁の開度な制御するようにしても良いこ
とは勿論である。Furthermore, in the embodiment shown in the figure, a case was explained in which a cooling water pump ψ) with a variable discharge amount was used.
It goes without saying that a control valve may be provided in the cooling water circulation path in place of the variable discharge pump, and the opening degree of this control valve may be controlled.
(トフ 発明の効果
以上のように、本発明は、吸収冷凍機への冷却水流量の
調節度合を冷却水入口温度で補償しつつ負荷に応じてコ
ントロールするようにしたものであるから、冷却水出口
温度をほぼ一定に保ちつつ負荷に見合う冷水を安全かつ
速みやかに取出すことができるという効果を秦するもの
である。(Effects of the Invention As described above, the present invention is designed to control the degree of adjustment of the cooling water flow rate to the absorption chiller according to the load while compensating the degree of adjustment of the cooling water flow rate to the absorption chiller with the cooling water inlet temperature. This provides the effect of safely and quickly taking out cold water suitable for the load while keeping the outlet temperature almost constant.
図面は本発明による吸収冷凍機の一実施例を示した概略
構成説明図である。
(1)・・・高温発生器、 (2)・・・低温発生器、
(3)・・・凝縮器、 (4)・・・蒸発器、 (5
)・・・吸収器、 (ハ)・・・冷却器、 (イ)・・
・熱交換器、 (ホ)・・・冷却器、 (イ)・・・冷
却塔、 (ホ)、(至)、(1)、3υ、(2)、(至
)・・・管、(4)・・・調整器、 (0・・・制御器
、 (ト)・・・吐出量可変の冷却水用ポンプ、(S、
)、(S2)・・・温度検出器、 閏・・・燃料制御弁
。The drawing is a schematic structural explanatory diagram showing one embodiment of an absorption refrigerator according to the present invention. (1)...High temperature generator, (2)...Low temperature generator,
(3)... Condenser, (4)... Evaporator, (5
)...Absorber, (C)...Cooler, (B)...
・Heat exchanger, (E)...Cooler, (B)...Cooling tower, (E), (To), (1), 3υ, (2), (To)...Pipe, ( 4)...Regulator, (0...Controller, (g)...Variable discharge amount cooling water pump, (S,
), (S2)...Temperature detector, Leap...Fuel control valve.
Claims (1)
る機構を備えた吸収冷凍機において、ポンプにより機内
へ供給する冷却水の流量を負荷検出器の信号で調節する
制御機構が備えられ、かつ、この制御機構には冷却水流
量の調節の度合を機内への冷却水流入温度により補償す
る調整機構が備えられていることを特徴とした吸収冷凍
機。(1) An absorption chiller equipped with a mechanism that adjusts the heating amount of the generator based on the signal from the load detector, is equipped with a control mechanism that uses the signal from the load detector to adjust the flow rate of cooling water supplied into the machine by the pump. , and the control mechanism is equipped with an adjustment mechanism that compensates the degree of adjustment of the cooling water flow rate based on the temperature of the cooling water flowing into the machine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18017084A JPS6159166A (en) | 1984-08-29 | 1984-08-29 | Absorption refrigerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18017084A JPS6159166A (en) | 1984-08-29 | 1984-08-29 | Absorption refrigerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6159166A true JPS6159166A (en) | 1986-03-26 |
Family
ID=16078617
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18017084A Pending JPS6159166A (en) | 1984-08-29 | 1984-08-29 | Absorption refrigerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6159166A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0267868U (en) * | 1988-11-08 | 1990-05-23 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5589664A (en) * | 1978-12-26 | 1980-07-07 | Ebara Mfg | Liquid concentration control method of absorption refrigerating machine |
JPS5847971A (en) * | 1981-09-17 | 1983-03-19 | 三洋電機株式会社 | Absorption cold and hot water machine |
JPS6110471B2 (en) * | 1976-12-03 | 1986-03-29 | Nippon Sooda Kk |
-
1984
- 1984-08-29 JP JP18017084A patent/JPS6159166A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6110471B2 (en) * | 1976-12-03 | 1986-03-29 | Nippon Sooda Kk | |
JPS5589664A (en) * | 1978-12-26 | 1980-07-07 | Ebara Mfg | Liquid concentration control method of absorption refrigerating machine |
JPS5847971A (en) * | 1981-09-17 | 1983-03-19 | 三洋電機株式会社 | Absorption cold and hot water machine |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0267868U (en) * | 1988-11-08 | 1990-05-23 |
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