JPH0451320Y2 - - Google Patents
Info
- Publication number
- JPH0451320Y2 JPH0451320Y2 JP1984005762U JP576284U JPH0451320Y2 JP H0451320 Y2 JPH0451320 Y2 JP H0451320Y2 JP 1984005762 U JP1984005762 U JP 1984005762U JP 576284 U JP576284 U JP 576284U JP H0451320 Y2 JPH0451320 Y2 JP H0451320Y2
- Authority
- JP
- Japan
- Prior art keywords
- solution
- solution concentration
- heater
- absorption chiller
- pipe
- 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
- 239000003507 refrigerant Substances 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 13
- 238000010521 absorption reaction Methods 0.000 claims description 12
- 238000005057 refrigeration Methods 0.000 claims description 12
- 239000000498 cooling water Substances 0.000 claims description 5
- 239000000243 solution Substances 0.000 description 34
- 238000001514 detection method Methods 0.000 description 8
- 239000006096 absorbing agent Substances 0.000 description 4
- 238000007710 freezing Methods 0.000 description 4
- 230000008014 freezing Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910003002 lithium salt Inorganic materials 0.000 description 1
- 159000000002 lithium salts Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【考案の詳細な説明】
〔考案の利用分野〕
本考案は吸収冷温水機の溶液濃度調整装置に関
する。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a solution concentration adjusting device for an absorption chiller/heater.
第1図に水−リチウム塩素系の吸収冷温水機の
一般的な例を示す。この吸収冷温水機は溶液の濃
度を調整するための装置を備えており、本考案は
この溶液濃度調整装置の改良に係るものである。
FIG. 1 shows a general example of a water-lithium chlorine absorption chiller/heater. This absorption chiller/heater is equipped with a device for adjusting the concentration of the solution, and the present invention relates to an improvement of this solution concentration adjusting device.
まず、吸収冷温水機の概要を簡単に説明する。
蒸発器1により発生した冷媒蒸気Aは吸収器2に
おいて吸収剤(リチウム塩水溶液の濃溶液、以下
濃溶液という。)Bに吸収される。ここで冷媒を
吸収して濃度が低下した溶液(以下、稀溶液とい
う。)Cは、溶液循環ポンプ3により熱交換器4
を経て第1再生器5に送られる。高温再生器5に
おいてガスバーナ6により加熱された稀溶液Cは
配管7を通じて気液分離器8により高温冷媒蒸気
Dと中間濃溶液Eとに分離される。このうち高温
冷媒蒸気Dは低温再生器9に導びかれ、熱交換器
4を経て導入された中間濃度溶液Eを再び加熱す
る。この加熱によつて溶液Eの濃度がさらに高く
なるとともに中温蒸気Gが生じる。中温蒸気Gは
凝縮器10において液化される。この凝縮は配管
11に流れる冷却水Hにより行われる。液化され
た溶液Iは冷媒槽13を介して蒸発器1に入り、
冷凍作用に供される。一方、溶液Eは配管14を
介して熱交換器4に送られ、稀溶液Cに熱をうば
われたのち、配管15を介して吸収器2に送られ
濃溶液Bとして吸収作用を行う。以下、上述のサ
イクルをくり返して冷凍が行われる。 First, we will briefly explain the outline of absorption chiller/heater.
Refrigerant vapor A generated by the evaporator 1 is absorbed by an absorbent (concentrated solution of lithium salt aqueous solution, hereinafter referred to as concentrated solution) B in the absorber 2. Here, the solution C whose concentration has decreased by absorbing the refrigerant (hereinafter referred to as dilute solution) is transferred to the heat exchanger 4 by the solution circulation pump 3.
It is sent to the first regenerator 5 through the. A dilute solution C heated by a gas burner 6 in the high-temperature regenerator 5 is separated into a high-temperature refrigerant vapor D and an intermediate concentrated solution E by a gas-liquid separator 8 through a pipe 7. Among them, the high-temperature refrigerant vapor D is led to the low-temperature regenerator 9 and heats the intermediate concentration solution E introduced through the heat exchanger 4 again. This heating further increases the concentration of solution E and generates intermediate temperature steam G. The intermediate temperature steam G is liquefied in the condenser 10. This condensation is performed by the cooling water H flowing through the pipe 11. The liquefied solution I enters the evaporator 1 via the refrigerant tank 13,
Subjected to freezing action. On the other hand, the solution E is sent to the heat exchanger 4 via the pipe 14, and after its heat is transferred to the dilute solution C, it is sent to the absorber 2 via the pipe 15, where it acts as a concentrated solution B. Thereafter, freezing is performed by repeating the above-mentioned cycle.
次に、濃度調整装置について説明する。冷媒槽
13から蒸発器1の圧力を検出するための配管
(以下、第1圧力検出配管という。)16が溶液濃
度調整室17の上部に配設され、凝縮器10から
凝縮器10の圧力を検出するための配管(以下、
第2圧力検出配管という。)18が溶液濃度調整
室17の底部に配設されている。すなわち、この
溶液濃度調整装置は、冷却水入口温度上昇に伴
い、凝縮器10と蒸発器1間の圧力差に応じて、
蒸発器1への液冷媒の供給を漸次減少し、溶液濃
度調整室17内の液冷媒の貯蔵を増加すると共
に、吸収器2内の溶液濃度を濃くして冷凍能力を
確保し、また冷却水入口温度の低下に伴い蒸発器
1への液冷媒の供給を漸次増加し、吸収器2内の
溶液濃度を薄くして溶液の晶析及び冷媒の凍結を
防止する。 Next, the density adjustment device will be explained. A pipe (hereinafter referred to as first pressure detection pipe) 16 for detecting the pressure of the evaporator 1 from the refrigerant tank 13 is disposed in the upper part of the solution concentration adjustment chamber 17, and is used to detect the pressure of the condenser 10 from the condenser 10. Piping for detection (hereinafter referred to as
This is called the second pressure detection pipe. ) 18 is arranged at the bottom of the solution concentration adjustment chamber 17. That is, this solution concentration adjustment device adjusts the pressure difference between the condenser 10 and the evaporator 1 as the cooling water inlet temperature increases.
The supply of liquid refrigerant to the evaporator 1 is gradually reduced to increase the storage of liquid refrigerant in the solution concentration adjustment chamber 17, and the concentration of the solution in the absorber 2 is increased to ensure the refrigerating capacity. As the inlet temperature decreases, the supply of liquid refrigerant to the evaporator 1 is gradually increased to dilute the concentration of the solution in the absorber 2 to prevent crystallization of the solution and freezing of the refrigerant.
しかし、上記従来の溶液濃度調整装置において
は、吸収冷温水機の運転を停止したとき、今まで
貯蔵していた液冷媒を機内に放出し、再運転時に
は最適溶液濃度になるように再度液冷媒を貯蔵す
る必要がある。 However, in the above-mentioned conventional solution concentration adjustment device, when the operation of the absorption chiller/heater is stopped, the liquid refrigerant that has been stored is released into the machine, and when restarting the machine, the liquid refrigerant is reused to reach the optimum solution concentration. need to be stored.
そのため、冷房停止ごとに貯蔵液冷媒を放出す
るもののこの放出冷媒は何ら冷凍能力に寄与する
ものではなく無効冷媒であるから冷凍成績係数が
悪化する。また、再運転時においては溶液が過剰
に稀釈されているため、運転の立上り時間が長く
なるという問題がある。 Therefore, although the stored liquid refrigerant is discharged every time the cooling is stopped, this discharged refrigerant does not contribute to the refrigeration capacity at all and is an ineffective refrigerant, which deteriorates the refrigeration coefficient of performance. Furthermore, since the solution is excessively diluted when restarting the operation, there is a problem that the start-up time of the operation becomes longer.
本考案は、冷凍運転時における無効冷媒をなく
し、かつ再運転時における運転立上り時間を短縮
しうる溶液濃度調整装置を提供することを目的と
する。
SUMMARY OF THE INVENTION An object of the present invention is to provide a solution concentration adjusting device that can eliminate ineffective refrigerant during refrigeration operation and shorten the start-up time during restart.
上記目的を達成するために、本発明による溶液
濃度調整装置は、冷凍運転停止時に凝縮器と溶液
濃度調整室間の第2圧力検出配管を閉じ、再運転
時には吸収冷温水機の動作が安定する時間だけ遅
延して前記第2圧力検出配管を開くよう制御され
る弁を設けた点に特徴を有する。
In order to achieve the above object, the solution concentration adjustment device according to the present invention closes the second pressure detection pipe between the condenser and the solution concentration adjustment chamber when refrigeration operation is stopped, and stabilizes the operation of the absorption chiller/heater when restarting operation. The present invention is characterized in that a valve is provided that is controlled to open the second pressure detection pipe with a time delay.
かかる構成によれば、冷凍運転停止時に弁を閉
じるので無効冷媒の放出は阻止され、また、再運
転時に冷温水機の安定化を待つて弁を開くので溶
液濃度を最適状態に保つことができ、したがつて
運転立上り時間を短縮できる。 According to this configuration, since the valve is closed when the refrigeration operation is stopped, release of ineffective refrigerant is prevented, and when the refrigeration operation is restarted, the valve is opened after waiting for the water chiller/heater to stabilize, so that the solution concentration can be maintained at an optimum state. Therefore, the start-up time can be shortened.
以下、本考案による溶液濃度調整装置の実施例
を図面に基づいて説明する。
Embodiments of the solution concentration adjusting device according to the present invention will be described below with reference to the drawings.
第2図に本考案の実施例を示す。この第2図に
おいて第1図と同一の部分には同一の符号を附し
てその説明を省略する。 FIG. 2 shows an embodiment of the present invention. In FIG. 2, the same parts as in FIG. 1 are given the same reference numerals, and their explanation will be omitted.
第2図において、第1図と異なる主な点、すな
わち本考案に係る点は第2圧力検出配管18に電
磁弁19が設けられている点である。この電磁弁
19は次のように開閉制御される(第3図参照)。
通常の吸収冷温水機の冷凍運転時Tdには電磁弁
19を開いておく。そうすることにより濃度調整
室17内には冷却水Hの温度に見合う液冷媒Iが
貯蔵される。次に、冷凍運転停止時Tsにおいて
は電磁弁19を運転停止と同時に閉じる。する
と、濃度調整室内17には停止時の液冷媒Iが貯
蔵されたままとなり、無効冷媒の放出は阻止され
る。次に、再運転を開始する際には電磁弁19を
一定時間△t後に開く。一定時間△tとは吸収冷
温水機の動作が安定状態になるまでの時間のこと
である。この遅延時間の設定は、例えば冷凍機の
操作盤(図示せず)の制御回路に設けられたタイ
マ20により行なえばよい。このように安定状態
に入つてから電磁弁19を開くので液冷媒Iが不
必要に薄められることがなく、したがつて運転立
上り時間が短かくなつて冷凍成績係数が向上す
る。 The main difference in FIG. 2 from FIG. 1, that is, the point related to the present invention, is that a solenoid valve 19 is provided in the second pressure detection pipe 18. This solenoid valve 19 is controlled to open and close as follows (see FIG. 3).
The solenoid valve 19 is kept open at Td during normal refrigeration operation of the absorption chiller/heater. By doing so, liquid refrigerant I matching the temperature of the cooling water H is stored in the concentration adjustment chamber 17. Next, at Ts when the refrigeration operation is stopped, the solenoid valve 19 is closed at the same time as the refrigeration operation is stopped. Then, the liquid refrigerant I at the time of stop remains stored in the concentration adjustment chamber 17, and discharge of the ineffective refrigerant is prevented. Next, when restarting the operation, the solenoid valve 19 is opened after a certain period of time Δt. The fixed time Δt is the time required for the operation of the absorption chiller/heater to reach a stable state. This delay time may be set, for example, by a timer 20 provided in a control circuit of an operation panel (not shown) of the refrigerator. Since the electromagnetic valve 19 is opened after entering a stable state in this manner, the liquid refrigerant I is not diluted unnecessarily, and therefore the operation start-up time is shortened and the refrigeration coefficient of performance is improved.
以上の制御は図示しない操作盤の制御回路によ
りシーケンシヤルに行なわれる。 The above control is performed sequentially by a control circuit of an operation panel (not shown).
なお、本実施例では弁として電磁弁を用いた
が、その他のON−OFF制御できる弁であれば使
用可能であり、この態様に限られない。 In this embodiment, a solenoid valve is used as the valve, but any other valve that can be controlled ON-OFF can be used, and the present invention is not limited to this embodiment.
以上述べた如く、第2圧力検出配管に弁を設
け、冷凍運転停止時に上記配管路を閉じて溶液濃
度調整室内の貯蔵冷媒の放出を阻止することによ
り無効冷媒の放出を防止し、かつ再運転時におい
て冷凍機の動作が安定するまでの時間だけ遅延さ
せてから前記弁を開くようにしたので液冷媒の濃
度を高くして運転開始することができ運転立上り
時間を早くすることが可能となる。このような構
成により成績係数の向上が望めることとなる。
As described above, by providing a valve in the second pressure detection pipe and closing the pipe line to prevent the release of the stored refrigerant in the solution concentration adjustment chamber when the refrigeration operation is stopped, the release of the ineffective refrigerant is prevented, and the refrigerating operation is resumed. Since the valve is opened after a delay until the operation of the refrigerator becomes stable, the operation can be started with a high concentration of liquid refrigerant, and the operation start-up time can be shortened. . With such a configuration, an improvement in the coefficient of performance can be expected.
第1図は従来一般の吸収冷温水機の例を示す配
管図、第2図は本考案による溶液濃度調整装置の
一実施例を示す配管図、第3図は本考案における
弁動作の説明図である。
1……蒸発器、10……凝縮器、17……溶液
濃度調整室、18……第2圧力検出配管、19…
…電磁弁、20……タイマ、H……冷却水、I…
…液冷媒、Ts……冷凍運転停止時、Tr……再運
転開始時、△t……遅延時間。
Fig. 1 is a piping diagram showing an example of a conventional absorption chiller/heater, Fig. 2 is a piping diagram showing an example of the solution concentration adjusting device according to the present invention, and Fig. 3 is an explanatory diagram of valve operation in the present invention. It is. DESCRIPTION OF SYMBOLS 1... Evaporator, 10... Condenser, 17... Solution concentration adjustment chamber, 18... Second pressure detection piping, 19...
...Solenoid valve, 20...Timer, H...Cooling water, I...
...Liquid refrigerant, Ts...When freezing operation is stopped, Tr...When restarting operation, △t...Delay time.
Claims (1)
蒸発器間の圧力差に応じて溶液濃度調整室内の液
冷媒貯蔵量を増加する吸収冷温水機の溶液濃度調
整装置において、 冷凍運転停止時に前記凝縮器と溶液濃度調整室
間に配された管路を閉じ、再運転開始時に当該吸
収冷温水機が安定化する時間だけ遅延して前記管
路を開く弁を前記管路に設けたことを特徴とする
吸収冷温水機の溶液濃度調整装置。[Claim for Utility Model Registration] Solution concentration adjustment in an absorption chiller/heater that increases the amount of liquid refrigerant stored in the solution concentration adjustment chamber in response to the pressure difference between the condenser and evaporator caused by an increase in cooling water inlet temperature. In the apparatus, when the refrigeration operation is stopped, a pipe arranged between the condenser and the solution concentration adjustment chamber is closed, and when the refrigerating operation is started, a valve is opened to open the pipe after a delay of time for the absorption chiller/heater to stabilize. A solution concentration adjusting device for an absorption chiller/heater, characterized in that it is provided in the pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP576284U JPS60118460U (en) | 1984-01-19 | 1984-01-19 | Solution concentration adjustment device for absorption chiller/heater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP576284U JPS60118460U (en) | 1984-01-19 | 1984-01-19 | Solution concentration adjustment device for absorption chiller/heater |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60118460U JPS60118460U (en) | 1985-08-10 |
JPH0451320Y2 true JPH0451320Y2 (en) | 1992-12-03 |
Family
ID=30482567
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP576284U Granted JPS60118460U (en) | 1984-01-19 | 1984-01-19 | Solution concentration adjustment device for absorption chiller/heater |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60118460U (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5717264U (en) * | 1980-06-25 | 1982-01-28 | ||
JPS582568B2 (en) * | 1979-01-25 | 1983-01-17 | トヨタ自動車株式会社 | Heat treatment distortion correction method and device |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS582568U (en) * | 1981-06-29 | 1983-01-08 | 矢崎総業株式会社 | Water-lithium salt double effect absorption refrigerator |
-
1984
- 1984-01-19 JP JP576284U patent/JPS60118460U/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS582568B2 (en) * | 1979-01-25 | 1983-01-17 | トヨタ自動車株式会社 | Heat treatment distortion correction method and device |
JPS5717264U (en) * | 1980-06-25 | 1982-01-28 |
Also Published As
Publication number | Publication date |
---|---|
JPS60118460U (en) | 1985-08-10 |
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