JPH0447227B2 - - Google Patents

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Publication number
JPH0447227B2
JPH0447227B2 JP625586A JP625586A JPH0447227B2 JP H0447227 B2 JPH0447227 B2 JP H0447227B2 JP 625586 A JP625586 A JP 625586A JP 625586 A JP625586 A JP 625586A JP H0447227 B2 JPH0447227 B2 JP H0447227B2
Authority
JP
Japan
Prior art keywords
temperature
cooling water
solution
path
absorber
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
Application number
JP625586A
Other languages
Japanese (ja)
Other versions
JPS62166273A (en
Inventor
Takashi Aoyama
Masakazu Fujimoto
Takashi Yasuda
Osayuki Inoe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Original Assignee
Ebara Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP625586A priority Critical patent/JPS62166273A/en
Publication of JPS62166273A publication Critical patent/JPS62166273A/en
Publication of JPH0447227B2 publication Critical patent/JPH0447227B2/ja
Granted legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、運転停止時の操作を行なう制御装置
を有する二重効用吸収冷凍機に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a dual-effect absorption refrigerator having a control device for operating during shutdown.

〔従来の技術〕[Conventional technology]

従来の吸収冷凍機においては、運転停止時に、
溶液の結晶化を防止するために、発生器加熱源の
制御弁を閉じて冷凍機の運転を停止した後も溶液
ポンプは運転を続け、溶液経路中の濃度を均一化
する希釈運転を行なつた後溶液ポンプを停止して
いるのであるが、冷却水ポンプも溶液ポンプと共
に運転を続け、溶液ポンプの停止と共に停止する
ようになつていた。
In conventional absorption chillers, when the operation is stopped,
To prevent solution crystallization, the solution pump continues to operate even after the control valve of the generator heating source is closed and the refrigerator operation is stopped, performing dilution operation to equalize the concentration in the solution path. However, the cooling water pump continued to operate along with the solution pump, and stopped when the solution pump stopped.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところが、通常は溶液ポンプの出力(例えば1
〜2kw)に比べ冷却水ポンプの出力は大きく(例
えば6〜10kw)、冷却水ポンプを必要以上に運転
するために動力の損失を招いた。
However, usually the output of the solution pump (for example, 1
The output of the cooling water pump was large (for example, 6 to 10 kW) compared to the 2 kW, and operating the cooling water pump more than necessary resulted in a loss of power.

また、冷却水の通水を必要以上に行なうと、高
温発生器の内圧が低下して溶液の循環が行なわれ
にくくなり、濃度の均一化が十分なされず結晶を
招くおそれがあつた。
In addition, if the cooling water is passed more than necessary, the internal pressure of the high temperature generator decreases, making it difficult to circulate the solution, and there is a risk that the concentration will not be sufficiently uniform, leading to crystal formation.

このような支障を避けるために、冷凍機の停止
時に冷却水ポンプを直ちに停止すると冷却されな
い高温のままのスプレー溶液が降りかかり、冷却
水チユーブ内の冷却水の温度が上がり、チユーブ
の熱膨張に基づく過大応力によりチユーブが損傷
したり再起動の際に、冷却塔内のプラスチツクの
充填材を損傷する、という支障を招いた。
To avoid such problems, if you stop the cooling water pump immediately when the refrigerator stops, the uncooled spray solution that remains at a high temperature will fall, increasing the temperature of the cooling water in the cooling water tube, and causing The excessive stress caused problems such as tube damage and damage to the plastic filling in the cooling tower during restart.

本発明は従来のものの上記の如き問題点を解決
し、動力の損失を軽減し、溶液の希釈を促進し、
熱応力によるチユーブの損傷を防ぎ、かつ再起動
時に冷却塔内の充填材を損傷することのない二重
効用吸収冷凍機を提供することを目的とするもの
である。
The present invention solves the above-mentioned problems of the conventional ones, reduces power loss, promotes solution dilution,
It is an object of the present invention to provide a dual-effect absorption refrigerating machine that prevents damage to the tubes due to thermal stress and does not damage the filling material in the cooling tower when restarted.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上記の問題点を解決するための手段
として蒸発器、吸収器、高温発生器、低温発生
器、凝縮器、これらの機器を接続する溶液経路、
冷媒経路、これらの経路に設けられた溶液ポン
プ、冷媒ポンプ、前記吸収器及び凝縮器に通じて
いる冷却水経路、該冷却水経路に設けられた冷却
水ポンプ、前記蒸発器に通じている冷水経路、該
冷水経路に設けられた冷水ポンプを備えている二
重効用吸収冷凍機において、 前記冷却水経路の冷却水温度を直接又は間接的
に検出する冷却水温度検出器と、 該冷却水温度検出器により検出した冷却水温度
又は冷却水温度相当値が、前記吸収冷凍機の運転
停止後に、所定の設定値以下となつたときにその
信号を受けて前記冷却水ポンプを停止せしめる停
止信号を発する制御装置と、を備えたことを特徴
とする二重効用吸収冷凍機を提供せんとするもの
である。
The present invention provides an evaporator, an absorber, a high-temperature generator, a low-temperature generator, a condenser, a solution path connecting these devices as a means for solving the above problems,
A refrigerant path, a solution pump provided in these paths, a refrigerant pump, a cooling water path communicating with the absorber and the condenser, a cooling water pump provided in the cooling water path, and a cold water communicating with the evaporator. A dual-effect absorption chiller including a cooling water path and a chilled water pump provided in the chilled water path, comprising: a cooling water temperature detector that directly or indirectly detects the temperature of the cooling water in the cooling water path; When the cooling water temperature or the equivalent value of the cooling water temperature detected by the detector becomes equal to or less than a predetermined set value after the operation of the absorption chiller is stopped, a stop signal is generated to stop the cooling water pump in response to the signal. It is an object of the present invention to provide a dual-effect absorption refrigerating machine characterized by being equipped with a control device for generating heat.

〔作用〕[Effect]

本発明により、吸収冷凍機停止時に、冷却水ポ
ンプを直ちに停止するのではなくしばらく運転を
続行せしめることにより、冷却水の循環が引続き
行なわれる。溶液ポンプは希釈運転のため引続き
運転され、溶液を循環が行なわれているが、発生
器での加熱は既に停止されているので冷却水によ
り冷却されて溶液温度は次第に低下し、冷却水温
度も次第に低下する。
According to the present invention, when the absorption refrigerating machine is stopped, the cooling water pump is not stopped immediately but is allowed to continue operating for a while, so that the cooling water continues to be circulated. The solution pump continues to operate for dilution, and the solution is being circulated, but since heating in the generator has already been stopped, the solution temperature gradually decreases as it is cooled by the cooling water, and the cooling water temperature also decreases. It gradually decreases.

冷却塔に用いられる充填材には、例えば硬質塩
化ビニール(PVC)などが用いられ、それらの
実用的な耐熱限度はおよそ60〜80℃程度である。
本発明は、冷凍機の停止後、低下してゆく凝縮出
口における冷却水温度を検出し、用いられている
材料の耐熱限度以下の、所定の、例えば20〜30℃
の範囲内の設定値以下に低下したとき、この信号
を制御装置が受けて停止信号を発し冷却水ポンプ
を停止せしめるようにしたので、20〜30℃程度に
低下した冷却水に冷却チユーブにおいて比較的高
温の溶液がスプレーされてもそれ程高温にはなら
ず、その上溶液自体もかなり温度が下降している
ので、冷却水温度が上記の耐熱限度にまで上昇す
ることはない。従つてその後冷凍機を再起動して
も冷却塔には十分低温となつた冷却水が送られる
ので充填材を損傷することがない。また、冷却水
チユーブは60℃程度までは考慮されて設計されて
いるので、熱応力による損傷を招くことはない。
しかも冷却水ポンプを必要以上に長く運転して動
力の損失を招いたり、高温発生器内圧力を低下さ
せ過ぎて希釈運転に支障を来すこともない。
The filling material used in cooling towers is, for example, hard vinyl chloride (PVC), and its practical heat resistance limit is approximately 60 to 80°C.
The present invention detects the decreasing cooling water temperature at the condensing outlet after the refrigerator is stopped, and sets it to a predetermined value, for example, 20 to 30°C, which is below the heat resistance limit of the material used.
When the temperature drops below the set value within the range, the control device receives this signal and issues a stop signal to stop the cooling water pump. Even if a solution at an extremely high temperature is sprayed, the temperature does not reach that high, and the temperature of the solution itself has dropped considerably, so the temperature of the cooling water will not rise to the above-mentioned heat resistance limit. Therefore, even if the refrigerator is restarted after that, the cooling water that has reached a sufficiently low temperature is sent to the cooling tower, so that the filling material will not be damaged. In addition, the cooling water tube is designed with temperatures up to about 60°C in mind, so it will not be damaged by thermal stress.
Furthermore, there is no need to operate the cooling water pump for an unnecessarily long period of time, resulting in loss of power, or to reduce the internal pressure of the high-temperature generator too much, thereby interfering with the dilution operation.

なお、冷却水の温度の検出点は、凝縮器出口に
おいて検出すれば負荷の状態も全部含んだ結果を
把握することになるので最も好ましいが、吸収器
の入口において検出してもよい。
Note that it is most preferable to detect the temperature of the cooling water at the outlet of the condenser because the result including all the load conditions can be detected, but it may also be detected at the inlet of the absorber.

また、冷却水温度検出として、冷却水自体の温
度を直接検出する代りに、冷却水温度に関連する
ものの温度を冷却水温度相当値として間接的に検
出し、冷却水温度の許容値に相当する設定値以下
になつたときに制御装置から冷却水ポンプの停止
信号を発するようにしてもよい。
In addition, instead of directly detecting the temperature of the cooling water itself, the temperature of something related to the cooling water temperature is indirectly detected as a cooling water temperature equivalent value, which corresponds to the allowable value of the cooling water temperature. The control device may issue a stop signal for the cooling water pump when the temperature falls below a set value.

例えば高温発生器からの戻り経路の溶液の温度
は冷却水温度に深い関係を有するので、吸収器に
戻る入口における溶液温度、発生器を出たところ
の溶液温度などを検出するようにしてもよい。設
定温度としては、吸収器入口温度に対しては30〜
40℃程度の温度、発生器出口温度に対しては110
〜130℃程度の温度が選ばれる。
For example, since the temperature of the solution in the return path from the high-temperature generator has a close relationship with the temperature of the cooling water, the solution temperature at the inlet returning to the absorber, the solution temperature at the exit from the generator, etc. may be detected. . The set temperature is 30~30 for the absorber inlet temperature.
110 for a temperature around 40℃, generator outlet temperature
A temperature of ~130°C is selected.

そのほか、冷却水が通過する熱交換器としての
吸収器内又は凝縮器内の温度も冷却水温度との関
連が深いので吸収器内の溶液温度、冷媒蒸気温
度、凝縮器内の冷媒蒸気温度、冷媒液温度を検出
するようにしてもよい。設定温度としては吸収器
内温度に対しては25〜30℃程度、凝縮器内温度に
対しては25〜30℃程度の温度が選ばれる。
In addition, the temperature inside the absorber or condenser as a heat exchanger through which the cooling water passes is also closely related to the temperature of the cooling water, so the temperature of the solution inside the absorber, the refrigerant vapor temperature, the refrigerant vapor temperature inside the condenser, The refrigerant liquid temperature may also be detected. As the set temperature, a temperature of about 25 to 30°C is selected for the temperature inside the absorber, and a temperature of about 25 to 30°C is selected for the temperature inside the condenser.

〔実施例〕〔Example〕

本発明の実施例につき図面を用いて説明する。 Embodiments of the present invention will be described with reference to the drawings.

第1図においてAは吸収器、Eは蒸発器、GH
は高温発生器、GLは低温発生器、Cは凝縮器、
XHは高温溶液熱交換器、XLは低温溶液熱交換
器、SPは溶液ポンプ、RPは冷媒ポンプ、Vは減
圧弁である。
In Figure 1, A is an absorber, E is an evaporator, and GH
is a high temperature generator, GL is a low temperature generator, C is a condenser,
XH is a high temperature solution heat exchanger, XL is a low temperature solution heat exchanger, SP is a solution pump, RP is a refrigerant pump, and V is a pressure reducing valve.

これらの機器の間を溶液経路3,4,5、冷媒
経路6,7,8が接続され、吸収溶液及び冷媒が
循環されている。
Solution paths 3, 4, and 5 and refrigerant paths 6, 7, and 8 are connected between these devices, and the absorption solution and refrigerant are circulated.

1は蒸気などの加熱源流体が流れる加熱源経路
であり、流量制御弁2により加熱源流体の流量を
制御して吸収冷凍機の容量を制御するようになつ
ている。
Reference numeral 1 denotes a heat source path through which a heat source fluid such as steam flows, and a flow rate control valve 2 controls the flow rate of the heat source fluid to control the capacity of the absorption refrigerator.

9は冷水経路であり、負荷10と蒸発器Eとの
間に冷水ポンプ11により冷水を循環するように
なつている。
Reference numeral 9 denotes a cold water path, in which cold water is circulated between the load 10 and the evaporator E by a cold water pump 11.

12は冷却水経路であり、冷却水が冷却水ポン
プ13により冷却塔14、吸収器A、凝縮器Cを
循環するようになつている。
12 is a cooling water path, in which cooling water is circulated through a cooling tower 14, an absorber A, and a condenser C by a cooling water pump 13.

15は容量制御装置であり、冷水出口温度を検
出する温度検出器16からの冷水温度信号を受
け、冷水温度が一定になるように流量制御弁2を
操作するようになつている。
Reference numeral 15 denotes a capacity control device which receives a cold water temperature signal from a temperature detector 16 that detects the cold water outlet temperature and operates the flow rate control valve 2 so that the cold water temperature is constant.

17は凝縮器Cの出口における冷却水温度を検
出する温度検出器であり、その検出温度が所定の
設定値以下になると、その信号を受けた制御装置
18が停止信号を発して冷却水ポンプ13を停止
するようになつている。
Reference numeral 17 denotes a temperature detector that detects the temperature of the cooling water at the outlet of the condenser C, and when the detected temperature falls below a predetermined set value, the control device 18 that receives the signal issues a stop signal to stop the cooling water pump 13. It's starting to stop.

冷却水の出口温度を検出する代りに、冷却水の
入口温度を検出する温度検出器19を用いてもよ
い。また、冷却水温度に関連の深い、戻り溶液の
温度として、吸収器Aの入口溶液温度を検出する
温度検出器20、或いは高温発生器GHの出口溶
液温度を検出する温度検出器21を用いてもよ
い。そのほか、冷却水温度に関連の深い吸収器A
内温度、或いは凝縮器C内温度を検出してもよ
い。
Instead of detecting the coolant outlet temperature, a temperature detector 19 that detects the coolant inlet temperature may be used. In addition, as the temperature of the returned solution, which is closely related to the cooling water temperature, a temperature detector 20 that detects the inlet solution temperature of the absorber A or a temperature detector 21 that detects the outlet solution temperature of the high temperature generator GH is used. Good too. In addition, absorber A, which is closely related to cooling water temperature,
The internal temperature or the internal temperature of the condenser C may be detected.

以上のうち、冷却水の温度を直接的に検出せ
ず、冷却水温度に関連するものの温度で間接的に
冷却水温度を検出する場合には、設定値として、
冷却水の許容限界の温度に相当する温度を設定値
とする。
Among the above, when the temperature of the cooling water is not detected directly but is detected indirectly using the temperature of something related to the temperature of the cooling water, the set value is as follows:
The temperature corresponding to the allowable temperature limit of the cooling water is set as the set value.

冷却水温度を間接的に検出する例として高温発
生器GHの出口温度を温度検出器21で検出する
場合の、冷凍機停止時のフローチヤートの例を第
2図に示す。設定値を120℃とした例を示す。
FIG. 2 shows an example of a flowchart when the refrigerator is stopped when the temperature detector 21 detects the outlet temperature of the high temperature generator GH as an example of indirectly detecting the cooling water temperature. An example is shown in which the set value is 120℃.

〔発明の効果〕〔Effect of the invention〕

本発明により、吸収冷凍機の運転停止に当た
り、無駄な動力の損失を防ぐと共に、溶液の希釈
を促進し、熱応力による吸収器の冷却水チユーブ
の損傷を防ぎ、かつ再起動に当たり冷却塔の充填
材の損傷を招くおそれのない二重効用冷凍機を提
供することができ、実用上極めて大なる効果を奏
する。
The present invention prevents wasteful power loss when shutting down an absorption chiller, promotes solution dilution, prevents damage to the cooling water tube of the absorber due to thermal stress, and fills the cooling tower when restarting. It is possible to provide a dual-effect refrigerator that does not cause damage to materials, which is extremely effective in practice.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の実施例のフロー図、第2図は
そのフローチヤートである。 1……加熱源経路、2……流量制御弁、3……
溶液経路、4……溶液経路、5……溶液経路、6
……冷媒経路、7……冷媒経路、8……冷媒経
路、9……冷水経路、10……負荷、11……冷
水ポンプ、12……冷却水経路、13……冷却水
ポンプ、14……冷却塔、15……容量制御装
置、16……温度検出器、17……温度検出器、
18……制御装置、19……温度検出器、20…
…温度検出器、21……温度検出器、A……吸収
器、E……蒸発器、GH……高温発生器、GL…
…低温発生器、C……凝縮器、XH……高温熱交
換器、XL……低温熱交換器、SP……溶液ポン
プ、RP……冷媒ポンプ、V……減圧弁。
FIG. 1 is a flowchart of an embodiment of the present invention, and FIG. 2 is a flowchart thereof. 1... Heat source path, 2... Flow rate control valve, 3...
Solution route, 4... Solution route, 5... Solution route, 6
... Refrigerant route, 7... Refrigerant route, 8... Refrigerant route, 9... Chilled water route, 10... Load, 11... Chilled water pump, 12... Cooling water route, 13... Cooling water pump, 14... ...Cooling tower, 15...Capacity control device, 16...Temperature detector, 17...Temperature detector,
18...control device, 19...temperature detector, 20...
...Temperature detector, 21...Temperature detector, A...Absorber, E...Evaporator, GH...High temperature generator, GL...
...Low temperature generator, C...Condenser, XH...High temperature heat exchanger, XL...Low temperature heat exchanger, SP...Solution pump, RP...Refrigerant pump, V...Pressure reducing valve.

Claims (1)

【特許請求の範囲】 1 蒸発器、吸収器、高温発生器、低温発生器、
凝縮器、これらの機器を接続する溶液経路、冷媒
経路、これらの経路に設けられた溶液ポンプ、冷
媒ポンプ、前記吸収器及び凝縮器に通じている冷
却水経路、該冷却水経路に設けられた冷却水ポン
プ、前記蒸発器に通じている冷水経路、該冷水経
路に設けられた冷水ポンプを備えている二重効用
吸収冷凍機において、 前記冷却水経路の冷却水温度を直接的又は間接
的に検出する冷却水温度検出器と、 該冷却水温度検出器により検出した冷却水温度
又は冷却水温度相当値が、前記吸収冷凍機の運転
停止後に、所定の設定値以下となつたときにその
信号を受けて前記冷却水ポンプを停止せしめる停
止信号を発する制御装置と、 を備えたことを特徴とする二重効用吸収冷凍機。 2 前記冷却水温度の間接的な検出が、前記高温
発生器又は低温発生器の出口から前記吸収器に至
る溶液戻り経路内又は前記吸収器内の溶液の温度
を検出することにより行なわれる特許請求の範囲
第1項記載の冷凍機。
[Claims] 1. Evaporator, absorber, high temperature generator, low temperature generator,
A condenser, a solution path connecting these devices, a refrigerant path, a solution pump provided in these paths, a refrigerant pump, a cooling water path leading to the absorber and the condenser, and a cooling water path provided in the cooling water path. In a dual-effect absorption refrigerator comprising a cooling water pump, a cold water path leading to the evaporator, and a cold water pump installed in the cold water path, the temperature of the cooling water in the cooling water path is directly or indirectly controlled. A cooling water temperature detector to detect, and a signal when the cooling water temperature or the equivalent value of the cooling water temperature detected by the cooling water temperature detector becomes less than a predetermined set value after the absorption chiller stops operating. and a control device that issues a stop signal to stop the cooling water pump in response to the above. 2. A patent claim in which the temperature of the cooling water is indirectly detected by detecting the temperature of the solution in the solution return path from the outlet of the high-temperature generator or the low-temperature generator to the absorber or in the absorber. The refrigerator according to item 1.
JP625586A 1986-01-17 1986-01-17 Double-effect absorption refrigerator Granted JPS62166273A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP625586A JPS62166273A (en) 1986-01-17 1986-01-17 Double-effect absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP625586A JPS62166273A (en) 1986-01-17 1986-01-17 Double-effect absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS62166273A JPS62166273A (en) 1987-07-22
JPH0447227B2 true JPH0447227B2 (en) 1992-08-03

Family

ID=11633373

Family Applications (1)

Application Number Title Priority Date Filing Date
JP625586A Granted JPS62166273A (en) 1986-01-17 1986-01-17 Double-effect absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS62166273A (en)

Also Published As

Publication number Publication date
JPS62166273A (en) 1987-07-22

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