JPS61235652A - Method of controlling absorption refrigerator - Google Patents

Method of controlling absorption refrigerator

Info

Publication number
JPS61235652A
JPS61235652A JP7348185A JP7348185A JPS61235652A JP S61235652 A JPS61235652 A JP S61235652A JP 7348185 A JP7348185 A JP 7348185A JP 7348185 A JP7348185 A JP 7348185A JP S61235652 A JPS61235652 A JP S61235652A
Authority
JP
Japan
Prior art keywords
temperature
solution
detected
predetermined value
value
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
Application number
JP7348185A
Other languages
Japanese (ja)
Inventor
田中 祥治
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 JP7348185A priority Critical patent/JPS61235652A/en
Publication of JPS61235652A publication Critical patent/JPS61235652A/en
Pending legal-status Critical Current

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  • 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】 〔産業上の利用分野〕 本発明は発生器の加熱量を調節して冷水温度を制御する
ようにした吸収冷凍機における制御方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a control method for an absorption chiller in which the temperature of chilled water is controlled by adjusting the heating amount of a generator.

〔従来の技術〕[Conventional technology]

一般に吸収冷凍機においては、冷水温度がほぼ一定値に
なるように発生器の加熱量を調節している。
Generally, in an absorption refrigerator, the amount of heating by the generator is adjusted so that the temperature of the chilled water is approximately constant.

冷凍機運転中に冷却塔の冷却ファンの故障或いは運転ミ
ス等により冷却水温度が」1昇すると吸収器の溶液温度
が上昇してこれが吸収作用に影響して溶液濃度を濃い方
向に移動させる。これを第1図で示せば、正常運転時に
は実線の如くであるものが、溶液濃度の上昇により破線
の方向に変化していき、最後には結晶線Kに近付き結晶
してしまう危険がある。
If the temperature of the cooling water rises by 1 due to a failure or operational error in the cooling fan of the cooling tower during operation of the refrigerator, the temperature of the solution in the absorber increases, which affects the absorption action and shifts the concentration of the solution toward higher concentrations. If this is shown in FIG. 1, what appears as a solid line during normal operation will change in the direction of the broken line as the solution concentration increases, and eventually it will approach the crystal line K and there is a danger of crystallization.

従来結晶防止方法としては、高濃度化されたことを検知
、結晶の危険があれば冷媒を溶液中に混入する方法(例
えば特公昭43−17338)などが用いられている。
Conventional crystallization prevention methods include a method of detecting a high concentration and mixing a refrigerant into the solution if there is a risk of crystallization (for example, Japanese Patent Publication No. 17338/1983).

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

しかしこの方法は発生器に熱を加えて作り出した冷媒を
、冷凍効果を発揮させることな(無駄に放出させること
になり、省エネルギに反する欠点を有する、という問題
点があった。
However, this method has a problem in that the refrigerant produced by adding heat to the generator is emitted unnecessarily without exerting its freezing effect, which is contrary to energy conservation.

本発明は、従来の方法の」1記の問題点を解決し、溶液
の結晶化の危険を防ぎ、しかもエネルギの無駄な消費を
防くことができる吸収冷凍機の制御方法を提供すること
を目的とするものである。
An object of the present invention is to provide a method for controlling an absorption refrigerating machine that can solve the problem described in item 1 of the conventional method, prevent the danger of crystallization of the solution, and prevent wasteful consumption of energy. This is the purpose.

〔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、
吸収器、発生器、凝縮器、蒸発器及びこれらの機器を接
続する溶液経路、冷媒経路を備え、冷水温度を検出して
その検出値により前記発生器における溶液加熱量を調節
して冷水温度を制御するようにした吸収冷凍機の制御方
法において、吸収器の溶液の温度を検出し、その検出溶
液温度に応じて冷水温度設定値を調節するカスケード制
御を行い、前記カスケード制御が、検出溶液温度が所定
値に達するまでは、特に別の制御Bが行われていない限
りは冷水温度設定値を一定となし、前記検出溶液温度が
所定の値を越えた場合に、前記検出溶液温度が高い程前
記冷水温度設定値を上昇さセるようにしたことを特徴と
する吸収冷凍機の制御方法を提供せんとするものである
The present invention, as a means for solving the above problems,
It is equipped with an absorber, a generator, a condenser, an evaporator, and a solution path and a refrigerant path that connect these devices, and detects the temperature of the cold water and adjusts the amount of solution heating in the generator based on the detected value to adjust the temperature of the cold water. In a method for controlling an absorption refrigerator, a cascade control is performed in which the temperature of a solution in an absorber is detected and a chilled water temperature set value is adjusted according to the detected solution temperature, and the cascade control Until reaches a predetermined value, the cold water temperature set value is kept constant unless another control B is performed, and when the detected solution temperature exceeds a predetermined value, the higher the detected solution temperature is, the higher the detected solution temperature is. It is an object of the present invention to provide a method for controlling an absorption refrigerator, characterized in that the chilled water temperature set value is increased.

〔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2図においてAは吸収器、Gは発生器、Cは凝縮器、
Eは蒸発器、Xは溶液熱交換器、spは溶液ポンプ、R
Pは冷媒ポンプである。配管1゜2.3.4は溶液管、
5はオーバーフロー管、配管6,7は冷媒管である。8
.9は冷却水管、10は冷水管、11は加熱管であり、
蒸気などの加熱媒体の流量を制御して溶液加熱量を調節
する流量制御弁12を備えている。
In Figure 2, A is an absorber, G is a generator, C is a condenser,
E is evaporator, X is solution heat exchanger, sp is solution pump, R
P is a refrigerant pump. Piping 1゜2.3.4 is a solution pipe,
5 is an overflow pipe, and pipes 6 and 7 are refrigerant pipes. 8
.. 9 is a cooling water pipe, 10 is a cold water pipe, 11 is a heating pipe,
It is equipped with a flow control valve 12 that controls the flow rate of a heating medium such as steam to adjust the amount of solution heating.

13は制御機構であり、温度検出器14により検出され
た冷水出口温度に応じて流量制御弁12を制御し冷水出
口温度を他の制御を行わない限り所定の設定値に保つ。
A control mechanism 13 controls the flow rate control valve 12 in accordance with the cold water outlet temperature detected by the temperature detector 14, and maintains the cold water outlet temperature at a predetermined set value unless other control is performed.

15は吸収器A内の溶液の温度を検出する温度検出器で
あり、その検出溶液温度に応じて制御機構13における
冷水温度設定値を変更するカスケード制御を行うように
なっている。
Reference numeral 15 denotes a temperature detector that detects the temperature of the solution in the absorber A, and performs cascade control to change the cold water temperature set value in the control mechanism 13 according to the detected solution temperature.

その設定値の変更は、吸収器内の検出溶液温度が所定値
(N’に約39℃)に達するまでは、特に他の制御を行
わない限り冷水温度設定値を変更しないで一定とし、検
出溶液温度が所定値を超過した場合は検出溶液温度が高
い程冷水温度設定値を上昇させるように変更するように
なっている。そして、さらに検出溶液温度が上昇すると
結晶化などの危険状態となるから、これを回避するため
に前記検出溶液温度の上述の第一の所定値の上方側に第
二の所定値(イ月;約45℃)を設定し、この第二の所
定値に達したとき冷凍機の運転を停止、例えば発生器へ
の熱源供給をストップさせるようにしたものである。
Changes to the set value should be made by keeping the chilled water temperature set value constant until the detected solution temperature in the absorber reaches a predetermined value (approximately 39°C at N') unless other controls are performed. When the solution temperature exceeds a predetermined value, the higher the detected solution temperature, the higher the cold water temperature setting value is changed. If the temperature of the detection solution further increases, a dangerous state such as crystallization will occur, so in order to avoid this, a second predetermined value (I) is set above the first predetermined value of the temperature of the detection solution. 45° C.), and when this second predetermined value is reached, the operation of the refrigerator is stopped, for example, the supply of heat source to the generator is stopped.

操作ミスや冷却ファンの故障などにより冷却水温度が上
昇した場合、溶液温度が上昇し、冷水温度が一定である
と、冷媒蒸気圧も一定となり、溶液濃度は濃くなり、結
晶線に近づく。
If the cooling water temperature rises due to an operational error or failure of the cooling fan, the solution temperature will rise, and if the chilled water temperature remains constant, the refrigerant vapor pressure will also remain constant, and the solution concentration will become thicker and approach the crystal line.

ここで冷水温度設定値を上げると、それに伴い溶液温度
はほぼ一定を保ちながら蒸発器Eの冷媒蒸発温度が上昇
する。従って溶液濃度は低濃度化され、第3図のように
、サイクルは、実線から破線のように移動する。このよ
うにして冷水温度設定値を上昇させるとサイクルが低濃
度方向に移動することを利用し、冷媒液を溶液中に混入
しないで結晶を回避しつつ少しでも長期間運転できるよ
うにすることができる。
If the chilled water temperature set value is increased here, the refrigerant evaporation temperature of the evaporator E increases while the solution temperature remains substantially constant. Therefore, the solution concentration is reduced, and the cycle moves from a solid line to a broken line as shown in FIG. In this way, by increasing the chilled water temperature set value, the cycle moves towards lower concentration, which can be used to avoid mixing the refrigerant liquid into the solution and avoid crystals while allowing operation for as long as possible. can.

結晶は、基本的には高濃度化により生じるものである。Crystals are basically formed by increasing the concentration.

従って吸収器Aの溶液温度(濃溶液の溶液熱交換器Xの
出ロー吸収器A−希溶液の溶液熱交換器Xの入口、の範
囲内のいづれかの一点の温度)を検知し、この温度が所
定値よりも上昇したとき、冷水温度の設定値を上昇させ
るようにする。
Therefore, the solution temperature of absorber A (the temperature at any one point within the range of the output of solution heat exchanger X for concentrated solutions and the inlet of solution heat exchanger X for dilute solutions) is detected, and this temperature is detected. When the temperature rises above a predetermined value, the set value of the cold water temperature is increased.

さらに精密な制御を行うには、溶液の温度のほかに濃度
を検出して両横出値に応じて冷水温度設定値を変更する
ようにするのが好ましい。
For more precise control, it is preferable to detect the concentration in addition to the temperature of the solution and change the cold water temperature set value in accordance with both side-out values.

濃度の検出は直接的でも間接的でもよく、例えば蒸発器
Eの冷媒液面を水位検出器16にて検出することによっ
ても検出できる。水位検出器16により検出した検出溶
液濃度の信号を制御機構13に送り、温度検出器15か
らの検出溶液温度の信号と併せ、所定のプログラムによ
り得られる値に冷水温度設定値を変更してカスケード制
御する。
The concentration may be detected directly or indirectly, for example, by detecting the refrigerant liquid level in the evaporator E with the water level detector 16. The detected solution concentration signal detected by the water level detector 16 is sent to the control mechanism 13, and together with the detected solution temperature signal from the temperature detector 15, the chilled water temperature set value is changed to a value obtained by a predetermined program and cascade is performed. Control.

本発明の制御に、さらに特願昭57−222118に示
された如き、カスケード制御が、検出溶液温度が、前述
の第一の所定値よりも低い成る第三の所定値以下の場合
は、検出溶液温度が低い程冷水温度設定値を上昇せしめ
るような制御を併用してもよい。
In addition to the control of the present invention, cascade control as shown in Japanese Patent Application No. 57-222118 is used to detect when the detected solution temperature is below a third predetermined value, which is lower than the first predetermined value. Control may also be used in which the cold water temperature setting value is increased as the solution temperature is lower.

なお、以上の方法は単効用、多重効用吸収冷凍機及び冷
温水機に利用できる。
Note that the above method can be used for single-effect and multiple-effect absorption refrigerators and cold/hot water machines.

〔発明の効果〕〔Effect of the invention〕

本発明は、冷凍機運転中に冷却塔の冷却ファン、冷却ポ
ンプ等が故障した場合とか運転ミスをした場合に冷却水
温度が上昇して溶液の結晶化の危険にさらされるおそれ
のある場合に対し、溶液温度を検出してその温度の所定
値以上の上昇に応じて冷水温度を上昇させることにより
、結晶線に近づいたサイクルを低濃度方向に移動させ、
冷媒液を溶液中に混入するような手段をとらないで結晶
化を回避しつつ長期間運転でき、エネルギの無駄な消費
を防ぐことができる効果を奏するものである。
The present invention is useful in cases where the cooling water temperature rises and there is a risk of solution crystallization when the cooling fan, cooling pump, etc. of the cooling tower malfunctions during operation of the refrigerator, or when an operational error occurs. On the other hand, by detecting the solution temperature and increasing the cold water temperature in response to a rise in temperature above a predetermined value, the cycle approaching the crystal line is moved to a lower concentration direction.
It is possible to operate for a long period of time while avoiding crystallization without taking measures such as mixing a refrigerant liquid into the solution, and has the effect of preventing wasteful consumption of energy.

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

第1図は従来の方法のサイクル線図、第2図は本発明の
実施例のフロー図、第3図はそのサイクル線図を示す。 1、 2. 3. 4・・・配管、5・・・オーバーフ
ロー管、6.7・・・配管、8.9・・・冷却水管、1
0・・・冷水管、11・・・加熱管、12・・・流量制
御弁、13・・・制御機構、14.15・・・温度検出
器、16・・・水位検出器、A・・・吸収器、G・・・
発生器、C・・・凝縮器、E・・・蒸発器、X・・・溶
液熱交換器、sp・・・溶液ポンプ、RP・・・冷媒ポ
ンプ。 特許出願人   株式会社  荏原製作所代理人弁理士
  高  木  正   行代理人弁理士  薬  師
      稔代理人弁理士  依  1) 孝 次 
部り71−− 則 藝
FIG. 1 is a cycle diagram of a conventional method, FIG. 2 is a flow diagram of an embodiment of the present invention, and FIG. 3 is a cycle diagram thereof. 1, 2. 3. 4... Piping, 5... Overflow pipe, 6.7... Piping, 8.9... Cooling water pipe, 1
0...Cold water pipe, 11...Heating pipe, 12...Flow rate control valve, 13...Control mechanism, 14.15...Temperature detector, 16...Water level detector, A...・Absorber, G...
Generator, C... Condenser, E... Evaporator, X... Solution heat exchanger, sp... Solution pump, RP... Refrigerant pump. Patent applicant: EBARA CORPORATION Representative Patent Attorney: Masayuki Takagi Representative Patent Attorney: Yakushi Minoru Representative Patent Attorney: Yori 1) Takaji
Section 71-- Nori Gei

Claims (1)

【特許請求の範囲】 1、吸収器、発生器、凝縮器、蒸発器及びこれらの機器
を接続する溶液経路、冷媒経路を備え、冷水温度を検出
してその検出値により前記発生器における溶液加熱量を
調節して冷水温度を制御するようにした吸収冷凍機の制
御方法において、吸収器の溶液の温度を検出し、その検
出溶液温度に応じて冷水温度設定値を調節するカスケー
ド制御を行い、前記カスケード制御が、前記検出溶液温
度が所定の値を越えた場合に、前記検出溶液温度が高い
程前記冷水温度設定値を上昇させるようにしたことを特
徴とする吸収冷凍機の制御方法。 2、前記検出溶液温度の前記所定値の上方側に第二の所
定値を設定し、前記検出溶液温度がこの第二の所定値を
越えた場合は冷凍機を停止させるようにした特許請求の
範囲第1項記載の方法。
[Claims] 1. An absorber, a generator, a condenser, an evaporator, and a solution path and a refrigerant path connecting these devices, detect the cold water temperature, and use the detected value to heat the solution in the generator. In a control method for an absorption chiller that controls the temperature of chilled water by adjusting the amount, the temperature of a solution in an absorber is detected, and a cascade control is performed in which a set value of the chilled water temperature is adjusted according to the detected solution temperature, A method for controlling an absorption refrigerator, wherein the cascade control is such that when the detected solution temperature exceeds a predetermined value, the higher the detected solution temperature is, the higher the chilled water temperature set value is. 2. A second predetermined value is set above the predetermined value of the detected solution temperature, and the refrigerator is stopped when the detected solution temperature exceeds the second predetermined value. The method described in Scope 1.
JP7348185A 1985-04-09 1985-04-09 Method of controlling absorption refrigerator Pending JPS61235652A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7348185A JPS61235652A (en) 1985-04-09 1985-04-09 Method of controlling absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7348185A JPS61235652A (en) 1985-04-09 1985-04-09 Method of controlling absorption refrigerator

Publications (1)

Publication Number Publication Date
JPS61235652A true JPS61235652A (en) 1986-10-20

Family

ID=13519511

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7348185A Pending JPS61235652A (en) 1985-04-09 1985-04-09 Method of controlling absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS61235652A (en)

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