JPH0399168A - Absorptive type freezer - Google Patents

Absorptive type freezer

Info

Publication number
JPH0399168A
JPH0399168A JP23515589A JP23515589A JPH0399168A JP H0399168 A JPH0399168 A JP H0399168A JP 23515589 A JP23515589 A JP 23515589A JP 23515589 A JP23515589 A JP 23515589A JP H0399168 A JPH0399168 A JP H0399168A
Authority
JP
Japan
Prior art keywords
temperature
absorption liquid
regenerator
heat exchanger
signal
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.)
Granted
Application number
JP23515589A
Other languages
Japanese (ja)
Other versions
JP2771626B2 (en
Inventor
Toshiyuki Kaneko
敏之 金子
Masahiro Furukawa
雅裕 古川
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP23515589A priority Critical patent/JP2771626B2/en
Publication of JPH0399168A publication Critical patent/JPH0399168A/en
Application granted granted Critical
Publication of JP2771626B2 publication Critical patent/JP2771626B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

PURPOSE:To uniform a reduction in a heat exchanging amount and prevent a substan tial reduction of a coefficient of performance by a method wherein a rate of tempera ture difference of absorbing liquid between an outlet port of an absorbing device and an inlet port of a regenerator in respect to a temperature difference between a cold water inlet and a cold water outlet of an evaporator is compared with a set value and then a signal is outputted and informing device operated in response to this signal is provided. CONSTITUTION:A rate of a temperature difference between a temperature of absorbed liquid at an outlet port of an absorbing device 5 and another temperature of an inlet port of a hot regenerator 1 and a physical amount varying in response to a variation of load of cold water of another temperature difference between a cold water inlet and a cold water outlet is calculated. This rate is compared with a set value, a control device 35 may output a signal and then an informing device 36 is operated in response to this signal. Due to this fact, when a crystal or the like is produced at heat exchangers 6 and 7 between the absorbing device 5 and the hot regenerator 1 and a heat exchanging amount is reduced, it is possible to inform a supervisor of it with an informing device 36 and an inspecting operation can be carried out for the heat exchangers 6 and 7 before a coefficient of performance of an absorptive freezer is substantially decreased.

Description

【発明の詳細な説明】 (イ〉産業上の利用分野 本発明は吸収冷2g!機に関し、特に熱交換器を備えた
吸収冷凍機に関する。
DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to an absorption chiller (2g!), and more particularly to an absorption chiller equipped with a heat exchanger.

(口〉従来の技術 例えば特公昭58−24705号公報には吸収器と発生
器との間に第1,第2熱交換器を設け、吸収器から流出
した稀吸収液と第2発生器から吸収器へ流れる濃吸収液
とを第1熱交換器(低温熱交換器)にて熱交換し、さら
に、第1熱交換器から第l発生器へ流れる稀吸収液と第
1発生器から第2発生器へ流れる中間吸収液とを第2熱
交換器(高温熱交換器)にて熱交換する吸収冷凍機が開
示されている. 〈ハ〉発明が解決しようとする課題 上記従来の技術にて説明した吸収冷凍機において、第1
熱交換器にて濃吸収液が結晶し、この結晶により第1熱
交換器又番よ第2熱交換器の伝熱管の内径が小さくなる
。そして、濃吸収液又延中間吸収液の流量が減少して第
1熱交換器又は第2熱交換器での濃吸収液又は中間吸収
液と稀吸収液との熱交換量が減少するため、そのままで
吸収冷凍機を運転した場合には、第1熱交換器、第2熱
交換器を介して第1発生器へ送られる稀吸収液の温度が
低下して第1発生器での加熱量が増加して運転効率が低
下するという問題が発生していた。
(Example) Conventional technology For example, in Japanese Patent Publication No. 58-24705, first and second heat exchangers are provided between the absorber and the generator, and the diluted absorption liquid flowing out from the absorber is exchanged with the second generator. The concentrated absorption liquid flowing to the absorber is heat exchanged with the first heat exchanger (low-temperature heat exchanger), and the dilute absorption liquid flowing from the first heat exchanger to the first generator is exchanged with the first heat exchanger. An absorption refrigerator is disclosed that exchanges heat with an intermediate absorption liquid flowing to a second generator in a second heat exchanger (high temperature heat exchanger). In the absorption refrigerator described in
The concentrated absorption liquid crystallizes in the heat exchanger, and this crystallization reduces the inner diameter of the heat transfer tubes of the first heat exchanger and the second heat exchanger. Then, the flow rate of the concentrated absorption liquid or the rolled intermediate absorption liquid decreases, and the amount of heat exchanged between the concentrated absorption liquid or intermediate absorption liquid and the dilute absorption liquid in the first heat exchanger or the second heat exchanger decreases. If the absorption refrigerator is operated as it is, the temperature of the dilute absorption liquid sent to the first generator via the first heat exchanger and second heat exchanger will decrease, and the amount of heating in the first generator will decrease. The problem has been that the amount of fuel increases and the operating efficiency decreases.

本発明は熱交換器での熱交換量の低下を管理者などに報
知し、或績係数の大幅な低下を防止することを目的とす
る, (二〉課題を解決するための手段 本発明は上記課題を解決するために、吸収器(5)の出
口側の吸収液温度と高温再生器(1)の入口側の吸収液
温度との差と蒸発器〈4)の冷水負荷に応じて変化する
冷水出入口の温度差との比率を算出し、この比率と設定
値とを比較して信号を出力する制御装置(35)と、こ
の制御装置(35)からの信号を入力して動作する報知
器(36〉とを備えた吸収冷凍機を提供するものである
The purpose of the present invention is to notify a manager, etc. of a decrease in the amount of heat exchanged in a heat exchanger, and to prevent a significant decrease in the coefficient of performance. In order to solve the above problems, the temperature of the absorption liquid changes depending on the difference between the temperature of the absorption liquid on the outlet side of the absorber (5) and the temperature of the absorption liquid on the inlet side of the high-temperature regenerator (1) and the cold water load of the evaporator (4). A control device (35) that calculates the ratio between the temperature difference at the cold water inlet and outlet, compares this ratio with a set value, and outputs a signal, and an alarm that operates by inputting the signal from this control device (35). The present invention provides an absorption refrigerator equipped with a container (36).

又、低温熱交換器(6)の入I1側の吸収液温度と高温
熱交換器(7〉の出口側の吸収液温度との差と蒸発器(
4)の冷水出入[1の温度差との比率を算出し、この比
率と設定値とを比較して信号を出力する制御装置〈35
)と、この制御装置(35〉からの信号を入力して動作
する報知器(36)とを備えた吸収冷凍機を提供するも
のである, 0)作用 吸収冷凍機の運転時、例えば冷却水温度の低下により吸
収器(5)から流出する稀吸収液の温度が低下し、低温
再生器(2)から流れて来た濃吸収液の温度が低温熱交
換器(6)にて大幅に低下すると、結晶が発生し、低温
熱交換器(6)を流れる濃吸収液の量が減少する。そし
て、吸収器〈5〉出口側の稀吸収液の温度と高温再生器
(1)の入r:J側稀吸収液温度との差が減少し、この
差に対する冷却水出入口温度の差の比率が15以下にな
ると制御装置(35)が報知器(36)に信号を出力す
る。そして、報知器(36)が動作して管理者に低温熱
交換器(6〉又は高温熱交換器(7〉での熱交換量の減
少を知らせることが可能になる。又、制御装置(35〉
は冷水出入口温度度差と稀吸収液温度差との比率と設定
値とを比較して報知器(36)へ信号を出力し、負荷が
変化して冷水出入口温度差、稀吸収液温度差が変化した
場合にも、報知器(36〉の誤動作を防止することが可
能になる. 又、吸収冷凍機の運転時、例えば低温熱交換器(6)に
結晶が発生し、この結晶により低温熱交換器(6)を流
れる濃吸収液の量が減少すると、低温熱交換器(6)で
の稀吸収液と濃吸収液との熱交換量が減少する。このた
め、低温熱交換器入口側の稀吸収液温度と高温熱交換器
(7)出口側の稀吸収液温度との差が減少する。すると
、この稀吸収液温度差に対する冷水出入口温度差の比率
が減少し、この比率が15以下になると、制御装置(3
5)が報知信号を出力し、報知器(36)が動作して管
理者に低温熱交換器(6)、又は高温熱交換器(7)で
の熱交換量の減少を知らせることが可能になり、又、負
荷の変動により稀吸収液温度差が変化した場合にも報如
器(36〉の誤動作を防止することが可能になる。
Also, the difference between the absorption liquid temperature on the inlet I1 side of the low-temperature heat exchanger (6) and the absorption liquid temperature on the outlet side of the high-temperature heat exchanger (7) and the evaporator (
4) A control device that calculates the ratio of cold water inlet and outlet [1] to the temperature difference, compares this ratio with a set value, and outputs a signal <35
) and an alarm (36) that operates by inputting a signal from the control device (35). Due to the decrease in temperature, the temperature of the dilute absorption liquid flowing out from the absorber (5) decreases, and the temperature of the concentrated absorption liquid flowing from the low-temperature regenerator (2) decreases significantly in the low-temperature heat exchanger (6). Then, crystals are generated and the amount of concentrated absorption liquid flowing through the low temperature heat exchanger (6) is reduced. Then, the difference between the temperature of the diluted absorption liquid on the outlet side of the absorber <5> and the temperature of the diluted absorption liquid on the inlet r:J side of the high-temperature regenerator (1) decreases, and the ratio of the difference in the cooling water inlet and outlet temperatures to this difference decreases. When becomes 15 or less, the control device (35) outputs a signal to the alarm (36). Then, the alarm (36) operates to notify the administrator of the decrease in the amount of heat exchange in the low-temperature heat exchanger (6) or the high-temperature heat exchanger (7). 〉
compares the ratio of the temperature difference between the chilled water inlet and outlet and the dilute absorption liquid temperature difference with the set value and outputs a signal to the alarm (36). It is also possible to prevent the alarm (36) from malfunctioning even if the When the amount of concentrated absorption liquid flowing through the exchanger (6) decreases, the amount of heat exchanged between the dilute absorption liquid and the concentrated absorption liquid in the low temperature heat exchanger (6) decreases. The difference between the temperature of the dilute absorbent at the outlet side of the high temperature heat exchanger (7) decreases.Then, the ratio of the temperature difference between the cold water inlet and outlet to this dilute absorbent temperature difference decreases, and this ratio becomes 15. When the control device (3
5) outputs a notification signal, and the notification device (36) operates to notify the administrator of a decrease in the amount of heat exchanged in the low-temperature heat exchanger (6) or the high-temperature heat exchanger (7). Furthermore, even when the temperature difference of the diluted absorbent liquid changes due to load fluctuations, it is possible to prevent the alarm device (36>) from malfunctioning.

(へ)実施例 以下、本発明の一実施例を図面に基づいて詳細に説明す
る。
(F) Example Hereinafter, an example of the present invention will be described in detail based on the drawings.

第1図に示したものは二重効用吸収冷凍機であり、冷媒
に水(U*O)、吸収剤(吸収液)に臭化リチウム(L
iBr)水溶液を使用したものである。
The one shown in Figure 1 is a dual-effect absorption refrigerator, in which the refrigerant is water (U*O) and the absorbent (absorbing liquid) is lithium bromide (L).
iBr) using an aqueous solution.

第1図において、(1)ほガスバーナ(IB)を備えた
高温再生器、(2)は低温再生器、(3〉は凝縮器、(
4)は蒸発器、(5)は吸収器、(6)は低温熱交換器
、〈7)は高温熱交換器、(8A) , (8B) ,
 (sc)、及び(9)ないし(12)は吸収液配管、
(15)は吸収液ボンブ、〈16〉ないし(l8)吐冷
媒配管、(19)は冷媒ボンブ、(20)はガスバーナ
(1B〉に接続されたガス配管、(21〉は加熱量制御
弁、(22)は冷水配管であり、それぞれは第1図に示
したように配管接続されている。又、(25)は冷却水
配管であり、この冷却水配管(25)の途中に1ま吸収
器熱交換器〈26)、及び凝縮器熱交換器〈27)が設
けられている。
In Figure 1, (1) a high-temperature regenerator equipped with an insulating gas burner (IB), (2) a low-temperature regenerator, (3> a condenser,
4) is an evaporator, (5) is an absorber, (6) is a low temperature heat exchanger, <7) is a high temperature heat exchanger, (8A), (8B),
(sc), and (9) to (12) are absorption liquid piping,
(15) is an absorption liquid bomb, <16> to (18) discharge refrigerant pipes, (19) is a refrigerant bomb, (20) is a gas pipe connected to a gas burner (1B>), (21> is a heating amount control valve, (22) is a cold water pipe, and each pipe is connected as shown in Fig. A condenser heat exchanger (26) and a condenser heat exchanger (27) are provided.

(31) , (32)はそれぞれ冷却水配管(22〉
の蒸発器(4)の入口側、及び出口側に取付けられた冷
水入口温度検出器(以下第1温度検出器という)、及び
冷水出口温度検出器(以下第2温度検出器という)であ
る。又、(33)は吸収液配管(8A〉に取付けられ吸
収器〈5〉出口側の稀吸収液温度を検出する温度検出器
(以下、第3温度検出器という)、(34〉は吸収液配
管(8C〉に取付けられ、高温再生器(1)入力側の稀
吸収液温度を検出する温度検出器(以下第4温度検出器
という)である。さらに、(35)は各温度検出器(3
1) . (32) , (33) , (34)から
信号を入力して動作する制御装置であり、(35)は制
御装置(35〉からの信号を入力して動作する報知器で
ある。そして、この報知器(36〉は複数の発光素子か
ら構成された表示器(37)と、プザー(38〉とから
構成されている。ここで、報知器(36〉は吸収冷凍機
の制御盤(図示せず)、又は吸収冷凍機の管理室などに
設けられている。
(31) and (32) are the cooling water pipes (22), respectively.
These are a cold water inlet temperature detector (hereinafter referred to as a first temperature detector) and a cold water outlet temperature detector (hereinafter referred to as a second temperature detector) attached to the inlet side and outlet side of the evaporator (4). In addition, (33) is a temperature detector (hereinafter referred to as the third temperature sensor) that is attached to the absorption liquid pipe (8A) and detects the temperature of the diluted absorption liquid on the outlet side of the absorber <5>, and (34> is the temperature sensor for detecting the temperature of the diluted absorption liquid on the outlet side of the absorber <5>). This is a temperature detector (hereinafter referred to as the fourth temperature detector) that is attached to the pipe (8C) and detects the temperature of the dilute absorption liquid on the input side of the high temperature regenerator (1). 3
1). It is a control device that operates by inputting signals from (32), (33), and (34), and (35) is an alarm that operates by inputting a signal from the control device (35>). The alarm (36) is composed of a display (37) composed of a plurality of light emitting elements and a puzzer (38). ), or in the control room of the absorption chiller.

以下、上記制御装置(35〉について第2図に基ついて
詳細に説明する。ここで、第1図と同じものには同じ図
番を付し、その詳細な説明は省略する.制御装置(35
〉はマイクロコンピュータにより構成されており、(4
0〉は各温度検出器からの信号を変換して出力する入力
インターフエイス、(41〉は入力インターフェイス(
40〉から出力された信号を入力して動作する中央処理
装置(以下CPUという)である.又、(42〉は記憶
素子(以下ROMという)であり、ROM(42)には
冷水入口温度と冷水出口温度との差、即ち冷水温度差を
演算するプログラム、吸収器(5)出口側の稀吸収液温
度と高温再生器(1)入口側の稀吸収液温度との差、即
ち稀吸収液温度差を演算するプログラム、上記冷水温度
差に対する稀吸収液温度差の比率を演算するプログラム
、及び上記比率と設定値とを比較するプログラムなどが
記憶されている。又、〈43)は各温度検出器(31)
 , (32) , (33) , (34)により検
出された温度データを一時記憶する記憶素子(以下RA
Mという)であり、〈44〉はCPU(41)から出力
された信号を変換して出力する出力インターフェイスで
ある。そして、出力インターフェイスク44)から報知
器(36)へ信号が出力される。又、(45)は所定時
間(例えば1分)ごとに信零を出力するCLOCKであ
る. 上記吸収冷凍機の運転時、従来の吸収冷凍機と同様に高
温再生器(1)で蒸発した冷媒は低温再生器(2〉を経
て凝縮器(3〉へ流れ、凝縮器熱交換器(27〉を流れ
る水と熱交換して凝縮液化した後冷媒配管(17〉を介
して蒸発器(4)へ流れる。そして、冷媒が冷水配管(
22)内の水と熱交換して蒸発し、気化熱によって冷水
配管(22〉内の水が冷却される。
Hereinafter, the above control device (35) will be explained in detail based on FIG. 2. Here, the same parts as in FIG.
〉 is composed of a microcomputer, and (4
0> is an input interface that converts and outputs the signal from each temperature sensor, (41> is an input interface (
This is a central processing unit (hereinafter referred to as CPU) that operates by inputting signals output from 40>. Further, (42> is a memory element (hereinafter referred to as ROM), and the ROM (42) contains a program for calculating the difference between the cold water inlet temperature and the cold water outlet temperature, that is, the cold water temperature difference, and a program on the outlet side of the absorber (5). A program that calculates the difference between the dilute absorption liquid temperature and the dilute absorption liquid temperature on the inlet side of the high temperature regenerator (1), that is, a dilute absorption liquid temperature difference, a program that calculates the ratio of the dilute absorption liquid temperature difference to the cold water temperature difference, and a program for comparing the above ratio and the set value. Also, <43) is for each temperature detector (31).
, (32), (33), (34) A memory element (hereinafter referred to as RA) that temporarily stores the temperature data detected by
44 is an output interface that converts and outputs the signal output from the CPU (41). A signal is then output from the output interface (44) to the alarm (36). Further, (45) is a CLOCK that outputs a signal zero every predetermined time (for example, one minute). When the absorption chiller is operated, the refrigerant evaporated in the high temperature regenerator (1) passes through the low temperature regenerator (2) and flows to the condenser (3), similar to the conventional absorption chiller, and flows into the condenser heat exchanger (27). After exchanging heat with the water flowing through the water pipe (17), the refrigerant is condensed and liquefied, and then flows to the evaporator (4) via the refrigerant pipe (17).
It evaporates by exchanging heat with the water in the cold water pipe (22), and the water in the cold water pipe (22) is cooled by the heat of vaporization.

そして、冷水が負荷に循環して冷房運転が行われる。ま
た、蒸発器(4)で蒸発した冷媒は吸収器(5)で吸収
液に吸収される。そして、冷媒を吸収して濃度が薄くな
った吸収液が吸収液ボンブ(15)の運転により低温熱
交換器(6〉、及び高温熱交換器(7〉を経て高温再生
器(1〉へ送られる。高温再生器(1)に入った吸収液
はバーナ(IB〉によって加熱され、冷媒が蒸発し、中
濃度の吸収液が高温熱交換器(7)を経て低温再生器(
2〉へ入る。そして、吸収液は高温再生器(1)から冷
媒配管(16)を流れて来た冷媒蒸気によって加熱され
、さらに冷媒が蒸発分離され濃度が高くなる。高濃度に
なった吸収液(以下濃度という)は低温熱交換器(6〉
を経て温度低下して吸収器(5)へ送られ、散布される
Then, the cold water is circulated to the load to perform cooling operation. Further, the refrigerant evaporated in the evaporator (4) is absorbed into an absorption liquid in the absorber (5). Then, the absorption liquid whose concentration has become diluted by absorbing the refrigerant is sent to the high-temperature regenerator (1>) through the low-temperature heat exchanger (6>) and the high-temperature heat exchanger (7>) by the operation of the absorption liquid bomb (15). The absorption liquid that has entered the high temperature regenerator (1) is heated by the burner (IB>, the refrigerant is evaporated, and the medium concentration absorption liquid passes through the high temperature heat exchanger (7) and is transferred to the low temperature regenerator (1).
Enter 2>. Then, the absorption liquid is heated by the refrigerant vapor flowing through the refrigerant pipe (16) from the high-temperature regenerator (1), and the refrigerant is further evaporated and separated, increasing its concentration. The highly concentrated absorption liquid (hereinafter referred to as concentration) is transferred to a low-temperature heat exchanger (6).
The temperature of the water is lowered, and the water is sent to the absorber (5) where it is dispersed.

以上のように吸収冷凍機が運転されているとき各温度検
出器、(31) , (32) . (33) . (
34)が冷水温度、及び稀吸収液の温度を検出する。以
下、制御装置(35)の動作について第3図のブローチ
勺一トに基づいて説明する。吸収冷凍機の運転時、各温
度検出器(31) , (32) , (33) , 
(34)が検出した温度データは入力インターフェイス
(40)、CPU(41)を介してRAM(43)に記
憶される。そして、CLO C K (45)がカウン
トアップして信号をCPU(4l〉へ出力すると、この
信号に基づいてCPU(41)が動作してR A M 
(43)から温度データを読み込む。又、CPU(41
)がROM(42)から上記各プログラムを読み込み動
作し、冷水温度差、稀吸収液温度差、及び冷水温度差に
対する稀吸収液温度差の比率を算出する。ここで、負荷
が例えば100%であり冷水出入口温度差が5゜C、吸
収器(4)出口側の稀吸収液温度が40″C、高温再生
器(1)入口側の稀吸収液温度140゜Cで稀吸収液温
度差が100″Cのときには冷水温度差に対する稀吸収
液100 温度差の比率は . =20になる。そして、RO M
 (42)に記憶されていた設定値例えば15と算出さ
れた比率20とがCPU(41)に比較され、算出され
た比率が設定値より大きいときにはCPU(41〉は出
力インターブエイス(44)へ信号を出力せず、出力イ
ンターフエイス(44〉から報知信号が出力されない。
As described above, when the absorption refrigerator is operating, each temperature detector, (31), (32) . (33). (
34) detects the cold water temperature and the temperature of the dilute absorption liquid. Hereinafter, the operation of the control device (35) will be explained based on the broaching process shown in FIG. When the absorption refrigerator is operating, each temperature detector (31), (32), (33),
The temperature data detected by (34) is stored in RAM (43) via input interface (40) and CPU (41). Then, when CLO C K (45) counts up and outputs a signal to CPU (4l), CPU (41) operates based on this signal and R A M
Read the temperature data from (43). Also, CPU (41
) reads each of the above programs from the ROM (42) and operates to calculate the cold water temperature difference, the diluted absorption liquid temperature difference, and the ratio of the diluted absorption liquid temperature difference to the cold water temperature difference. Here, the load is, for example, 100%, the temperature difference between the cold water inlet and outlet is 5°C, the temperature of the diluted absorption liquid on the outlet side of the absorber (4) is 40"C, and the temperature of the diluted absorption liquid on the inlet side of the high temperature regenerator (1) is 140"C. When the temperature difference of the diluted absorbent liquid is 100"C at 100°C, the ratio of the temperature difference of the diluted absorbent liquid to the cold water temperature difference is . =20. And R.O.M.
The CPU (41) compares the set value, for example 15, stored in (42) with the calculated ratio 20, and when the calculated ratio is greater than the set value, the CPU (41) outputs the output interval (44). No signal is output to the output interface (44), and no notification signal is output from the output interface (44).

このため、報知器(36〉は動作しない。Therefore, the alarm (36>) does not operate.

その後、負荷がほとんど変化せず冷水出入口温度差が5
℃で変化していないとき、例えば低温熱交換器(6)を
流れる稀吸収液の温度が低下し、濃吸収液の温度が大幅
に低下した場合、低温熱交換器(6〉にて濃吸収液が結
晶する。そして、この結晶のために、低温熱交換器(6
)の熱交換パイプ(図示せず)の内径が次第に減少する
と、低温熱交換器(6)を流れる濃吸収液の量が減少す
る。又、低温熱交換器(6)内のヘドロによっても濃吸
収液の流量が減少する。そして、濃吸収液と稀吸収液と
の熱交換量が減少する。このため。例えば稀吸収液温度
差が減少して例えは上記100゜Cから75゜Cになり
、冷水温度差に対する稀吸収液温度差75 の比率が丁=15になるとC P U(41)は出力イ
ンターフエイス(44)へ信号を出力する。そして、出
力インターフェイス(44)はこの信号に基づいて報知
信号を報知器(36〉へ出力する。報知器(36)は報
知信号を入力すると動作し、表示器(37)にて例えば
ALARMの文字が点滅するとともにブザー(38)が
発音する。そして、管理者が表示器(37)の文字の点
滅、又はブザー(38〉の発音により低温熱交換器(6
)又は高温熱交換器(7)の熱交換量の減少を知り、例
えば吸収冷凍機の運転停止中に各熱交換器の点滅が行わ
れ、低温熱交換器〈6〉の交換作業等が行われる。又、
高温熱交換器(7)に結晶が発生し、熱交換量が減少し
て稀吸収液温度差が減少し、冷水温度差に対する稀吸収
液温度差の比率が15以下になると、制御装置(35〉
が報知信号を出力し、報知器(36)が動作する。そし
て、上記と同様に点検等が行われる。
After that, the load hardly changed and the temperature difference between the cold water inlet and outlet was 5.
For example, if the temperature of the dilute absorption liquid flowing through the low-temperature heat exchanger (6) decreases and the temperature of the concentrated absorption liquid decreases significantly, the temperature of the concentrated absorption liquid in the low-temperature heat exchanger (6>) decreases. The liquid crystallizes.For this crystallization, a low temperature heat exchanger (6
) gradually decreases the inner diameter of the heat exchange pipe (not shown), the amount of concentrated absorption liquid flowing through the low temperature heat exchanger (6) decreases. Furthermore, the flow rate of the concentrated absorption liquid is also reduced due to sludge in the low temperature heat exchanger (6). Then, the amount of heat exchange between the concentrated absorption liquid and the dilute absorption liquid decreases. For this reason. For example, when the dilute absorbent temperature difference decreases from 100°C to 75°C, and the ratio of the dilute absorbent temperature difference 75 to the cold water temperature difference becomes 15, the CPU (41) outputs the output interface. A signal is output to the face (44). Based on this signal, the output interface (44) outputs a notification signal to the notification device (36>).The notification device (36) operates when the notification signal is input, and the display device (37) displays, for example, the words ALARM. blinks and the buzzer (38) sounds. Then, the administrator turns on the low-temperature heat exchanger (6) by blinking the characters on the display (37) or by sounding the buzzer (38).
) or the amount of heat exchanged by the high-temperature heat exchanger (7) has decreased, for example, each heat exchanger is blinked while the absorption chiller is stopped, and replacement work for the low-temperature heat exchanger (6) is performed. be exposed. or,
When crystals occur in the high temperature heat exchanger (7), the amount of heat exchange decreases and the temperature difference of the diluted absorption liquid decreases, and the ratio of the diluted absorption liquid temperature difference to the cold water temperature difference becomes 15 or less, the controller (35) 〉
outputs a notification signal, and the notification device (36) operates. Inspections and the like are then performed in the same manner as above.

又、負荷と冷水出入口温度差とはほぼ比例し、例えば負
荷が80%のときには冷水出入口温度差吐4゜C、負荷
が60%のときには冷水出入口温度差は3゜Cになる。
Further, the load and the temperature difference between the cold water inlet and outlet are almost proportional; for example, when the load is 80%, the temperature difference between the cold water inlet and outlet is 4°C, and when the load is 60%, the temperature difference between the cold water inlet and outlet is 3°C.

又、負荷の減少に伴ない高温再生器(1〉の加熱量も減
少し、高温再生器(1)から高温熱交換器(7〉、及び
低温再生器(2〉を経て低温熱交換器(6)へ流れる中
間吸収液、及び濃吸収液の温度が低下する。そして、稀
吸収液温度差も減少し、例えば負荷が80%のとき稀吸
収液温度差が例えば80゜Cに低下し、冷水温度差に対
する稀吸80 収液温度差の比率がT=20であり、設定値より大きい
ときにはC P U(41)は出力インターフェイス(
44〉へ信号を出力せず、報知器(36)は動作しない
。又、稀吸収液温度差が例えば64゜Cであり、負荷が
100%のときには報知器(36〉が動作する温度にな
った場合にも、負荷が80%の場合.64 には上記比率かT=16であるため、CPU(41)は
信号を出力せず、報知器(36〉は動作しない。
In addition, as the load decreases, the amount of heating in the high temperature regenerator (1) also decreases, and the heat is transferred from the high temperature regenerator (1) through the high temperature heat exchanger (7) and the low temperature regenerator (2) to the low temperature heat exchanger (2). 6) The temperature of the intermediate absorption liquid and the concentrated absorption liquid flowing into the tank decreases.The temperature difference of the diluted absorption liquid also decreases, for example, when the load is 80%, the temperature difference of the diluted absorption liquid decreases to, for example, 80°C, When the ratio of the rare absorption 80 and collected liquid temperature difference to the cold water temperature difference is T=20 and is larger than the set value, the CPU (41) outputs the output interface (
44>, and the alarm (36) does not operate. Also, if the dilute absorbent temperature difference is, for example, 64°C, and the load is 100%, the temperature at which the alarm (36) operates will be reached, but if the load is 80%, the above ratio will change. Since T=16, the CPU (41) does not output a signal and the alarm (36>) does not operate.

又、低温熱交換器(6)にて結晶が発生して低温熱交換
器(6)での熱交換量が減少して稀吸収液温度60 差が減少して60″C以下になり、上記比率がT=15
以下になったときにはCPU(41)は出力インターフ
エイス(44)へ信号を出力する。そして、出力インタ
ーフエイス(44)が報知信号を報知器(36〉へ出力
し、報知器(36)は上記負荷が100%のときと同様
に動作する. 又、負荷が例えば60%の場合(冷水出入口温度差は3
゜C)には、稀吸収液温度差が45゜C以下になり冷水
出入口温度差に対する稀吸収液温度差カインターフエイ
ス(44)へ信号を出力し、報知器(36〉が動作する
In addition, crystals are generated in the low temperature heat exchanger (6), and the amount of heat exchanged in the low temperature heat exchanger (6) decreases, and the dilute absorption liquid temperature difference decreases to 60"C or less, and the above The ratio is T=15
When the value is below, the CPU (41) outputs a signal to the output interface (44). Then, the output interface (44) outputs the notification signal to the notification device (36>), and the notification device (36) operates in the same manner as when the load is 100%. Also, when the load is, for example, 60% ( The temperature difference between the cold water inlet and outlet is 3
When the dilute absorption liquid temperature difference becomes 45 degrees Celsius or less, a signal is output to the dilute absorption liquid temperature difference relative to the cold water inlet/outlet temperature difference interface (44), and the alarm (36>) is activated.

以下、同様に負荷が変化した場合にも、冷水出入[コ温
度差に対する稀吸収液温度差が15以下になったときに
はC P U(41)が出力インターフェイス(44)
へ信号を出力し、報知器(36〉が動作する。
Similarly, when the load changes, the CPU (41) connects the output interface (44) to
The alarm (36) is activated.

上記実施例によれば、吸収冷凍機の運転中に、低温熱交
換器(6)又は高温熱交換器(7〉にて結晶が発生し、
低温熱交換器(6)、又は高温熱交換器(7〉を流れる
吸収液の量が減少し、濃吸収液又は中間吸収液と稀吸収
液との熱交換量が減少し、冷水出入口温度差に対する稀
吸収液温度差の比率が設定値以下になった場合には、制
御装置(35〉から報知器(36〉へ報知信号が出力さ
れ、この信号を入力した報知器(36〉が動作するので
、低温熱交換器(6〉の熱交換量の減少を管理者に知ら
せることができ、管理者は低温熱交換器(6〉又は高温
熱交換器?7)の熱交換量が大幅に低下して、吸収冷凍
機の成績係数が大幅に低下する前に点検を行い、低温熱
交換器〈6)、又は高温熱交換器の交換を行うことがで
きる。
According to the above embodiment, crystals are generated in the low temperature heat exchanger (6) or the high temperature heat exchanger (7>) during operation of the absorption refrigerator,
The amount of absorption liquid flowing through the low-temperature heat exchanger (6) or the high-temperature heat exchanger (7) decreases, the amount of heat exchanged between the concentrated absorption liquid or intermediate absorption liquid and the dilute absorption liquid decreases, and the temperature difference between the cold water inlet and outlet decreases. When the ratio of the dilute absorption liquid temperature difference to Therefore, it is possible to notify the administrator of the decrease in the heat exchange amount of the low temperature heat exchanger (6>), and the administrator can notify the administrator of the decrease in the heat exchange amount of the low temperature heat exchanger (6> or high temperature heat exchanger? 7). Therefore, it is possible to perform an inspection and replace the low-temperature heat exchanger (6) or the high-temperature heat exchanger before the coefficient of performance of the absorption refrigerator drops significantly.

又、負荷の変化に応じて変化する冷水出入口温度差に対
する稀吸収液温度差との比率と設定値とを比較して報知
器(36〉を動作させるため、負荷が減少して稀吸収液
温度差が減少したときの報知器(36〉の誤動作を回避
することができる.尚、上記実施例において第3,第4
温度検出器(33) , (34)をそれぞれ吸収液配
管(8A) , (8C)に取付けたが、第3温度検出
■(33)を吸収器(5)の吸収液溜り(5A)に取付
けても、又、第4温度検出器(34)を吸収液配管{8
B}に設けても良い。ここで、第4温度検出器(34)
を吸収液配管(8B)に設けた場合には、報知器(36
〉を動作させるときの冷水出入口温度差に対する稀吸収
液温度差の比率を上記実施例の15より小さく設定する
。又、上記実施例において、報知器(36)を動作させ
るときの冷水出入口温度差に対する稀吸収液温度差の比
率を15と設定したが、この設定値は15に限定される
ものではない。
In addition, since the alarm (36) is operated by comparing the ratio of the temperature difference between the cold water inlet and outlet to the temperature difference of the diluted absorbent liquid and the set value, which changes according to the change in load, the load decreases and the temperature of the diluted absorbent liquid decreases. It is possible to avoid malfunction of the alarm (36) when the difference decreases.In addition, in the above embodiment, the third and fourth
Temperature detectors (33) and (34) were installed on the absorption liquid piping (8A) and (8C), respectively, but the third temperature sensor (33) was installed on the absorption liquid reservoir (5A) of the absorber (5). However, the fourth temperature sensor (34) is also connected to the absorption liquid piping {8
B} may be provided. Here, the fourth temperature detector (34)
is installed in the absorption liquid piping (8B), the alarm (36
The ratio of the dilute absorption liquid temperature difference to the cold water inlet/outlet temperature difference when operating the above is set smaller than 15 of the above embodiment. Further, in the above embodiment, the ratio of the dilute absorption liquid temperature difference to the cold water inlet/outlet temperature difference when operating the alarm (36) is set to 15, but this set value is not limited to 15.

(ト)発明の効果 本発明は以上のように構成された吸収冷凍機であり、吸
収器の出口側の吸収液温度と再生器の入口側の吸収液温
度との差と蒸発器の冷水出入口温度差などの冷水負荷の
変化に応じて変化する物理量との比率を算出し、この比
率と設定値とを比較して制御装置が信号を出力し、この
信号により報知器が動作するので、吸収器と再生器との
間の熱交換器に結晶などが発生して熱交換量が減少した
ときには、管理者などに報知器により知らせることがで
き、吸収冷凍機の成績係数が大幅に低下する前に熱交換
器の点検作業などを行うことができる。又、負荷により
変化する冷水出入口温度差と上記吸収液の温度差との比
率を算出して、この比率により制御装置が信号を出力す
るため、負荷が変化して冷水出入口温度差が変化した場
合にも報知器の誤動作を防止できる。
(G) Effects of the Invention The present invention is an absorption refrigerating machine configured as described above, which is characterized by the difference between the absorption liquid temperature on the outlet side of the absorber and the absorption liquid temperature on the inlet side of the regenerator and the cold water inlet/outlet of the evaporator. Calculates the ratio with physical quantities that change according to changes in chilled water load such as temperature difference, compares this ratio with a set value, and outputs a signal.This signal activates the alarm, so the absorption If crystals occur in the heat exchanger between the regenerator and the regenerator and the amount of heat exchange decreases, an alarm can be used to notify the administrator, etc., before the coefficient of performance of the absorption chiller decreases significantly. It is possible to perform inspection work on heat exchangers, etc. In addition, the ratio between the temperature difference between the cold water inlet and outlet, which changes depending on the load, and the temperature difference of the above-mentioned absorption liquid is calculated, and the control device outputs a signal based on this ratio, so if the load changes and the temperature difference between the cold water inlet and outlet changes. This can also prevent alarm malfunctions.

又、吸収器と再生器との間に設けられた熱交換器の入口
側吸収液温度と出11側吸収液温度との差と蒸発器の冷
水出入口温度の差との比率を算出し、この比率と設定値
とを比較して制御装置が信号を出力し、この信号により
報知器が動作するので、熱交換器の熱交換量が減少した
ときには管理者などに報知でき、吸収冷凍機の成績係数
が大幅に低下する前に熱交換器の点検作業等を行うこと
ができ、又、負荷が変化した場合の報知器の誤動作を防
止することができる。
Also, calculate the ratio of the difference between the temperature of the absorption liquid on the inlet side and the absorption liquid temperature on the output 11 side of the heat exchanger provided between the absorber and the regenerator and the difference in the temperature of the cold water inlet and outlet of the evaporator. The control device outputs a signal by comparing the ratio with the set value, and this signal activates the alarm, so when the heat exchange amount of the heat exchanger decreases, it can notify the administrator etc., and the performance of the absorption chiller can be monitored. It is possible to perform inspection work on the heat exchanger before the coefficient decreases significantly, and it is also possible to prevent malfunction of the alarm when the load changes.

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

第1図は本発明の一実施例を示す吸収冷凍機の回路構成
図、第2図は制御装置のブロック・ダイヤグラム、第3
図は報知器の動作を説明するためのブローチャートであ
る。 (1)・・・高温再生器、 (4)・・・蒸発器、 (
5)・・・吸収器、 (6)・・・低温熱交換器、 <
35)・・・制御装置、 (36)・・・報知器。
Fig. 1 is a circuit configuration diagram of an absorption refrigerator showing an embodiment of the present invention, Fig. 2 is a block diagram of a control device, and Fig. 3 is a block diagram of a control device.
The figure is a flowchart for explaining the operation of the alarm. (1)...High temperature regenerator, (4)...Evaporator, (
5)...Absorber, (6)...Low temperature heat exchanger, <
35)...Control device, (36)...Alarm device.

Claims (1)

【特許請求の範囲】 1、吸収器、再生器、この再生器と吸収器との間に設け
られ吸収器から再生器へ流れる吸収液と再生器から吸収
器へ流れる吸収液とを熱交換する熱交換器、及び蒸発器
をそれぞれ配管接続してなる吸収冷凍機において、吸収
器の出口側の吸収液温度と再生器の入口側の吸収液温度
との差と蒸発器の冷水出入口の温度差との比率を算出し
、この比率と設定値とを比較して信号を出力する制御装
置と、この制御装置からの信号を入力信号として動作す
る報知器とを備えたことを特徴とする吸収冷凍機。 2、吸収器、再生器、吸収器と再生器との間に設けられ
、吸収器から再生器へ流れる吸収液と再生器から吸収器
へ流れる吸収液とを熱交換する熱交換器、及び蒸発器を
それぞれ配管接続した吸収冷凍機において、熱交換器の
吸収液入口側温度と吸収液出口側温度との差と蒸発器の
冷水出入口温度差との比率を算出し、この比率と設定値
とを比較して信号を出力する制御装置と、この制御装置
から信号を入力して動作する報知器とを備えたことを特
徴とする吸収冷凍機。 3、吸収器、再生器、この再生器と吸収器との間に設け
られた熱交換器、及び蒸発器などをそれぞれ配管接続し
、吸収器と再生器との間に熱交換器を設けた吸収冷凍機
において、熱交換器の入口側の吸収液温度と出口側の吸
収液温度との差と蒸発器の冷水負荷に応じて変化する物
理量との比率を算出し、この比率と設定値とを比較して
信号を出力する制御装置と、この制御装置から信号を入
力して動作する報知器とを備えたことを特徴とする吸収
冷凍機。
[Claims] 1. Absorber, regenerator, provided between the regenerator and the absorber to exchange heat between the absorption liquid flowing from the absorber to the regenerator and the absorption liquid flowing from the regenerator to the absorber. In an absorption refrigerator in which a heat exchanger and an evaporator are connected through piping, the difference between the temperature of the absorption liquid on the outlet side of the absorber and the temperature of the absorption liquid on the inlet side of the regenerator, and the temperature difference between the cold water inlet and outlet of the evaporator. Absorption refrigeration characterized by comprising: a control device that calculates a ratio between the two, compares this ratio with a set value, and outputs a signal; and an alarm that operates using a signal from the control device as an input signal. Machine. 2. Absorber, regenerator, heat exchanger installed between the absorber and regenerator to exchange heat between the absorption liquid flowing from the absorber to the regenerator and the absorption liquid flowing from the regenerator to the absorber, and evaporation. In an absorption chiller with pipes connected to each other, calculate the ratio of the difference between the temperature at the absorption liquid inlet side and the temperature at the absorption liquid outlet side of the heat exchanger and the temperature difference between the cold water inlet and outlet of the evaporator, and calculate the ratio between this ratio and the set value. 1. An absorption refrigerating machine comprising: a control device that compares and outputs a signal; and an alarm that operates by inputting a signal from the control device. 3. The absorber, the regenerator, the heat exchanger installed between the regenerator and the absorber, the evaporator, etc. are each connected by piping, and the heat exchanger is installed between the absorber and the regenerator. In an absorption chiller, calculate the ratio between the difference between the absorbent temperature on the inlet side of the heat exchanger and the absorbent liquid temperature on the outlet side and a physical quantity that changes depending on the chilled water load of the evaporator, and calculate the ratio between this ratio and the set value. 1. An absorption refrigerating machine comprising: a control device that compares and outputs a signal; and an alarm that operates by inputting a signal from the control device.
JP23515589A 1989-09-11 1989-09-11 Absorption refrigerator Expired - Fee Related JP2771626B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23515589A JP2771626B2 (en) 1989-09-11 1989-09-11 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23515589A JP2771626B2 (en) 1989-09-11 1989-09-11 Absorption refrigerator

Publications (2)

Publication Number Publication Date
JPH0399168A true JPH0399168A (en) 1991-04-24
JP2771626B2 JP2771626B2 (en) 1998-07-02

Family

ID=16981865

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23515589A Expired - Fee Related JP2771626B2 (en) 1989-09-11 1989-09-11 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JP2771626B2 (en)

Also Published As

Publication number Publication date
JP2771626B2 (en) 1998-07-02

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