JPH0791783A - Trouble diagnosing system for absorption chilled and warm water machine - Google Patents

Trouble diagnosing system for absorption chilled and warm water machine

Info

Publication number
JPH0791783A
JPH0791783A JP23932793A JP23932793A JPH0791783A JP H0791783 A JPH0791783 A JP H0791783A JP 23932793 A JP23932793 A JP 23932793A JP 23932793 A JP23932793 A JP 23932793A JP H0791783 A JPH0791783 A JP H0791783A
Authority
JP
Japan
Prior art keywords
concentration
concentrated liquid
concentrated
cooling water
load
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
JP23932793A
Other languages
Japanese (ja)
Other versions
JP3340814B2 (en
Inventor
Ryuichiro Kawakami
隆一郎 川上
Yasuharu Kuroki
靖治 黒木
Yoshio Ozawa
芳男 小澤
Masahiro Furukawa
雅裕 古川
Taiji Kamata
泰司 鎌田
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.)
Osaka Gas Co Ltd
Sanyo Electric Co Ltd
Original Assignee
Osaka Gas Co Ltd
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 Osaka Gas Co Ltd, Sanyo Electric Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP23932793A priority Critical patent/JP3340814B2/en
Publication of JPH0791783A publication Critical patent/JPH0791783A/en
Application granted granted Critical
Publication of JP3340814B2 publication Critical patent/JP3340814B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide a trouble diagnosing system which can effectively detect an internal malfunction even at the time of a low load in an absorption chilled and warm water machine. CONSTITUTION:A concentration (concentrated liquid) of absorbent liquid to be scattered by an absorber, a coolant inlet temperature, a refrigerating load are detected based on various measured values by a sensor group. A concentrated liquid concentration characteristic calculator 74 of an arithmetic processor previously stores concentrated liquid concentration characteristics for representing a variation in the concentration at the time of a normal operation, and calculates the concentration (suitable concentrated liquid concentration) at the time of the normal operation based on the coolant temperature and a detected value of a refrigerating load. A malfunction degree detector 7 calculates a difference of the detected value of the concentration (evaluated concentrated liquid concentration) and a suitable concentrated liquid concentration, and a trouble diagnosing unit 76 prepares diagnosis data representing a malfunction degree based on the difference, and outputs it.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、吸収式冷凍機に代表さ
れる吸収式冷温水機に関し、特に吸収器にて散布される
吸収液、即ち濃液の濃度に基づいて、各種異常に起因す
る運転能力の低下を検知する故障診断システムに関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption chiller-heater typified by an absorption chiller, and in particular, it is caused by various abnormalities based on the concentration of an absorption liquid, that is, a concentrated liquid sprayed in the absorber. The present invention relates to a failure diagnosis system that detects a decrease in driving ability.

【0002】[0002]

【従来の技術】吸収式冷凍機においては、凝縮器、蒸発
器、吸収器、再生器等を相互に配管接続して1つの冷凍
サイクルが構成される。特に二重効用型の吸収式冷凍機
は冷凍効率が高いため、広く採用されている(例えば特
開昭62-77567号〔F25B15/00〕参照)。
2. Description of the Related Art In an absorption chiller, a condenser, an evaporator, an absorber, a regenerator and the like are connected to each other by piping to form one refrigeration cycle. In particular, double-effect absorption chillers are widely used because of their high refrigeration efficiency (see, for example, JP-A-62-77567 [F25B15 / 00]).

【0003】図1は二重効用型の吸収式冷凍機の構成を
示しており、凝縮器(11)及び低温再生器(12)からなる上
胴(1)、蒸発器(21)及び吸収器(22)からなる下胴(2)、
バーナ(31)を内蔵した高温再生器(3)、高温熱交換器
(4)、低温熱交換器(5)等が相互に配管接続されてい
る。
FIG. 1 shows the structure of a double-effect type absorption refrigerator. The upper body (1) is composed of a condenser (11) and a low temperature regenerator (12), an evaporator (21) and an absorber. Lower body (2) consisting of (22),
High temperature regenerator (3) with built-in burner (31), high temperature heat exchanger
(4), the low temperature heat exchanger (5), etc. are connected to each other by piping.

【0004】吸収式冷凍機においては、冷却水の汚れ、
吸収液循環量の異常、真空度の異常等、冷凍機の内部異
常を診断するべく、蒸発器(21)、凝縮器(11)等の各熱交
換ユニットについて、診断時における対数平均温度差Δ
Tと正常運転時における対数平均温度差ΔTsから、下
記数1によって定義される異常度Aを算出し、この異常
度を監視することが行なわれている。
In the absorption refrigerator, the cooling water becomes dirty,
In order to diagnose internal abnormalities of the refrigerator such as abnormal absorption liquid circulation volume and vacuum degree, logarithmic mean temperature difference Δ at the time of diagnosis for each heat exchange unit such as evaporator (21) and condenser (11)
From T and the logarithmic average temperature difference ΔTs during normal operation, an abnormality degree A defined by the following equation 1 is calculated and this abnormality degree is monitored.

【0005】[0005]

【数1】A=(ΔT−ΔTs)/ΔTs## EQU1 ## A = (ΔT−ΔTs) / ΔTs

【0006】ところで、吸収式冷凍機においては、何ら
かの内部異常が発生すると、冷凍効率が低下する結果、
吸収器にて散布される吸収液、即ち濃液の濃度が上昇す
ることになる。濃液濃度が一定値を越えると、吸収液の
結晶化等、重大な障害を招く。そこで、吸収式冷凍機に
は、濃液濃度を監視して、濃液濃度が一定値を越える
と、冷凍機の運転を停止させる安全装置が装備されてい
る。
By the way, in the absorption refrigerator, if any internal abnormality occurs, the refrigeration efficiency is lowered,
The concentration of the absorption liquid, that is, the concentrated liquid, which is sprayed by the absorber, increases. When the concentration of the concentrated liquid exceeds a certain value, it causes serious troubles such as crystallization of the absorbing liquid. Therefore, the absorption chiller is equipped with a safety device that monitors the concentration of the concentrated liquid and stops the operation of the refrigerator when the concentration of the concentrated liquid exceeds a certain value.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、濃液濃
度は冷凍負荷や他の運転状態に応じて変動し、例えば定
負荷時には低い値を示していたとしても、冷凍負荷が急
激に増大すると、これに応じて濃液濃度が急上昇し、運
転停止に至ることなる。この様に突然に運転が停止する
と、その復旧期間は負荷の高い時期であるにも拘わら
ず、冷凍機が全く機能せず、大きな問題を招来する。こ
こで、上述の異常度の監視によって内部状態の異常を予
知せんとしても、異常度の変化率は冷凍負荷に依存し、
高負荷状態に比べて低負荷状態では、その変化が顕著に
現われない。従って、低負荷状態では、冷凍機内部の異
常を的確に検出することが困難である。
However, the concentration of the concentrated liquid fluctuates depending on the refrigerating load and other operating conditions, and even if it shows a low value at a constant load, if the refrigerating load rapidly increases, As a result, the concentration of the concentrated liquid sharply rises and the operation is stopped. When the operation is suddenly stopped in this way, the refrigerator does not function at all even though the restoration period is a period when the load is high, which causes a serious problem. Here, even if the abnormality of the internal state is not predicted by monitoring the degree of abnormality described above, the rate of change of the degree of abnormality depends on the refrigeration load,
The change does not significantly appear in the low load state as compared with the high load state. Therefore, in the low load state, it is difficult to accurately detect the abnormality inside the refrigerator.

【0008】本発明の目的は、低負荷時であっても内部
の異常を的確に検出することが出来る故障診断システム
を提供することである。又、本発明の他の目的は、内部
異常の検出に基づいて、濃液濃度に関する運転の余裕度
を定量的に認識し、負荷を制限する等の対策を講じるこ
とが出来る故障診断システムを提供することである。
An object of the present invention is to provide a failure diagnosis system capable of accurately detecting an internal abnormality even when the load is low. Another object of the present invention is to provide a failure diagnosis system capable of quantitatively recognizing the operating margin regarding the concentration of concentrated liquid based on the detection of an internal abnormality and taking measures such as limiting the load. It is to be.

【0009】[0009]

【課題を解決する為の手段】本発明に係る吸収式冷温水
機の第1の故障診断システムは、吸収器にて散布される
吸収液の濃度(濃液濃度)、該吸収液の冷却に関与する冷
却水の温度、及び冷凍負荷を検出する検出手段と、冷凍
負荷を変数、冷却水温度をパラメータとして、正常運転
時における濃液濃度の変化を表わす濃液濃度特性が、予
め格納されている記憶手段と、冷却水温度と冷凍負荷の
検出値に基づいて、前記記憶手段から正常運転時の濃液
濃度(適正濃液濃度)を導出する濃度導出手段と、濃液濃
度の検出値(評価濃液濃度)と前記適正濃液濃度の差を算
出すると共に、該濃度差に基づいて、異常の程度を表わ
す診断データを作成して出力する診断処理手段とを具え
ている。
A first failure diagnosis system for an absorption chiller-heater according to the present invention is provided for the concentration of the absorbing liquid (concentration of concentrated liquid) dispersed in the absorber and the cooling of the absorbing liquid. The detection means for detecting the temperature of the cooling water and the refrigeration load involved, and the concentration characteristic of the concentrated liquid representing the change of the concentrated liquid concentration during the normal operation with the cooling load as a variable and the cooling water temperature as a parameter are stored in advance. Based on the detected value of the cooling water temperature and the refrigeration load, the concentration derivation means for deriving the concentrated concentration of the normal operation (proper concentrated concentration) from the storage means, and the detected value of the concentrated concentration ( A diagnostic processing means is provided for calculating a difference between the evaluation concentrated liquid concentration) and the proper concentrated liquid concentration, and for producing and outputting diagnostic data indicating the degree of abnormality based on the concentration difference.

【0010】又、本発明に係る第2の故障診断システム
は、上記検出手段、記憶手段、及び濃度導出手段に加え
て、濃液濃度の検出値(評価濃液濃度)と前記適正濃液濃
度の差を算出すると共に、該濃度差分だけ、前記記憶手
段に格納されている濃液濃度特性をシフトすることによ
って、濃液濃度の最大許容値を限度とする現在の運転能
力の余裕度を算出する演算手段を具えている。
In addition to the detection means, the storage means, and the concentration derivation means, the second failure diagnosis system according to the present invention is further provided with a detection value of the concentration of concentrated liquid (evaluated concentration of concentrated liquid) and the proper concentration of concentrated liquid. Is calculated, and the concentration characteristic of the concentrated liquid stored in the storage means is shifted by the concentration difference to calculate the margin of the current driving capacity within the maximum allowable concentration of the concentrated liquid. It is equipped with a calculation means for performing.

【0011】具体的構成において、上記演算手段は、シ
フトされた濃液濃度特性に基づいて、冷却水温度がその
検出値に保持されたまま冷凍負荷が増大したときの濃液
濃度の変化を求め、該濃液濃度がその最大許容値に達す
ることとなる冷凍負荷の上限値を導出し、該上限値を最
大運転能力として、現在の運転能力の余裕度を算出する
ものである。
In a concrete configuration, the calculating means obtains a change in the concentration of the concentrated liquid when the refrigeration load increases while the temperature of the cooling water is held at the detected value, based on the shifted characteristic of the concentration of the concentrated liquid. The upper limit value of the refrigerating load at which the concentrated concentration reaches the maximum allowable value is derived, and the upper limit value is used as the maximum operating capacity to calculate the margin of the current operating capacity.

【0012】[0012]

【作用】先ず本発明に係る吸収式冷温水機の故障診断の
原理について、図3及び図4に基づいて説明する。真空
度異常や冷却水の汚れ等、吸収式冷凍機に生じる殆どの
異常状態は、最終的には、吸収液の濃度が上昇する現象
となって現われる。従って、正常運転状態における吸収
液の濃度の適正値が判明していれば、吸収液の濃度を異
常状態の監視パラメータとして用いることが出来る。特
に、吸収器にて散布される吸収液の濃度(濃液濃液)の上
昇は、結晶の発生等、運転停止を招く内部異常の直接の
要因となり得るため、異常の検出には、濃液濃度を用い
ることが適当である。
First, the principle of failure diagnosis of the absorption chiller-heater according to the present invention will be described with reference to FIGS. 3 and 4. Most abnormal states that occur in the absorption refrigerator such as abnormal vacuum degree and contamination of cooling water finally appear as a phenomenon in which the concentration of the absorbing liquid increases. Therefore, if the proper value of the concentration of the absorbing liquid in the normal operation state is known, the concentration of the absorbing liquid can be used as a monitoring parameter for the abnormal state. In particular, an increase in the concentration of the absorbing liquid (concentrated liquid concentrated liquid) sprayed in the absorber can be a direct cause of internal abnormalities such as the occurrence of crystals that cause operation stop. It is appropriate to use a concentration.

【0013】吸収液濃度の適正値は冷凍負荷及び冷却水
温度に依存する。図3は、冷凍機が正常に運転されてい
る状態における濃液濃度の変化特性を、冷凍負荷及び冷
却水入口温度をパラメータとしてプロットしたものであ
る。図示の如く、冷却水入口温度を一定に保った場合、
冷凍負荷と濃液濃度の間には一義的な関数関係が成立す
る。そこで、予め図4の如く正常運転状態における濃液
濃度の変化を、冷凍負荷を変数、冷却水入口温度をパラ
メータとする濃度特性曲線に表わす。そして、該特性曲
線に基づいて、濃液濃度の検出値(評価濃液濃度)と適正
濃度濃液の差を算出すれば、該濃度差の大小が内部異常
の程度を表わすことになる。
The appropriate value of the absorption liquid concentration depends on the refrigeration load and the cooling water temperature. FIG. 3 is a plot of the characteristics of changes in the concentration of the concentrated liquid when the refrigerator is operating normally, with the refrigeration load and the cooling water inlet temperature as parameters. As shown, if the cooling water inlet temperature is kept constant,
A unique functional relationship holds between the refrigeration load and the concentration of the concentrated liquid. Therefore, as shown in FIG. 4, a change in the concentration of the concentrated liquid in the normal operation state is shown in advance in a concentration characteristic curve using the refrigeration load as a variable and the cooling water inlet temperature as a parameter. Then, if the difference between the detected value of concentrated liquid concentration (evaluated concentrated liquid concentration) and the appropriate concentrated liquid concentration is calculated based on the characteristic curve, the magnitude of the concentration difference indicates the degree of internal abnormality.

【0014】又、該濃度差分だけ図4の濃液濃度特性を
シフトすれば、異常発生状態における濃液濃度特性が得
られる。例えば図4に点P′で示す様に、冷凍負荷が略
50%での濃液濃度の検出値(評価濃液濃度)が62%、
冷却水入口温度が28℃であったとすると、そのときの
適正濃液濃度は点Pで示すように略58%である。従っ
て、評価濃液濃度と適正濃液濃度の差dDsだけ、28
℃のときの濃度特性曲線P−Qをシフトして、異常発生
状態における特性曲線P′−Q′を得る。そして、該特
性曲線P′−Q′が、濃液濃度の最大許容値(運転許容
限界濃度)Ds_maxのレベルと交差する点Q′にお
ける冷凍負荷Lc_eを、その異常発生状態での運転能
力限界値に設定する。従って、運転能力限界値Lc_e
と冷凍負荷の検出値Lcの差dLcが運転能力の余裕度
を表わすことになる。
Further, by shifting the concentrated liquid concentration characteristic of FIG. 4 by the concentration difference, the concentrated liquid concentration characteristic in the abnormal state can be obtained. For example, as shown by point P ′ in FIG. 4, the detected value of the concentrated liquid concentration (evaluated concentrated liquid concentration) when the refrigeration load is approximately 50% is 62%
Assuming that the cooling water inlet temperature is 28 ° C., the appropriate concentrated liquid concentration at that time is about 58% as indicated by the point P. Therefore, only the difference dDs between the evaluation concentrated liquid concentration and the proper concentrated liquid concentration is 28
The concentration characteristic curve P-Q at the temperature of ° C is shifted to obtain the characteristic curve P'-Q 'in the abnormal state. Then, the refrigerating load Lc_e at the point Q'where the characteristic curve P'-Q 'intersects with the level of the maximum permissible value of concentration of concentrated liquid (operating permissible limit concentration) Ds_max is changed to the operating capacity limit value in the abnormal state. Set to. Therefore, the driving capacity limit value Lc_e
And the difference dLc between the detection value Lc of the refrigeration load and the refrigeration load represent the margin of the operating capacity.

【0015】本発明に係る故障診断システムは上記考察
から生れたものであって、上記第1の故障診断システム
においては、各種センサーや推定演算によって濃度濃
度、冷却水温度、及び冷凍負荷が直接に測定され、或い
は推定によって算出される。記憶手段には図4に示す如
き濃液濃度特性が関数化されて格納されており、冷却水
温度と冷凍負荷の検出値に基づいて、正常運転時の濃液
濃度(適正濃液濃度)Ds_nが導出される。そして、濃
液濃度の検出値(評価濃液濃度)Ds_mと前記適正濃液
濃度Ds_nの差dDsを算出し、該濃度差の大小に応
じて、異常の程度を表わす診断データ、例えば“正常”
“やや異常”“異常”が作成される。
The failure diagnosis system according to the present invention is derived from the above consideration. In the first failure diagnosis system, the concentration and concentration, the cooling water temperature, and the refrigeration load are directly measured by various sensors and estimation calculations. Measured or calculated by estimation. The concentrated liquid concentration characteristic as shown in FIG. 4 is stored in the storage means as a function, and the concentrated liquid concentration (adequate concentrated liquid concentration) Ds_n during normal operation is stored based on the detected values of the cooling water temperature and the refrigeration load. Is derived. Then, the difference dDs between the detected value of concentrated liquid concentration (evaluated concentrated liquid concentration) Ds_m and the proper concentrated liquid concentration Ds_n is calculated, and diagnostic data indicating the degree of abnormality, for example, “normal”, is calculated according to the magnitude of the concentration difference.
An "abnormal" or "abnormal" is created.

【0016】又、上記第2の故障診断システムにおいて
は、更に図4の濃液濃度特性を濃度差dDsだけシフト
することによって、異常状態における濃液濃度特性を作
成し、これに基づいて、濃液濃度の最大許容値を限度と
する現在の運転能力の余裕度が算出される。
Further, in the second failure diagnosis system, the concentrated liquid concentration characteristic in the abnormal state is created by further shifting the concentrated liquid concentration characteristic of FIG. 4 by the concentration difference dDs, and based on this, the concentrated liquid concentration characteristic is created. The margin of the current driving capacity within the maximum allowable liquid concentration is calculated.

【0017】[0017]

【発明の効果】本発明に係る吸収式冷温水機の故障診断
システムによれば、低負荷時であっても濃液濃度の正常
値と検出値の差に基づいて、内部異常が的確に検出され
る。又、内部異常の検出に基づいて、濃液濃度に関する
運転の余裕度が定量的に認識されるから、異常発生時に
は、負荷を制限する等の対策を講じることによって、冷
温水機の異常停止を回避出来る。
According to the failure diagnosing system for the absorption chiller-heater according to the present invention, the internal abnormality can be accurately detected based on the difference between the normal value and the detected value of the concentrated concentration even when the load is low. To be done. In addition, since the operation margin regarding the concentration of concentrated liquid is quantitatively recognized based on the detection of internal abnormality, when abnormalities occur, measures such as limiting the load can be taken to stop the chiller-heater abnormally. It can be avoided.

【0018】[0018]

【実施例】以下、本発明を二重効用型の吸収式冷凍機に
実施した一例につき、図面に沿って詳述する。図1に示
す如く吸収式冷凍機は、冷媒として水、吸収液として臭
化リチウム(LiBr)溶液を用いたもので、凝縮器(11)
及び低温再生器(12)からなる上胴(1)、蒸発器(21)及び
吸収器(22)からなる下胴(2)、バーナ(31)を内蔵した高
温再生器(3)、高温熱交換器(4)、低温熱交換器(5)等
を相互に配管接続して構成されている。尚、これら複数
の機器の媒体入出力部には、必要なセンサー(図示省略)
が取り付けられており、後述の各種物理量が測定され
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An example in which the present invention is applied to a double-effect absorption refrigerator is described below in detail with reference to the drawings. As shown in FIG. 1, the absorption refrigerator uses water as a refrigerant and lithium bromide (LiBr) solution as an absorption liquid, and a condenser (11)
And an upper body (1) including a low temperature regenerator (12), a lower body (2) including an evaporator (21) and an absorber (22), a high temperature regenerator (3) including a burner (31), and high temperature heat The exchanger (4), the low temperature heat exchanger (5) and the like are connected to each other by piping. In addition, necessary sensors (not shown) are installed in the medium input / output unit of these multiple devices.
Is attached, and various physical quantities described later are measured.

【0019】クーリングタワー(図示省略)から供給され
る温度の低い冷却水は、先ず吸収器(22)を通過した後、
凝縮器(11)を通過し、これによって温度が上昇した冷却
水は再びクーリングタワーへ戻される。又、室内ユニッ
ト(図示省略)からの温度の高い冷水は蒸発器(21)を通過
し、これによって冷却された温度の低い冷水が室内ユニ
ットへ供給される。
Cooling water having a low temperature supplied from a cooling tower (not shown) first passes through the absorber (22) and then
The cooling water, which has passed through the condenser (11) and the temperature of which has risen, is returned to the cooling tower again. Further, cold water having a high temperature from the indoor unit (not shown) passes through the evaporator (21), and cold water having a low temperature cooled by this is supplied to the indoor unit.

【0020】図2は、本発明に係る故障診断システムの
構成を示している。センサー群(6)は、低温再生器(12)
の温度Ts_hi、凝縮器(11)の凝縮温度Tv_con
d、吸収器(22)の冷却水入口温度Tco_in、冷却水
中間温度Tco_mid、冷却水出口温度Tco_ou
t、蒸発器(21)の冷水出口温度Tc_out、冷水入口
温度Tc_in、冷水流量Vc等を夫々測定するための
圧力計、温度計、流量計を具えている。
FIG. 2 shows the configuration of the failure diagnosis system according to the present invention. The sensor group (6) is a low temperature regenerator (12).
Temperature Ts_hi, condensation temperature Tv_con of the condenser (11)
d, cooling water inlet temperature Tco_in of the absorber (22), cooling water intermediate temperature Tco_mid, cooling water outlet temperature Tco_ou
t, a cold water outlet temperature Tc_out of the evaporator (21), a cold water inlet temperature Tc_in, a cold water flow rate Vc, and the like, respectively, and a pressure gauge, a thermometer, and a flow meter are provided.

【0021】演算処理回路(7)はマイクロコンピュータ
によって構成され、4つの計算部(71)(72)(74)(77)の
他、推定部(73)、検出部(75)及び診断部(76)を具えてい
る。濃液濃度推定部(73)は、低温再生器温度Ts_hi
及び凝縮温度Tv_condから、下記数2に基づいて
濃液濃度の推定値Ds(%)を算出するものである。尚、
該算出式は実験式であって、精度の良い推定式として知
られている。
The arithmetic processing circuit (7) is composed of a microcomputer, and in addition to the four calculation units (71), (72), (74) and (77), the estimation unit (73), the detection unit (75) and the diagnosis unit ( 76). The concentrated liquid concentration estimation unit (73) determines the low temperature regenerator temperature Ts_hi.
And the condensing temperature Tv_cond, the estimated value Ds (%) of the concentrated liquid concentration is calculated based on the following equation 2. still,
The calculation formula is an empirical formula and is known as an accurate estimation formula.

【0022】[0022]

【数2】 Ds=(Ts_hi+280.0)×139.0/(Tv_cond+273.0)−102.4[Formula 2] Ds = (Ts_hi + 280.0) × 139.0 / (Tv_cond + 273.0) −102.4

【0023】冷凍負荷計算部(71)は、冷水流量Vc、冷
水出口温度Tc_out及び冷水入口温度Tc_inか
ら、下記数3に基づいて冷凍負荷Lcを算出する。
The refrigerating load calculating unit (71) calculates the refrigerating load Lc from the cold water flow rate Vc, the cold water outlet temperature Tc_out and the cold water inlet temperature Tc_in based on the following equation 3.

【数3】Lc=Vc(Tc_in−Tc_out)## EQU3 ## Lc = Vc (Tc_in-Tc_out)

【0024】正常時の濃液濃度特性計算部(74)には、図
4の如く冷凍負荷を変数として正常運転時における濃液
濃度の変化を表わす濃液濃度曲線が、複数の異なる冷却
水入口温度をパラメータとして関数化され、格納されて
いる。下記数4は特定の冷却水入口温度における濃液濃
度曲線を2次式で近似したものである。
As shown in FIG. 4, the normal concentrated liquid concentration characteristic calculation unit (74) has a plurality of different cooling water inlets each having a concentrated liquid concentration curve representing a change in the concentrated liquid concentration during normal operation with the refrigeration load as a variable. The function is stored with the temperature as a parameter. The following expression 4 is a quadratic approximation of the concentrated liquid concentration curve at a specific cooling water inlet temperature.

【0025】[0025]

【数4】Ds=a×Lc2+b×Lc+c ここで、定数a、b及びcは、図3のグラフに示す実測
値に最小二乗法を適用することによって決定される。
## EQU4 ## Ds = a × Lc 2 + b × Lc + c Here, the constants a, b and c are determined by applying the least squares method to the actual measurement values shown in the graph of FIG.

【0026】濃液濃度特性計算部(74)は、冷凍負荷計算
部(71)から送られてくる冷凍負荷Lcと、センサー群
(6)から送られてくる冷却水入口温度Tco_inに基
づいて、正常運転時の濃液濃度を算出する。この際、パ
ラメータにない冷却水入口温度に関しては、補間処理に
よって正確な濃液濃度が算出される。
The concentrated liquid concentration characteristic calculation unit (74) includes a refrigeration load Lc sent from the refrigeration load calculation unit (71) and a sensor group.
Based on the cooling water inlet temperature Tco_in sent from (6), the concentration of concentrated liquid during normal operation is calculated. At this time, for the cooling water inlet temperature which is not included in the parameters, an accurate concentrated liquid concentration is calculated by the interpolation process.

【0027】異常の程度検出部(75)は、前記濃液濃度の
推定値Dsを評価濃液濃度Ds_m、前記濃液濃度特性
計算部(74)の算出値を適正濃液濃度Ds_nとして、下
記数5に基づいて、両者の濃度差dDsを算出する。
The abnormality level detection unit (75) uses the estimated value Ds of the concentrated liquid concentration as an evaluation concentrated liquid concentration Ds_m and the calculated value of the concentrated liquid concentration characteristic calculation unit (74) as an appropriate concentrated liquid concentration Ds_n, Based on Equation 5, the density difference dDs between the two is calculated.

【0028】[0028]

【数5】dDs=Ds_m−Ds_n## EQU00005 ## dDs = Ds_m-Ds_n

【0029】そして、濃度差dDsの大小に応じ、次の
様に診断データを作成し、必要に応じて表示し或いはプ
リントアウトする。 dDs<t1 :“正常” t1<dDs<t2:“やや異常” t2<dDs :“異常” ここで、t1及びt2は予め設定された定数である。
Then, diagnostic data is created as follows according to the magnitude of the density difference dDs, and is displayed or printed out as necessary. dDs <t1: “normal” t1 <dDs <t2: “slightly abnormal” t2 <dDs: “abnormal” where t1 and t2 are preset constants.

【0030】又、運転余裕度計算部(77)は、上記濃度差
dDsだけ図4に実線で示す濃液濃度特性をシフトし
て、鎖線でその一部を示す様に異常発生時の濃液濃度特
性を作成する。即ち、前記数4に表わされた濃液濃度特
性曲線に濃度差dDsを加算して、下記数6の如き濃液
濃度曲線を得る。
Further, the operation allowance calculation unit (77) shifts the concentrated liquid concentration characteristic shown by the solid line in FIG. 4 by the above-mentioned concentration difference dDs, and the concentrated liquid at the time of abnormality occurrence is shown as a part of it by the chain line. Create concentration characteristics. That is, the concentration difference dDs is added to the concentration characteristic curve of the concentrated liquid expressed by the equation 4 to obtain a concentrated concentration curve of the following equation 6.

【0031】[0031]

【数6】Ds′=a×Lc2+b×Lc+c+dDs## EQU6 ## Ds' = a × Lc 2 + b × Lc + c + dDs

【0032】運転余裕度計算部(77)は、数6によって計
算される濃液濃度の値が運転許容限界濃度Ds_max
に達することとなる限界の冷凍負荷Lc_eを求め、必
要に応じて、この値Lc_e、或いは運転能力限界値L
c_eとの差dLcを、運転の余裕度として出力する。
The operation allowance calculator (77) determines that the concentration value of the concentrated liquid calculated by the equation 6 is the operation allowable limit concentration Ds_max.
The refrigerating load Lc_e that reaches the limit is calculated, and if necessary, this value Lc_e or the operating capacity limit value L
The difference dLc from c_e is output as the driving margin.

【0033】運転余裕度計算部(77)から得られる冷凍負
荷の限界値Lc_eはガス入量制御部(8)へ送出され、
該限界値Lc_eと、冷凍負荷の定格値Lc_max
と、ガス入量の定格値Gas_maxから、下記数7に
基づいて、ガス入量の最大値Gasを決定する。
The refrigeration load limit value Lc_e obtained from the operation allowance calculation unit (77) is sent to the gas inlet amount control unit (8),
The limit value Lc_e and the rated value Lc_max of the refrigeration load
Then, the maximum value Gas of the gas amount is determined from the rated value Gas_max of the gas amount based on the following equation 7.

【0034】[0034]

【数7】 Gas<Gas_max×Lc_e/Lc_max## EQU00007 ## Gas <Gas_max × Lc_e / Lc_max

【0035】そして、この値Gasに基づいて高温再生
器(3)のバーナ(31)へのガス入量が制限される。従っ
て、外部から要求される冷凍負荷が限界値Lc_eを上
回ったとしても、冷凍機の出力は限界値Lc_eに制限
され、濃液濃度が運転許容限界濃度Ds_maxに達す
ることはない。
The amount of gas entering the burner (31) of the high temperature regenerator (3) is limited based on this value Gas. Therefore, even if the refrigeration load requested from the outside exceeds the limit value Lc_e, the output of the refrigerator is limited to the limit value Lc_e, and the concentrated concentration does not reach the operation allowable limit concentration Ds_max.

【0036】更に図2の演算処理回路(7)においては、
各種故障診断指標計算部(72)が設けられており、センサ
ー群(6)から送られてくる各種測定に基づいて、故障診
断の指標となるデータ、例えば前述の異常度A等が算出
される。これらの指標は故障診断部(76)へ送られ、前記
正常時と異常時の濃液濃度差dDsと併せて故障診断の
対象とされる。これによって、濃液濃度の異常上昇の原
因、例えば真空異常、冷却水汚れ、冷媒に対する吸収液
の混入等が究明されることになる。
Further, in the arithmetic processing circuit (7) of FIG.
Various failure diagnosis index calculation units (72) are provided, and data serving as an index for failure diagnosis, such as the above-mentioned abnormality degree A, is calculated based on various measurements sent from the sensor group (6). . These indexes are sent to the failure diagnosis section (76), and are subjected to failure diagnosis together with the concentrated liquid concentration difference dDs between the normal state and the abnormal state. As a result, the cause of the abnormal increase in the concentration of the concentrated liquid, for example, the abnormal vacuum, the contamination of the cooling water, the mixing of the absorbing liquid with the refrigerant, etc. will be investigated.

【0037】上述の如く本発明に係る故障診断システム
によれば、低負荷時であっても正常時と異常時の濃液濃
度差dDsに基づいて、内部異常が的確に検出される。
又、内部異常の検出に基づいて、運転の余裕度が定量的
に認識されるから、異常発生時には、負荷を制限するこ
とによって、冷凍機の異常停止を未然に回避することが
出来る。更に、濃液濃度差dDsを異常度等の他の指標
と組み合わせることによって、より高度な故障診断が可
能となる。
As described above, according to the failure diagnosis system of the present invention, the internal abnormality can be accurately detected based on the concentrated liquid concentration difference dDs between the normal state and the abnormal state even when the load is low.
Further, since the operational margin is quantitatively recognized based on the detection of the internal abnormality, when the abnormality occurs, the load can be limited to prevent the abnormal stop of the refrigerator. Furthermore, by combining the concentration difference dDs of the concentrated liquid with other indexes such as the degree of abnormality, it is possible to perform more advanced failure diagnosis.

【0038】上記実施例の説明は、本発明を説明するた
めのものであって、特許請求の範囲に記載の発明を限定
し、或は範囲を減縮する様に解すべきではない。又、本
発明の各部構成は上記実施例に限らず、特許請求の範囲
に記載の技術的範囲内で種々の変形が可能であることは
勿論である。例えば図3に示す濃液濃度特性を表わす
際、パラメータとしては冷却水入口温度以外に、冷却水
中間温度或いは冷却水出口温度を採用することも可能で
ある。
The above description of the embodiments is for explaining the present invention, and should not be construed as limiting the invention described in the claims or reducing the scope. The configuration of each part of the present invention is not limited to the above-mentioned embodiment, and it goes without saying that various modifications can be made within the technical scope described in the claims. For example, when expressing the concentration characteristic of concentrated liquid shown in FIG. 3, it is possible to adopt not only the cooling water inlet temperature but also the cooling water intermediate temperature or the cooling water outlet temperature as a parameter.

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

【図1】本発明を実施すべき吸収式冷凍機の構成図であ
る。
FIG. 1 is a configuration diagram of an absorption refrigerator according to the present invention.

【図2】本発明に係る故障診断システムのブロック図で
ある。
FIG. 2 is a block diagram of a failure diagnosis system according to the present invention.

【図3】冷却水入口温度及び冷凍負荷をパラメータとし
て濃液濃度の実測値をプロットしたグラフである。
FIG. 3 is a graph in which measured values of concentrated liquid concentration are plotted with the cooling water inlet temperature and the refrigeration load as parameters.

【図4】上記濃液濃度特性を関数化したグラフである。FIG. 4 is a graph in which the concentration characteristic of the concentrated liquid is made into a function.

【符号の説明】[Explanation of symbols]

(1) 上胴 (11) 凝縮器 (12) 低温再生器 (2) 下胴 (21) 蒸発器 (22) 吸収器 (3) 高温再生器 (6) センサー群 (7) 演算処理回路 (8) ガス入量制御部 (1) Upper body (11) Condenser (12) Low temperature regenerator (2) Lower body (21) Evaporator (22) Absorber (3) High temperature regenerator (6) Sensor group (7) Arithmetic processing circuit (8) ) Gas charge control unit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小澤 芳男 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (72)発明者 古川 雅裕 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 (72)発明者 鎌田 泰司 大阪府守口市京阪本通2丁目18番地 三洋 電機株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshio Ozawa 2-18 Keihanhondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd. (72) Inventor Masahiro Furukawa 2-18th Keihanhondori, Moriguchi-shi, Osaka Sanyo Denki Incorporated (72) Inventor Yasushi Kamata 2-18 Keihan Hondori, Moriguchi City, Osaka Sanyo Electric Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 吸収器にて散布される吸収液の濃度(濃
液濃液)、該吸収液の冷却に関与する冷却水の温度、及
び冷凍負荷を検出する検出手段と、 冷凍負荷及び冷却水温度を変数として、正常運転時にお
ける濃液濃度の変化を表わす濃液濃度特性が、予め格納
されている記憶手段と、 冷却水温度と冷凍負荷の検出値に基づいて、前記記憶手
段から正常運転時の濃液濃度(適正濃液濃度)を導出する
濃度導出手段と、 濃液濃度の検出値(評価濃液濃度)と前記適正濃液濃度の
差を算出すると共に、該濃度差に基づいて、異常の程度
を表わす診断データを作成して出力する診断処理手段と
を具えた吸収式冷温水機の故障診断システム。
1. A detection means for detecting the concentration of the absorbing liquid (concentrated liquid concentrated liquid) dispersed in the absorber, the temperature of cooling water involved in cooling the absorbing liquid, and the refrigerating load, and the refrigerating load and cooling. Using the water temperature as a variable, the concentrated liquid concentration characteristics that represent changes in the concentrated liquid concentration during normal operation are stored in advance and stored in the storage device based on the detected values of the cooling water temperature and the refrigeration load. Concentration deriving means for deriving the concentration of concentrated liquid during operation (proper concentration of concentrated liquid), calculating the difference between the detected value of concentration of concentrated liquid (evaluated concentration of concentrated liquid) and the appropriate concentration of concentrated liquid, and based on the difference in concentration. And a diagnostic processing means for producing and outputting diagnostic data representing the degree of abnormality, and a failure diagnostic system for an absorption chiller-heater.
【請求項2】 吸収器にて散布される吸収液の濃度(濃
液濃液)、該吸収液の冷却に関与する冷却水の温度、及
び冷凍負荷を検出する検出手段と、 冷凍負荷を変数、冷却水温度をパラメータとして、正常
運転時における濃液濃度の変化を表わす濃液濃度特性
が、予め格納されている記憶手段と、 冷却水温度と冷凍負荷の検出値に基づいて、前記記憶手
段から正常運転時の濃液濃度(適正濃液濃度)を導出する
濃度導出手段と、 濃液濃度の検出値(評価濃液濃度)と前記適正濃液濃度の
差を算出すると共に、該濃度差分だけ、前記記憶手段に
格納されている濃液濃度特性をシフトすることによっ
て、濃液濃度の最大許容値を限度とする現在の運転能力
の余裕度を算出する演算手段とを具えた吸収式冷温水機
の故障診断システム。
2. A detection means for detecting the concentration of the absorbing liquid (concentrated liquid concentrated liquid) dispersed in the absorber, the temperature of cooling water involved in cooling the absorbing liquid, and the refrigerating load, and the refrigerating load as a variable. , The concentration means for expressing the concentration of the concentrated liquid in the normal operation using the cooling water temperature as a parameter is stored in advance, and the storage means is based on the detected values of the cooling water temperature and the refrigerating load. Concentration deriving means for deriving the concentration of concentrated liquid during normal operation (appropriate concentration of concentrated liquid), calculating the difference between the detected value of concentrated concentration (evaluated concentration of concentrated liquid) and the appropriate concentration of concentrated liquid, and calculating the concentration difference The absorption-type cold temperature including a calculation means for calculating the margin of the current operating capacity within the maximum allowable value of the concentrated concentration by shifting the concentrated concentration characteristic stored in the storage means. Water machine failure diagnosis system.
【請求項3】 演算手段は、シフトされた濃液濃度特性
に基づいて、冷却水温度がその検出値に保持されたまま
冷凍負荷が増大したときの濃液濃度の変化を求め、該濃
液濃度がその最大許容値に達することとなる冷凍負荷の
上限値を導出し、該上限値を最大運転能力とする現在の
運転能力の余裕度を算出する請求項2に記載の故障診断
システム。
3. The calculating means obtains, based on the shifted concentrated liquid concentration characteristic, a change in the concentrated liquid concentration when the refrigeration load increases while the cooling water temperature is held at the detected value, and the concentrated liquid concentration is changed. The fault diagnosis system according to claim 2, wherein an upper limit value of the refrigerating load at which the concentration reaches the maximum allowable value is derived, and a margin of the current operating capacity with the upper limit value as the maximum operating capacity is calculated.
JP23932793A 1993-09-27 1993-09-27 Absorption chiller / heater fault diagnosis system Expired - Fee Related JP3340814B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23932793A JP3340814B2 (en) 1993-09-27 1993-09-27 Absorption chiller / heater fault diagnosis system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23932793A JP3340814B2 (en) 1993-09-27 1993-09-27 Absorption chiller / heater fault diagnosis system

Publications (2)

Publication Number Publication Date
JPH0791783A true JPH0791783A (en) 1995-04-04
JP3340814B2 JP3340814B2 (en) 2002-11-05

Family

ID=17043077

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23932793A Expired - Fee Related JP3340814B2 (en) 1993-09-27 1993-09-27 Absorption chiller / heater fault diagnosis system

Country Status (1)

Country Link
JP (1) JP3340814B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008151461A (en) * 2006-12-19 2008-07-03 Chofu Seisakusho Co Ltd Air conditioner
US10628804B2 (en) 2016-05-20 2020-04-21 Panasonic Intellectual Property Management Co., Ltd. Degradation estimation method and degradation estimation apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008151461A (en) * 2006-12-19 2008-07-03 Chofu Seisakusho Co Ltd Air conditioner
JP4726081B2 (en) * 2006-12-19 2011-07-20 株式会社長府製作所 Air conditioner
US10628804B2 (en) 2016-05-20 2020-04-21 Panasonic Intellectual Property Management Co., Ltd. Degradation estimation method and degradation estimation apparatus

Also Published As

Publication number Publication date
JP3340814B2 (en) 2002-11-05

Similar Documents

Publication Publication Date Title
JPH0791783A (en) Trouble diagnosing system for absorption chilled and warm water machine
JP3253190B2 (en) Cooling water flow rate estimation method for absorption chiller / heater
JP3054553B2 (en) Absorption chiller / heater failure diagnosis device
JP6940983B2 (en) Performance diagnosis device and performance diagnosis method for absorption chillers
JP3083930B2 (en) Failure diagnosis system for absorption refrigerator
JP2902946B2 (en) Abnormality determination device for absorption type water heater
JP2909368B2 (en) Cooling water dirt diagnosis system for absorption chiller / heater
JP3083929B2 (en) Failure diagnosis system for absorption refrigerator
JP3083931B2 (en) Failure diagnosis system for absorption refrigerator
JP3253189B2 (en) Diagnosis system for damper opening of absorption chiller / heater
JP3054554B2 (en) Abnormality detector for absorption type water heater
JPH07234048A (en) Trouble diagnostic system for absorption type water cooling and heating machine
JP3253211B2 (en) Absorption chiller / heater fault diagnosis system
JP3054552B2 (en) Absorption chiller / heater failure diagnosis device
JP3195085B2 (en) Absorption refrigerator
JP7022658B2 (en) Performance diagnosis system for absorption chillers
JP3058677B2 (en) Absorption refrigerator
JP2810430B2 (en) Absorption refrigerator protection device
JPH0447568Y2 (en)
KR100317155B1 (en) Fault diagnosis system of absorption chiller
JPH07324851A (en) Malfunction detecting method for heat exchanger and absorption type hot and chilled water generator
JPH06159871A (en) Absorption type refrigerating machine
JPS6365258A (en) Efficiency lowering annunciator for absorption refrigerator
JPH06159852A (en) Absorption type freezer
JPH05203297A (en) Operation abnormality detection device for absorption refrigerator

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20020730

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080816

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080816

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090816

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090816

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100816

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110816

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110816

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120816

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120816

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130816

Year of fee payment: 11

LAPS Cancellation because of no payment of annual fees