JPH0796978B2 - Absorption refrigerator operation monitoring device - Google Patents
Absorption refrigerator operation monitoring deviceInfo
- Publication number
- JPH0796978B2 JPH0796978B2 JP28472188A JP28472188A JPH0796978B2 JP H0796978 B2 JPH0796978 B2 JP H0796978B2 JP 28472188 A JP28472188 A JP 28472188A JP 28472188 A JP28472188 A JP 28472188A JP H0796978 B2 JPH0796978 B2 JP H0796978B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- difference
- condenser
- refrigerant
- absorption
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】 〈産業上の利用分野〉 本発明は吸収冷凍機や吸収ヒートポンプ装置など(以
下、吸収冷凍機という)の運転監視装置の改良に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION <Field of Industrial Application> The present invention relates to an improvement of an operation monitoring device for an absorption refrigerating machine, an absorption heat pump device and the like (hereinafter referred to as an absorption refrigerating machine).
〈従来の技術〉 吸収冷凍機の運転監視の従来の技術として、吸収冷凍機
の凝縮器において互いに熱交換する一方の流体である冷
却水の出入口温度およびこの冷却水と熱交換する他方の
流体である冷媒の出口温度、すなわち凝縮冷媒の温度を
検出し、これらの検出温度から所定の汚れ状態を推定す
るデータに基いて、凝縮器の伝熱管の汚れ状態を第3図
に示すように算出し、これを表示する手段(特公昭61−
15993号公報参照)がある。なお、第3図は汚れ状態の
算出方法をグラフにして表示した図であり、この図にお
いて、T1は冷却水入口温度、T2は冷却水出口温度、T3は
凝縮冷媒温度を表わし、また、縦軸は温度(℃)、横軸
は冷凍能力(%)を表わしており、汚れa2を示す破線よ
りも上方のゾーン(赤ゾーン)は汚れのひどい状態、汚
れa1を示す一点鎖線よりも下方のゾーン(青ゾーン)は
汚れの少ない状態、これらの中間ゾーン(黄ゾーン)は
ひどい汚れではないもののかなりの汚れのある状態を表
わしている。また、右下方向に傾斜させた実線は冷却水
の出・入口温度の差と冷凍能力との関係を示したグラフ
である。<Prior art> As a conventional technology for operation monitoring of an absorption refrigeration machine, the inlet / outlet temperature of cooling water, which is one fluid that exchanges heat with each other in a condenser of an absorption refrigeration machine, and the other fluid that exchanges heat with this cooling water are used. The outlet temperature of a certain refrigerant, that is, the temperature of the condensed refrigerant is detected, and based on the data for estimating the predetermined fouling state from these detected temperatures, the fouling state of the heat transfer tube of the condenser is calculated as shown in FIG. , Means for displaying this (Japanese Patent Publication Sho 61-
15993). It is to be noted that FIG. 3 is a graph showing a method of calculating the dirty state, in which T 1 is the cooling water inlet temperature, T 2 is the cooling water outlet temperature, and T 3 is the condensed refrigerant temperature. The vertical axis represents temperature (° C) and the horizontal axis represents refrigerating capacity (%). The zone (red zone) above the broken line showing dirt a 2 is in a state of severe dirt, and one point shows dirt a 1. The zone below the chain line (blue zone) represents a less dirty state, and the middle zone (yellow zone) represents a less dirty but considerably dirty state. The solid line inclined to the lower right is a graph showing the relationship between the difference between the inlet and outlet temperatures of cooling water and the refrigerating capacity.
そして、この従来の手段においては、冷却水出入口温度
差が〔T2−T1〕であった場合、その矢印線と前記実線と
の交点を起点として、温度差〔T2−T1〕に対応する冷凍
能力QYを求める。一方、凝縮冷媒温度と冷却水出口温度
とを検出し、その温度差が例えば〔T3−T2〕である場
合、その矢印線と冷凍能力QYの矢印線との交点PYを求
め、汚れの状態が黄ゾーンにあることを表示するように
なっている。Then, in this conventional means, when the cooling water inlet / outlet temperature difference is [T 2 −T 1 ], the temperature difference [T 2 −T 1 ] is set with the intersection of the arrow line and the solid line as the starting point. Find the corresponding refrigeration capacity Q Y. On the other hand, detects a condensation refrigerant temperature and the cooling water outlet temperature, in which case the temperature difference is, for example, [T 3 -T 2], to obtain the intersection P Y with arrows and the arrows refrigerating capacity Q Y, It indicates that the dirt condition is in the yellow zone.
〈発明が解決しようとする課題〉 上記した従来の手段においては、吸収冷凍機の冷凍能力
が小さくなるにつれて汚れの状態を示すゾーンが狭くな
る(第3図参照)ため、検出温度にわずかの誤差があっ
ても実際の汚れの状態とは異なる表示をしやすいという
問題点がある。例えば、冷凍能力QYのときの交点PYで示
されている汚れ状態が実際のそれである場合に、冷房負
荷が1/4に減って冷凍能力をQY1/4のQXに減らしたとき検
出温度〔T3−T2〕が0.5〜0.25℃の範囲になければ実際
の汚れの状態と異なる表示、すなわち赤ゾーンもしくは
青ゾーンの表示がなされていることになる。<Problems to be Solved by the Invention> In the above-mentioned conventional means, as the refrigerating capacity of the absorption refrigerating machine becomes smaller, the zone showing the state of dirt becomes narrower (see FIG. 3). However, there is a problem in that a display different from the actual state of dirt can be easily displayed. For example, if the stain state at the intersection P Y when the refrigerating capacity Q Y is real with it, the refrigerating capacity was reduced to Q X of Q Y 1/4 cooling load is reduced to 1/4 If the detected temperature [T 3 −T 2 ] is not within the range of 0.5 to 0.25 ° C, a display different from the actual stain state, that is, a red zone or a blue zone is displayed.
本発明は、この問題点に鑑み、汚れの状態を従来のもの
よりも正しく把握することの可能な装置の提供を目的と
したものである。The present invention has been made in view of this problem, and an object thereof is to provide an apparatus capable of grasping the state of dirt more correctly than the conventional apparatus.
〈課題を解決するための手段〉 本発明は、吸収冷凍機の冷水出入口温度差△TEの計測器
と、吸収冷凍機の凝縮器の冷媒温度TRと冷却水出口温度
TCの差〔TR−TC〕の計測器と、これらの信号を受けつつ
△TEに対する〔TR−TC〕の比率を算出する演算器と、算
出した比率〔TR−TC〕/△TEを汚れ指数として表示する
表示器と、汚れ指数としてプリントアウトするプリンタ
ーにより吸収冷凍機の運転監視装置を構成したものであ
る。<Means for Solving the Problems> The present invention provides a measuring device for the cold water inlet / outlet temperature difference ΔT E of an absorption refrigerator, a refrigerant temperature T R and a cooling water outlet temperature of a condenser of the absorption refrigerator.
Measuring device for the difference in T C [T R −T C ], an arithmetic unit that calculates the ratio of [T R −T C ] to ΔT E while receiving these signals, and a calculated ratio [T R −T C The operation monitoring device for the absorption chiller is composed of an indicator that displays C ] / ΔT E as a dirt index and a printer that prints out as a dirt index.
〈作 用〉 吸収冷凍機の凝縮器の伝熱管の汚れと前記の温度差〔TR
−TC〕とは関係があり、汚れがひどくなるほどこの温度
差が大きくなる。一方、この温度差は、冷水負荷と比例
関係にあり、一定の冷水流量の場合に吸収冷凍機の冷水
出入口温度差△TEに比例する。したがって、温度差〔TR
−TC〕の大小のみで凝縮器の伝熱管の汚れの程度を正し
く把握することはできないものの、この汚れの程度は△
TEと温度差〔TR−TC〕との比率に関係していることが分
かる。<Operation> Dirt on the heat transfer tube of the condenser of the absorption refrigerator and the temperature difference [T R
-T C ], the temperature difference increases as the dirt gets worse. On the other hand, this temperature difference is proportional to the cold water load, and is proportional to the cold water inlet / outlet temperature difference ΔT E of the absorption refrigerator in the case of a constant cold water flow rate. Therefore, the temperature difference [T R
Although it is not possible to accurately grasp the degree of contamination of the heat transfer tube of the condenser only by the magnitude of −T C ], the degree of contamination is
It can be seen that it is related to the ratio of T E to the temperature difference [T R −T C ].
そして、実験によれば、凝縮器の伝熱管の汚れの程度が
一定である場合、冷水負荷の大小にかかわらず、〔TR−
TC〕/△TEの値は第2図に示すようにほぼ一定であるこ
とが確認された。かつまた、〔TR−TC〕/△TEが大きく
なるほど汚れがひどくなっていることも確認された。Then, according to experiments, when the degree of fouling of the heat transfer tube of the condenser is constant, regardless of the cold water load, [T R -
It was confirmed that the value of T C ] / ΔT E was almost constant as shown in FIG. It was also confirmed that the larger [T R −T C ] / ΔT E was, the more severe the stain was.
本発明の装置においては、〔TR−TC〕/△TEを算出する
ことによって、冷水負荷が小さい場合にも凝縮器の伝熱
管の汚れの程度を正しく把握することが可能である。In the device of the present invention, by calculating [T R −T C ] / ΔT E , it is possible to correctly grasp the degree of fouling of the heat transfer tube of the condenser even when the cold water load is small.
〈実施例〉 第1図は本発明による吸収冷凍機の一実施例を示した概
略構成説明図である。第1図において、Aは吸収冷凍機
であり、この吸収冷凍機は高温発生器1、低温発生器
2、凝縮器3、蒸発器4、吸収器5、低温、高温溶液熱
交換器6,7、冷媒用ポンプPRおよび溶液用ポンプPAを冷
媒用管路8,9、冷媒液流下用管路10、冷媒液還流用管路1
1,12、稀溶液用管路13,14、中間濃度の溶液用管路15,16
および濃溶液用管路17,18で接続して冷媒(水)と溶液
(臭化リチウム水溶液)の循環路を形成している。な
お、19は手動弁VB付きの冷媒ブロー用管路である。<Embodiment> FIG. 1 is a schematic structural explanatory view showing an embodiment of an absorption refrigerator according to the present invention. In FIG. 1, A is an absorption refrigerator, which is a high temperature generator 1, a low temperature generator 2, a condenser 3, an evaporator 4, an absorber 5, a low temperature high temperature solution heat exchanger 6,7. , The refrigerant pump P R and the solution pump P A are connected to the refrigerant lines 8 and 9, the refrigerant liquid flow-down line 10, and the refrigerant liquid recirculation line 1.
1,12, pipelines for dilute solution 13,14, pipelines for medium concentration solution 15,16
And the concentrated solution pipes 17 and 18 are connected to form a circulation path for the refrigerant (water) and the solution (lithium bromide aqueous solution). In addition, 19 is a refrigerant blow pipe line with a manual valve V B.
20は高温発生器1の燃焼加熱室、21,21…は燃焼ガス用
通路、22は燃焼ガス用排気路、23は低温発生器2の加熱
器、24は凝縮器3の冷却器、25は蒸発器4の熱交換器、
26は吸収器5の冷却器であり、Bは高温発生器1に備え
たバーナーである。20 is a combustion heating chamber of the high temperature generator 1, 21, 21 ... are combustion gas passages, 22 is a combustion gas exhaust passage, 23 is a low temperature generator 2 heater, 24 is a condenser 3 cooler, and 25 is Heat exchanger of the evaporator 4,
Reference numeral 26 is a cooler of the absorber 5, and B is a burner provided in the high temperature generator 1.
FはバーナーBと接続した燃料供給路、27,28は熱交換
器25と接続した冷水用管路であり、29,30,31は冷却器2
6,24を直列に接続した冷却水用管路である。F is a fuel supply passage connected to the burner B, 27 and 28 are cold water pipes connected to the heat exchanger 25, and 29, 30 and 31 are coolers 2
This is a cooling water pipeline in which 6,24 are connected in series.
VFは燃料供給路Fで配備した制御弁、S1,S2は冷水出入
口の温度センサー、SLは冷却水出口の温度センサー、SR
は凝縮器3の冷媒の温度センサーである。V F is a control valve installed in the fuel supply path F, S 1 and S 2 are temperature sensors at the cold water inlet / outlet, S L is a temperature sensor at the cooling water outlet, and S R
Is a temperature sensor for the refrigerant of the condenser 3.
MEは温度センサーS1,S2と電気的に接続されている計測
器で、これにより冷水入口温度から冷水出口温度を差引
いた温度差△TEが計測される。またMCは温度センサー
SR,SCと電気的に接続されている計測器で、これにより
凝縮器3の冷媒温度TRから冷却水出口温度TCを差引いた
温度差〔TR−TC〕が計測される。かつまた、Jは計測器
MC,MEと接続されているマイクロコンピュータ内蔵の演
算器で、これにより温度差△TEに対する温度差〔TR−
TC〕の比率KXが算出される。Skは演算器Jのセット部で
ある。ここで算出された比率KXは汚れ指数とし、表示器
Hに表示される他プリンターCVにプリントアウトされ
る。M E is a measuring instrument electrically connected to the temperature sensors S 1 and S 2, and this measures a temperature difference ΔT E obtained by subtracting the cold water outlet temperature from the cold water inlet temperature. M C is a temperature sensor
A measuring device electrically connected to S R and S C , which measures the temperature difference [T R −T C ] obtained by subtracting the cooling water outlet temperature T C from the refrigerant temperature T R of the condenser 3. . And again, J is a measuring instrument
M C, a microcomputer built-in calculator, which is connected to the M E, thereby the temperature difference with respect to the temperature difference △ T E [T R -
The ratio K X of T C ] is calculated. S k is a set part of the computing unit J. The ratio K X calculated here is used as a stain index and is printed out on the other printer C V displayed on the display H.
プリントアウト例を第4図に示す。An example of printout is shown in FIG.
なおまた、温度センサーSRは管路10に備えるようにして
も良い。さらにまた、センサーSRを温度センサーの代り
に圧力センサーに置き換えても良い。この場合、冷媒の
飽和蒸気気圧に相当する飽和温度を算出することによっ
て冷媒温度を求め得る。The temperature sensor S R may be provided in the conduit 10. Furthermore, the sensor S R may be replaced with a pressure sensor instead of the temperature sensor. In this case, the refrigerant temperature can be obtained by calculating the saturation temperature corresponding to the saturated vapor pressure of the refrigerant.
上述のような構成の運転監視装置を備えた吸収冷凍機A
においては、凝縮器3の伝熱管の汚れが殆んどない場
合、KXは例えば0.5に近い値となり(第2図参照)、汚
れが大きくなるに従ってKXも大となる。Absorption refrigerator A equipped with the operation monitoring device configured as described above
In the above, in the case where the heat transfer tube of the condenser 3 is hardly contaminated, K X becomes a value close to, for example, 0.5 (see FIG. 2), and as the contamination becomes larger, K X also becomes larger.
そして、実験によれば、凝縮器3の伝熱管に銅管を用い
た場合、その汚れがひどいときの△TEに対する〔TR−
TC〕の値は0.7以上であった。According to the experiment, when a copper tube is used as the heat transfer tube of the condenser 3, [T R − with respect to ΔT E when the contamination is severe
The value of T C ] was 0.7 or more.
従って運転管理者は汚れ指数を表示器で見るか、プリン
ターからプリントされたものを見ることにより伝熱管の
汚れ具合を知ることが可能となった。Therefore, it became possible for the operation manager to know the degree of contamination of the heat transfer tube by looking at the stain index on the display or by looking at the printed matter from the printer.
その結果、運転管理者は伝熱管の洗浄を適正に行うこと
が可能となる。As a result, the operation manager can properly clean the heat transfer tubes.
〈発明の効果〉 以上の通り、本発明によれば、負荷の大小に拘わらず、
表示器を確認するか、プリンターからのプリントを確認
することにより吸収冷凍機の凝縮器の伝熱管の汚れの状
態を正確に把握することができ、その洗浄時期を適正に
決めることができるので、伝熱管の汚れ過ぎに伴なう吸
収冷凍機の運転効率低下の防止効果がもたらさらされ
る。かつまた、洗浄する必要のない時期に吸収冷凍機の
運転を停止することに伴なうその稼動率低下を防止する
効果ももたらされる。<Effects of the Invention> As described above, according to the present invention, regardless of the magnitude of the load,
By checking the display or the print from the printer, you can accurately grasp the state of dirt on the heat transfer tube of the condenser of the absorption refrigerator, and you can properly decide the cleaning time, The effect of preventing the operation efficiency of the absorption refrigerator from lowering due to excessive fouling of the heat transfer tube is brought about. Moreover, there is an effect of preventing a decrease in the operating rate of the absorption refrigerating machine, which is caused by stopping the operation of the absorption refrigerating machine at a time when the cleaning is not necessary.
第1図は本発明の一実施例としての運転監視装置を備え
た吸収冷凍機の概略構成説明図、第2図は凝縮器の冷媒
温度と冷却水出口温度との差の冷水出入口温度差に対す
る比率と、冷水負荷との関係を表わした線図、第3図は
従来の手段における伝熱管の汚れ状態の算出方法をグラ
フにして表わした図、第4図は汚れ指数のプリントアウ
ト図である。 ……吸収冷凍機、1……高温発生器、3……凝縮器、4
……蒸発器、S1,S2,SR,SC……温度検出器、MC,ME……計
測器、J……判定器、SK……セット部、H……表示器、
CV……プリンター。FIG. 1 is a schematic configuration explanatory view of an absorption refrigerating machine equipped with an operation monitoring device as an embodiment of the present invention, and FIG. FIG. 3 is a graph showing the relationship between the ratio and the cold water load, FIG. 3 is a graph showing the method of calculating the dirt state of the heat transfer tube in the conventional means, and FIG. 4 is a printout drawing of the dirt index. . ... Absorption refrigerator, 1 ... High temperature generator, 3 ... Condenser, 4
…… Evaporator, S 1 , S 2 , S R , S C …… Temperature detector, M C , M E …… Measuring instrument, J …… Judgement unit, S K …… Set unit, H …… Display unit ,
C V …… Printer.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岸本 哲郎 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 金子 敏之 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 宮城 龍雄 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 (56)参考文献 特開 昭56−146966(JP,A) 特開 昭63−70055(JP,A) 特開 平1−123959(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tetsuro Kishimoto 2-18 Keihanhondori, Moriguchi City, Osaka Sanyo Electric Co., Ltd. (72) Toshiyuki Kaneko 2-18th Keihanhondori, Moriguchi City, Osaka Sanyo Denki Incorporated (72) Inventor Tatsuo Miyagi 2-18 Keihanhondori, Moriguchi-shi, Osaka Sanyo Electric Co., Ltd. (56) Reference JP-A-56-146966 (JP, A) JP-A-63-70055 (JP) , A) JP-A-1-123959 (JP, A)
Claims (1)
その差を計る冷水温度差計測器と吸収冷凍機の凝縮器の
冷媒温度および冷却水出口温度を検出しつつその差を計
る温度差計測定器と、これら計測器の信号を受けつつ冷
水温度差に対する凝縮器の冷媒温度と冷却水出口温度と
の差の比率を算出する演算器と、この比率を汚れ指数と
して表示する表示器あるいは上記比率を汚れ指数として
プリントアウトするプリンターとから構成されているこ
とを特徴とした吸収冷凍機の運転監視装置。1. A chilled water temperature difference measuring device for detecting a cold water inlet / outlet temperature of an absorption chiller while measuring the difference between the chilled water temperature measuring device and a refrigerant temperature of a condenser of the absorption chiller and a cooling water outlet temperature for measuring the difference. Meter, a calculator that calculates the ratio of the difference between the refrigerant temperature of the condenser and the outlet temperature of the cooling water with respect to the cold water temperature difference while receiving the signals of these measuring devices, and an indicator that displays this ratio as a dirt index or An operation monitor of an absorption refrigerating machine, comprising: a printer that prints out using the above ratio as a dirt index.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28472188A JPH0796978B2 (en) | 1988-11-10 | 1988-11-10 | Absorption refrigerator operation monitoring device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28472188A JPH0796978B2 (en) | 1988-11-10 | 1988-11-10 | Absorption refrigerator operation monitoring device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02130363A JPH02130363A (en) | 1990-05-18 |
| JPH0796978B2 true JPH0796978B2 (en) | 1995-10-18 |
Family
ID=17682122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28472188A Expired - Lifetime JPH0796978B2 (en) | 1988-11-10 | 1988-11-10 | Absorption refrigerator operation monitoring device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0796978B2 (en) |
-
1988
- 1988-11-10 JP JP28472188A patent/JPH0796978B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02130363A (en) | 1990-05-18 |
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