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JP3058677B2 - Absorption refrigerator - Google Patents
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JP3058677B2 - Absorption refrigerator - Google Patents

Absorption refrigerator

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Publication number
JP3058677B2
JP3058677B2 JP2329270A JP32927090A JP3058677B2 JP 3058677 B2 JP3058677 B2 JP 3058677B2 JP 2329270 A JP2329270 A JP 2329270A JP 32927090 A JP32927090 A JP 32927090A JP 3058677 B2 JP3058677 B2 JP 3058677B2
Authority
JP
Japan
Prior art keywords
temperature
refrigerant
absorber
evaporator
cooling water
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 - Fee Related
Application number
JP2329270A
Other languages
Japanese (ja)
Other versions
JPH04203778A (en
Inventor
吉旦 岸
和夫 大沢
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP2329270A priority Critical patent/JP3058677B2/en
Publication of JPH04203778A publication Critical patent/JPH04203778A/en
Application granted granted Critical
Publication of JP3058677B2 publication Critical patent/JP3058677B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Sorption Type Refrigeration Machines (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、吸収式冷凍機における、故障診断,予防保
全,経年劣化予想,保守指標、及び内部サイクル変化の
検出による保守全般の監視手法に関する機器保全手段に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a monitoring method for overall maintenance of an absorption chiller by detecting a failure, a preventive maintenance, an aging prediction, a maintenance index, and an internal cycle change. Equipment maintenance means.

〔従来の技術〕[Conventional technology]

従来の運転監視システムは、内部サイクルポイント点
の温度を検知し、蒸気表や、デューリング線図からサイ
クルポイントの溶液濃度を計算し、その時点での、冷
水,冷却水,入熱量を検出し、その条件に於ける理論濃
度数値を算出、比較判定するシステムであったが、測定
ポイントが多く、システム的に複雑であり、実用化への
問題が多く、測定ポイントの決定や、汎用性等より、よ
り簡潔に、対応,検出出来る管理指標として、本発明の
保守管理指標は、機械の性能維持が目的であるため、性
能面に大きく影響を及ぼす点の変位量を検出し、正常値
を比較する事でその目的が達せられる。このため、伝熱
性能の偏位量を定量的に検出する方法として、冷水出口
温度と、冷媒温度の温度差を冷水系伝熱性能の指数と
し、冷却水系を、冷却水出口温度と、吸収器溶液出口温
度の温度差をその指数としてとらえる事にした。この結
果、内部温度検出部位は二点であり、外部系統で二点の
計四点で、保守管理指標の目的は達せられる。
The conventional operation monitoring system detects the temperature at the internal cycle point, calculates the solution concentration at the cycle point from the steam table and the During diagram, and detects the cold water, cooling water, and heat input at that time. , A system that calculates and compares theoretical concentration values under these conditions, but has many measurement points, is complex in terms of system, and has many problems for practical use. Determination of measurement points, versatility, etc. As a management index that can be more easily handled and detected, the maintenance management index of the present invention is intended to maintain the performance of the machine. The purpose is achieved by comparison. Therefore, as a method for quantitatively detecting the deviation amount of the heat transfer performance, the difference between the chilled water outlet temperature and the refrigerant temperature is used as an index of the chilled water heat transfer performance, and the cooling water system is set to the cooling water outlet temperature and the absorption. The temperature difference between the temperature of the solution outlet of the vessel was taken as the index. As a result, the internal temperature detection site is two points, and the external system has two points, for a total of four points, so that the purpose of the maintenance management index can be achieved.

なお、この種のものとして例えば特開昭63−297990号
公報があげられる。
Incidentally, as this kind, for example, JP-A-63-297990 can be mentioned.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

従来、吸収式冷凍機の保守、及び故障時の原因解明等
に当っては、日常の運転日誌え、運転具の感覚にたよっ
ていた他、運転時間,起動回数等により、判断,判定し
ていた。また、吸収式冷凍機の異常性は、外部から目標
や感触により断定する事が極めて難しいため、場合によ
っては、分解や開放、時には、本体を切開する事で、状
況の把握をし、判定を下す事もある。
Conventionally, in the maintenance of absorption chillers and the elucidation of the cause at the time of failure, etc., in addition to relying on daily operation diaries and feelings of driving tools, judgments and judgments are made based on operation time, number of startups, and the like. Was. In addition, since it is extremely difficult to determine the abnormality of the absorption chiller from the outside based on the target and feel, in some cases, disassembly, opening, and sometimes opening the main body to grasp the situation and make a judgment. Sometimes I do.

本発明は、内部サイクルと、冷水・冷却水温度の相関
性に視点を置きサイクル温度の変化や、変位量、又は偏
差を検出する事により、機械の異常性,保守点検の時期
などを知らせる他、故障に関係する場合は、検出記録の
チェックで、その異常の発生時期を知る事が出来る。
The present invention is based on the correlation between the internal cycle and the cooling water / cooling water temperature, and detects a change in the cycle temperature, a displacement amount, or a deviation, thereby notifying the abnormality of the machine, the timing of maintenance and the like, and the like. In the case of a failure, the time of occurrence of the abnormality can be known by checking the detection record.

本発明は、保守点検及びチューブ洗浄,清掃時期を決
定する指標とする事を目的とする他、冷媒の物性変化
や、スプレー状況の変化等を知らせる吸収式冷凍機を提
供することを目的とする。
An object of the present invention is to provide an absorption type refrigerator for notifying a change in physical properties of a refrigerant, a change in a spraying state, and the like, in addition to being used as an index for determining maintenance inspection, tube cleaning, and cleaning time. .

〔課題を解決するための手段〕[Means for solving the problem]

吸収式冷凍機は、伝熱管の管内の汚れによって大幅な
性能低下が起きる。このため、管内の汚れや、スケール
の付着を取り除く必要がある。
Absorption refrigerators have a significant performance degradation due to dirt in the heat transfer tubes. For this reason, it is necessary to remove dirt in the pipe and adhesion of scale.

吸収器の上部より散布される溶液は、管内の冷却水と
熱交換し、冷却され、冷媒を吸収し低温の希溶液となっ
て吸収器より送り出されるが、この吸収器の出口溶液温
度と、溶液を冷却する冷却水の出口温度は、正常な伝熱
性能をもつ場合は、非常に近似した値を示す。また同様
に、蒸発器の上部より、散布される冷媒は、管内の冷水
と熱交換し、蒸発するが、この時の蒸発滴下した冷媒
は、蒸発圧力の飽和温度に近似した温度であり、冷水の
出口温度との相関性も正常な伝熱性能をもっている場合
は、非常に近い値となる。この相対関係に視点を置き、
伝熱性能の低下を検出する手段として、冷却水出口温度
と吸収器溶液温度を検出し、その温度差を一つの指標と
し、また、冷水出口温度と冷媒スプレー温度を検出し、
その温度差も一つの指標とする。
The solution sprayed from the upper part of the absorber exchanges heat with the cooling water in the tube, is cooled, absorbs the refrigerant, and is sent out from the absorber as a low-temperature dilute solution. The outlet temperature of the cooling water for cooling the solution shows a very similar value when the heat transfer performance is normal. Similarly, the refrigerant sprayed from the upper part of the evaporator exchanges heat with the cold water in the pipe and evaporates. The correlation with the outlet temperature is very close when the heat transfer performance is normal. Focusing on this relative relationship,
As means for detecting a decrease in heat transfer performance, the cooling water outlet temperature and the absorber solution temperature are detected, and the temperature difference is used as one index, and the chilled water outlet temperature and the refrigerant spray temperature are detected,
The temperature difference is also used as one index.

〔作用〕[Action]

吸収式冷凍機の勤収器溶液出口部分と、冷却水出口部
分に温度検出端を設け、差温演算機能をもつマイコン装
置に入力し、異常差温条件を設定しておく事により、警
報を発し、異常伝熱状態を自動検出する。
A temperature detection terminal is provided at the solution outlet of the absorption chiller and at the outlet of the cooling water, and is input to a microcomputer device having a differential temperature calculation function to set an abnormal differential temperature condition, and an alarm is issued. Emit and automatically detect abnormal heat transfer status.

同様の方式で、蒸発器冷媒スプレー導入部分と冷水出
口部分に温度検出端を設け、マイコン装置に入力,差温
条件により異常伝熱状態を自動検出する。
In the same manner, a temperature detection end is provided at the evaporator refrigerant spray introduction part and the chilled water outlet part, and an abnormal heat transfer state is automatically detected based on a temperature difference condition inputted to a microcomputer device.

吸収式冷凍機の内部サイクル状態は、高真空条件下に
於いて、各サイクルポイントは、相関性をもつ温度,圧
力,温度によっている。
In the internal cycle state of the absorption refrigerator, under high vacuum conditions, each cycle point is based on correlated temperature, pressure and temperature.

一方、機械の保守は、性能を維持することが最大の寿
命であり、冷水系,冷却水系の伝熱性能を保つ事であ
る。このため、冷水出口温度と冷媒温度の温度差は、伝
熱性能が低下する事によりその差が大きくなる。同様
に、吸収器出口溶液温度と、冷却水出口温度の温度差
も、伝熱性能が低下する事により大きくなる。この傾向
を利用し、正常範囲を決め、マイコン装置に予め入力し
ておく事で比較演算し、指定範囲を外れた時点で、警報
を発する装置とした。
On the other hand, in the maintenance of the machine, maintaining the performance is the maximum life, and maintaining the heat transfer performance of the chilled water system and the cooling water system. For this reason, the temperature difference between the chilled water outlet temperature and the refrigerant temperature becomes large due to a decrease in heat transfer performance. Similarly, the temperature difference between the solution temperature at the outlet of the absorber and the temperature at the outlet of the cooling water also increases due to a decrease in heat transfer performance. Taking advantage of this tendency, a normal range is determined, a comparison operation is performed by inputting the normal range to a microcomputer device in advance, and an alarm is issued when the specified range is deviated.

〔実施例〕〔Example〕

以下、本発明の一実施例を図面を参照し、説明する。 Hereinafter, an embodiment of the present invention will be described with reference to the drawings.

第1図は、本発明の実施例に係る直焚吸収式冷温水発
生機のサイクル系統図である。
FIG. 1 is a cycle diagram of a direct-fired absorption-type cold / hot water generator according to an embodiment of the present invention.

図に於て、蒸発器1,吸収器2,凝縮器3,高温再生器4,低
温再生器5,熱交換器6などから構成されており、これら
の機器は、溶液ポンプ7,冷却ポンプ8及び配管によって
流路を構成し、冷水9,冷却水10を通水し、冷凍サイクル
を成立させている。
In the figure, the apparatus comprises an evaporator 1, an absorber 2, a condenser 3, a high-temperature regenerator 4, a low-temperature regenerator 5, a heat exchanger 6, and the like. A flow path is constituted by the cooling water 9 and the cooling water 10 to establish a refrigeration cycle.

蒸発器1の伝熱管群上部より散布された冷媒は、管内
を通る冷水9と熱交換し、蒸発し、吸収器2へ流入し、
ここで伝熱管群上部より散布される高温高濃度の溶液に
吸収される。冷媒蒸気を吸収する高温溶液は、管内を通
る冷却水10によって冷却され、低温希溶液となり、溶液
ポンプ7によって熱交換器6を経て、高温再生器4及
び、低温再生器5へ送られ、加熱濃縮され再び熱交換器
6を経て吸収器2の上部に設けられたスプレーダクトに
戻り、管群上部へ散布される。一方、高温再生器4で冷
媒は加熱蒸発し高温冷媒蒸気となって、低温再生器5に
入り、低温再生器5の溶液を加熱し凝縮高温冷媒とな
り、凝縮器3に入る。低温再生器5で蒸発した冷媒蒸気
は、凝縮器3の伝熱管内を通る冷却水10によって冷却さ
れ凝縮し、低温再生器5で凝縮した冷媒と混合され、再
び、蒸発器1に戻り、冷媒ポンプ8によって、管群上部
のスプレーダクトに運ばれ、管群上部からスプレーされ
る。
The refrigerant sprayed from the upper part of the heat transfer tube group of the evaporator 1 exchanges heat with the cold water 9 passing through the tubes, evaporates, flows into the absorber 2,
Here, it is absorbed by the high-temperature and high-concentration solution sprayed from the upper part of the heat transfer tube group. The high-temperature solution that absorbs the refrigerant vapor is cooled by the cooling water 10 passing through the pipe, becomes a low-temperature dilute solution, is sent to the high-temperature regenerator 4 and the low-temperature regenerator 5 via the heat exchanger 6 by the solution pump 7, and is heated. It is concentrated and returns to the spray duct provided at the upper part of the absorber 2 via the heat exchanger 6 again, and is sprayed to the upper part of the tube group. On the other hand, the refrigerant is heated and evaporated in the high-temperature regenerator 4 to become high-temperature refrigerant vapor, enters the low-temperature regenerator 5, heats the solution in the low-temperature regenerator 5, turns into a condensed high-temperature refrigerant, and enters the condenser 3. The refrigerant vapor evaporated in the low-temperature regenerator 5 is cooled and condensed by the cooling water 10 passing through the heat transfer tube of the condenser 3, mixed with the refrigerant condensed in the low-temperature regenerator 5, returned to the evaporator 1, and returned to the evaporator 1 again. By the pump 8, it is conveyed to the spray duct at the upper part of the tube group, and sprayed from the upper part of the tube group.

この様なサイクル構成の中で、まず蒸発器1側の伝熱
性能を監視するため、蒸発器管群上部より滴下して来た
冷媒温度を検出するため、冷媒温度検出端11を設け、演
算マイコン装置15に送信する。一方、冷水9の出口側
に、冷水出口温度検出端12を設け、演算マイコン装置に
送信する。演算マイコン装置15では、送信されて来た各
々の温度をメモリに入れ、温度差温量の演算と、予め入
力されている異常分岐差温値との偏差量を比較させる
他、冷媒温度の上,下限値の監視をさせ異常入力値との
比較演算の結果を出力させ、異常時や、警報を表示とし
て出力させる。
In such a cycle configuration, first, a refrigerant temperature detecting end 11 is provided to monitor the heat transfer performance on the side of the evaporator 1 and to detect the temperature of the refrigerant dropped from the upper part of the evaporator tube group. It is transmitted to the microcomputer device 15. On the other hand, a chilled water outlet temperature detection end 12 is provided on the outlet side of the chilled water 9 and is transmitted to the arithmetic microcomputer device. The arithmetic microcomputer device 15 stores each transmitted temperature in a memory, compares the difference between the calculation of the temperature difference and the difference between the previously input abnormal branch difference temperature, and the temperature of the refrigerant. , Monitor the lower limit value, output the result of the comparison operation with the abnormal input value, and output an error or an alarm as a display.

また、吸収器2側の伝熱性能を監視するため吸収器溶
液出口部に吸収器溶液出口温度検出端13を設ける他、冷
却水10の出口側に、冷却水出口温度検出端4を設け、そ
れぞれ、演算マイコン装置15に送信する。演算マイコン
装置15では、それぞれの温度をメモリに入れ、温度差温
量を演算させ、予め入力されている異常分岐差温値との
偏差量を比較させる他、冷却水出口温度の上限値の監視
をさせ、異常入力値との比較演算の結果を出力させ、異
常時や警報を表示,出力させる。
Further, in addition to providing an absorber solution outlet temperature detecting end 13 at the absorber solution outlet to monitor the heat transfer performance of the absorber 2, a cooling water outlet temperature detecting end 4 is provided at the outlet side of the cooling water 10, Each is transmitted to the arithmetic microcomputer device 15. The arithmetic microcomputer device 15 stores each temperature in a memory, calculates a temperature difference temperature, compares the difference with a previously input abnormal branch difference temperature value, and monitors the upper limit value of the cooling water outlet temperature. To output the result of the comparison operation with the abnormal input value, and display and output an abnormal time and an alarm.

これらの出力表示により保守上の指標とした。 These output displays were used as indicators for maintenance.

〔発明の効果〕〔The invention's effect〕

本発明によって、伝熱管の洗浄又は、清掃の時点が明
確となる他、他の検出モードと組合せる事によって、故
障や、異常性の事前検出,異常事態の回避等に結びつく
他、メンテナンス指標の重要なポイントとなる。
According to the present invention, in addition to clarifying the time of cleaning or cleaning of the heat transfer tube, combining with another detection mode leads to failure, advance detection of anomaly, avoidance of an abnormal situation, and the like, and maintenance index. This is an important point.

この結果 (1)吸収式冷凍機の保守点検サイクルの設定が可能と
なる。
As a result, (1) the maintenance and inspection cycle of the absorption refrigerator can be set.

(2)監視機能の充実により、故障回避,保全の向上に
なる。
(2) By improving the monitoring function, failure avoidance and maintenance are improved.

(3)異常時の解明手段になり、早期対応が図れる。(3) Becomes a means for elucidating abnormalities, and enables early response.

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

第1図は本発明の一実施例の直焚吸収式冷温水発生機の
全体サイクル系統図である。 1……蒸発器、2……吸収器、3……凝縮器、4……高
温再生器、5……低温再生器、6……熱交換器、7……
溶液ポンプ、8……冷媒ポンプ、9……冷水、10……冷
却水、11……冷媒温度検出端、12……冷水出口温度検出
端、13……吸収器溶液出口温度検出端。
FIG. 1 is an overall cycle system diagram of a direct-fired absorption-type cold / hot water generator according to one embodiment of the present invention. DESCRIPTION OF SYMBOLS 1 ... Evaporator, 2 ... Absorber, 3 ... Condenser, 4 ... High temperature regenerator, 5 ... Low temperature regenerator, 6 ... Heat exchanger, 7 ...
Solution pump, 8 ... Refrigerant pump, 9 ... Cold water, 10 ... Cooling water, 11 ... Refrigerant temperature detecting end, 12 ... Cold water outlet temperature detecting end, 13 ... Absorber solution outlet temperature detecting end.

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F25B 49/04 F25B 15/00 Continuation of front page (58) Field surveyed (Int.Cl. 7 , DB name) F25B 49/04 F25B 15/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】冷水が流通する蒸発器と、冷却水が流通す
る吸収器及び凝縮器と、熱源となる再生器と、吸収器に
散布された溶液を前記再生器に送る溶液ポンプと、蒸発
器に貯まった冷媒を蒸発器が有する散布手段に送る冷媒
ポンプとを互いに作動的に接続した吸収式冷凍機におい
て、 前記吸収器を出た溶液の温度を検出する吸収器溶液出口
温度検出手段と、前記吸収器から前記凝縮器を経て流出
した冷却水の温度を検出する冷却水出口温度検出手段
と、検出された吸収器溶液出口温度と冷却水出口温度と
の温度差が予め記憶された温度差の基準値をこえたら異
常と判断し出力するマイコン装置と、前記蒸発器を出た
冷水の温度を検出する冷水出口温度検出手段と、前記蒸
発器から流出する冷媒の温度を検出する冷媒温度検出手
段とを設け、前記マイコン装置は、検出された冷水出口
温度と冷媒温度との第2の温度差が予め記憶された温度
差の基準値を越えたら異常と判断するとともに、検出さ
れた冷媒温度が予め記憶された上限値と下限値の範囲外
であるときにも異常であると判断し、出力することを特
徴とする吸収式冷凍機。
1. An evaporator through which cold water flows, an absorber and a condenser through which cooling water flows, a regenerator as a heat source, a solution pump for sending a solution sprayed on the absorber to the regenerator, An absorption-type refrigerator in which a refrigerant pump for sending a refrigerant stored in an evaporator to a spraying means included in an evaporator is operatively connected to each other, wherein an absorber solution outlet temperature detecting means for detecting a temperature of a solution exiting the absorber; A cooling water outlet temperature detecting means for detecting a temperature of cooling water flowing out of the absorber through the condenser, and a temperature in which a temperature difference between the detected outlet temperature of the absorber solution and the detected temperature of the cooling water outlet is stored in advance. A microcomputer device for determining and outputting an abnormality when the difference exceeds the reference value, a chilled water outlet temperature detecting means for detecting the temperature of the chilled water exiting the evaporator, and a refrigerant temperature for detecting the temperature of the refrigerant flowing out of the evaporator Detection means, The microcomputer device determines that the abnormality is abnormal when the second temperature difference between the detected chilled water outlet temperature and the refrigerant temperature exceeds the reference value of the temperature difference stored in advance, and stores the detected refrigerant temperature in advance. An absorption chiller that determines that an abnormality has occurred even when it is outside the range between the upper limit and the lower limit, and outputs the result.
JP2329270A 1990-11-30 1990-11-30 Absorption refrigerator Expired - Fee Related JP3058677B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2329270A JP3058677B2 (en) 1990-11-30 1990-11-30 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2329270A JP3058677B2 (en) 1990-11-30 1990-11-30 Absorption refrigerator

Publications (2)

Publication Number Publication Date
JPH04203778A JPH04203778A (en) 1992-07-24
JP3058677B2 true JP3058677B2 (en) 2000-07-04

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Family Applications (1)

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JP2329270A Expired - Fee Related JP3058677B2 (en) 1990-11-30 1990-11-30 Absorption refrigerator

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Publication number Publication date
JPH04203778A (en) 1992-07-24

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