JP3384111B2 - Absorption refrigerator - Google Patents

Absorption refrigerator

Info

Publication number
JP3384111B2
JP3384111B2 JP12336794A JP12336794A JP3384111B2 JP 3384111 B2 JP3384111 B2 JP 3384111B2 JP 12336794 A JP12336794 A JP 12336794A JP 12336794 A JP12336794 A JP 12336794A JP 3384111 B2 JP3384111 B2 JP 3384111B2
Authority
JP
Japan
Prior art keywords
hydrogen gas
palladium cell
pressure
absorption refrigerator
alarm
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
JP12336794A
Other languages
Japanese (ja)
Other versions
JPH07332819A (en
Inventor
満嗣 河合
公明 田中
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries 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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP12336794A priority Critical patent/JP3384111B2/en
Publication of JPH07332819A publication Critical patent/JPH07332819A/en
Application granted granted Critical
Publication of JP3384111B2 publication Critical patent/JP3384111B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

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、系内に、水等の冷媒と
共に、これを吸収する臭化リチウム水溶液等の腐食性の
強い溶液を封入した吸収式冷凍機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption type refrigerator in which a highly corrosive solution such as an aqueous solution of lithium bromide which absorbs a refrigerant such as water is enclosed in a system.

【0002】[0002]

【従来の技術】従来、系内に混入する極微量の酸素によ
り各機器や配管の内面に腐食が生じ、この腐食によって
系内に水素ガスが発生し、これが溜ると冷凍能力が低下
してしまうことから、この水素ガスを系外つまり大気に
排出するようにしている。
2. Description of the Related Art Conventionally, an extremely small amount of oxygen mixed in the system causes corrosion on the inner surfaces of various devices and pipes, and this corrosion produces hydrogen gas in the system, which accumulates and reduces the refrigerating capacity. Therefore, this hydrogen gas is discharged to the outside of the system, that is, to the atmosphere.

【0003】この種のものとして、特開平2−2752
62号公報が知られており、このものは、図5に示すよ
うに、気液分離器AとパージタンクBとをもつ抽気装置
Cを設けて、吸収器Dの内部から延設する排気管Eを、
溶液ポンプFの下流側から分岐する分岐管Gとエゼクタ
Hを介して接続し、その合流管Jを気液分離器Aに開放
させ、分離した吸収液は戻し管Kを介して吸収器Dに戻
し、水素ガスはパージタンクBからパラジウムセルLを
介して大気に開放させている。
As this type, Japanese Patent Laid-Open No. 2-2752 is known.
No. 62 publication is known, and as shown in FIG. 5, an exhaust pipe extending from the inside of an absorber D is provided with a bleed device C having a gas-liquid separator A and a purge tank B. E
A branch pipe G branched from the downstream side of the solution pump F is connected via an ejector H, and a confluent pipe J is opened to a gas-liquid separator A, and the separated absorption liquid is passed to a absorber D via a return pipe K. The hydrogen gas is returned to the atmosphere through the purge tank B and the palladium cell L.

【0004】そして、パージタンクBには配管M及びバ
ルブNを介してトラップTを接続しており、このトラッ
プTの内部に、超音波ガス濃度検出器から成る水素濃度
検出器Sを挿入しており、定期的なメンテナンス時に、
この水素濃度検出器Sにより系内の水素ガスの発生量を
測定して腐食の程度を把握し、溶液に予め添加し、腐食
部分に被膜を形成して消費される腐食抑制剤の残存量を
調べ、該腐食抑制剤が不足していると判断したときに
は、新たな腐食抑制剤を系内に追加充填するいった管理
が行えるようになっている。
A trap T is connected to the purge tank B via a pipe M and a valve N, and a hydrogen concentration detector S composed of an ultrasonic gas concentration detector is inserted inside the trap T. And during regular maintenance,
The amount of hydrogen gas generated in the system is measured by the hydrogen concentration detector S to grasp the degree of corrosion, and the residual amount of the corrosion inhibitor consumed by forming a film on the corroded portion by adding it to the solution in advance is calculated. When it is determined that the corrosion inhibitor is insufficient, a control such as additionally filling the system with a new corrosion inhibitor can be performed.

【0005】[0005]

【発明が解決しようとする課題】しかし、以上のもので
は、水素ガスの検出にあたり、配管M及びバルブNを介
してトラップTをわざわざ設けているため、水素ガスの
検出構造が複雑であると共に、そのトラップTの内部に
超音波ガス濃度検出器から成る水素濃度検出器Sを挿入
させて、系内において水素ガスの検出を行っているた
め、系の内外を貫通する部分ができ、系内を完全密封状
態に保持し難く、そのシール部分等から極々微量の空気
が侵入し、腐食を増大させるおそれがある問題もある。
However, in the above, in detecting hydrogen gas, the trap T is purposely provided through the pipe M and the valve N, so that the hydrogen gas detecting structure is complicated and The hydrogen concentration detector S, which is an ultrasonic gas concentration detector, is inserted inside the trap T to detect hydrogen gas in the system, so that a portion penetrating the inside and outside of the system is formed and There is also a problem that it is difficult to maintain a completely sealed state, and an extremely small amount of air may invade from the sealed portion or the like to increase corrosion.

【0006】本発明では、系内で発生する水素ガスを系
外で検出することにより、構造簡易で、しかも系内の密
閉状態を良好に保てながら、水素ガスの検出が行える吸
収式冷凍機を提供することを主目的とする。
In the present invention, by detecting hydrogen gas generated in the system outside the system, an absorption refrigerator having a simple structure and capable of detecting hydrogen gas while maintaining a good sealed state in the system. The main purpose is to provide.

【0007】[0007]

【課題を解決するための手段】そこで、上記主目的を達
成するため、請求項1記載の発明は、図2に示すよう
に、蒸発器1、吸収器2、発生器3,4、及び凝縮器5
を備え、図1に明示するように、系内で発生する水素ガ
スをパラジウムセル101を介して大気に排出するよう
にした吸収式冷凍機において、パラジウムセル101の
出口側に位置する大気中に、排出する水素ガスを検出す
る水素ガス検出手段8を設けた。
In order to achieve the above main object, the invention according to claim 1 is, as shown in FIG. 2, an evaporator 1, an absorber 2, generators 3, 4 and a condenser. Bowl 5
As shown in FIG. 1, in an absorption refrigerating machine in which hydrogen gas generated in the system is discharged to the atmosphere via the palladium cell 101, in an atmosphere located on the outlet side of the palladium cell 101, A hydrogen gas detecting means 8 for detecting the discharged hydrogen gas is provided.

【0008】請求項2記載の発明は、請求項1記載の発
明において、水素ガスの検出精度を上げるため、パラジ
ウムセル101の出口側に、通路の横断面に送風ファン
105を配した通風筒104を設けて、この通風筒10
4における送風ファン105の二次側に、水素ガス検出
手段8を配設した。
The invention according to claim 2 is, in the invention according to claim 1, in order to improve the detection accuracy of hydrogen gas, a ventilation tube 104 having a blower fan 105 arranged on the cross section of the passage on the outlet side of the palladium cell 101. This ventilation tube 10 is provided with
The hydrogen gas detection means 8 was disposed on the secondary side of the blower fan 105 in the No. 4 air conditioner.

【0009】請求項3記載の発明は、請求項1又は請求
項2記載の各発明において、水素ガスの透過に伴うパラ
ジウムセル101の劣化を検出できるようにするため、
パラジウムセル101の入口側の圧力を検出する圧力検
出手段92cを設け、水素ガス検出手段8で検出する水
素ガスの排出速度に対し、圧力検出手段92cで検出す
る内部圧力の上昇速度が所定以上に大きいとき、パラジ
ウムセル101の異常と判定する劣化判定手段108を
設けた。
According to the invention of claim 3, in each of the inventions of claim 1 or 2, the deterioration of the palladium cell 101 due to permeation of hydrogen gas can be detected.
The pressure detecting means 92c for detecting the pressure on the inlet side of the palladium cell 101 is provided, and the rising rate of the internal pressure detected by the pressure detecting means 92c is higher than a predetermined rate with respect to the discharge rate of hydrogen gas detected by the hydrogen gas detecting means 8. When it is large, the deterioration determining means 108 for determining that the palladium cell 101 is abnormal is provided.

【0010】請求項4記載の発明は、請求項3記載の発
明において、パラジウムセル101の交換時期を知るこ
とができるようにするため、劣化判定手段108で異常
を判定したとき、警報を発する警報手段109を設け
た。
According to the invention of claim 4, in the invention of claim 3, in order to know the replacement time of the palladium cell 101, when the deterioration judging means 108 judges an abnormality, an alarm is issued. Means 109 were provided.

【0011】[0011]

【作用】請求項1記載の発明では、系内で発生する水素
ガスは、パラジウムセル101を透過して系外の大気に
排出され、この大気に排出される水素ガスを、パラジウ
ムセル101の出口側に設けた水素ガス検出手段8によ
り検出することにより、系内で発生した水素ガスを検出
することができる。こうして、水素ガス検出手段8は大
気側に設けるため、構造簡易で、しかも、系の内外を貫
通する部分を無くせ、系内の密閉状態を良好に保つこと
ができる。
According to the first aspect of the invention, the hydrogen gas generated in the system passes through the palladium cell 101 and is discharged to the atmosphere outside the system, and the hydrogen gas discharged to the atmosphere is discharged from the outlet of the palladium cell 101. The hydrogen gas generated in the system can be detected by the hydrogen gas detecting means 8 provided on the side. Thus, since the hydrogen gas detecting means 8 is provided on the atmosphere side, the structure is simple, and moreover, the portion penetrating the inside and outside of the system can be eliminated, and the hermetically sealed state in the system can be maintained.

【0012】請求項2記載の発明では、通風筒104の
内部における単位時間あたりの通過ガス量は送風ファン
105による強制送風によりほぼ一定しているから、こ
の通風筒104における送風ファン105の二次側に水
素ガス検出手段8を配設することにより、水素ガスの検
出精度を向上することができる。
According to the second aspect of the present invention, since the amount of passing gas per unit time inside the ventilation tube 104 is substantially constant by the forced air blowing by the ventilation fan 105, the secondary of the ventilation fan 105 in the ventilation tube 104 is secondary. By disposing the hydrogen gas detecting means 8 on the side, the accuracy of detecting hydrogen gas can be improved.

【0013】請求項3記載の発明では、パラジウムセル
101が水素ガスの透過に伴い劣化してくると、水素ガ
スの透過力が落ち、水素ガスの排出がスムーズに行えな
くなる。このため、パラジウムセル101の出口側にお
いて、水素ガス検出手段8で検出する水素ガスの排出速
度に対し、その入口側において、圧力検出手段92cで
検出する内部圧力の上昇速度が所定以上に大きくなる。
そして、これを劣化判定手段108で判定することによ
り、パラジウムセル101の異常を判定することができ
る。
According to the third aspect of the present invention, when the palladium cell 101 deteriorates along with the permeation of hydrogen gas, the permeation power of hydrogen gas decreases and the hydrogen gas cannot be discharged smoothly. Therefore, on the outlet side of the palladium cell 101, the rate of increase of the internal pressure detected by the pressure detecting means 92c on the inlet side becomes higher than a predetermined rate with respect to the discharge rate of hydrogen gas detected by the hydrogen gas detecting means 8. .
Then, by determining this by the deterioration determining means 108, it is possible to determine the abnormality of the palladium cell 101.

【0014】請求項4記載の発明は、劣化判定手段10
8で異常を判定したとき、警報手段109から警報が発
せられるため、パラジウムセル101の交換時期を知る
ことができる。
According to a fourth aspect of the invention, the deterioration determining means 10 is provided.
When the abnormality is determined in 8, an alarm is issued from the alarm means 109, so that the replacement time of the palladium cell 101 can be known.

【0015】[0015]

【実施例】図4に示す吸収式冷凍機は、冷媒液の散布器
12及び冷媒ポンプ13をもち、冷媒を蒸発させて冷水
管11に冷房に用いる冷水を取り出す蒸発器1と、該蒸
発器1と同一容器20内にエリミネータ21を挟んで隣
接状に設けられ、濃溶液の散布器22及び冷却水配管2
3をもち、蒸発器1で蒸発した冷媒を溶液に吸収させる
吸収器2と、該吸収器2と溶液ポンプ25並びに低温熱
交換器26及び高温熱交換器27を介して接続され、バ
ーナー31により吸収器2で多量に冷媒を吸収した稀溶
液から冷媒を発生させる高温側の発生器3、該発生器3
で発生する冷媒蒸気を流す加熱器41をもち、高温側の
発生器3で再生されて高温熱交換器27を通過した後の
中間濃度溶液から冷媒を発生させる低温側の発生器4
と、該低温側の発生器4と同一容器50内に設けられ、
吸収器2の冷却水配管23の後段に連続して設ける冷却
水配管24により各発生器3,4で発生した冷媒蒸気を
凝縮させる凝縮器5とを備えている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The absorption refrigerator shown in FIG. 4 has an evaporator 1 for spraying a refrigerant liquid and a refrigerant pump 13, and an evaporator 1 for evaporating the refrigerant to take out cold water for cooling to a cold water pipe 11, and the evaporator. 1 is provided adjacent to each other in the same container 20 with an eliminator 21 sandwiched therebetween, and a concentrated solution sprayer 22 and a cooling water pipe 2 are provided.
3, an absorber 2 for absorbing the refrigerant evaporated in the evaporator 1 into a solution, the absorber 2 is connected to the solution pump 25, a low temperature heat exchanger 26 and a high temperature heat exchanger 27, and a burner 31 is used. High temperature side generator 3 for generating a refrigerant from a dilute solution in which a large amount of the refrigerant is absorbed by the absorber 2, and the generator 3
The low-temperature generator 4 which has a heater 41 for flowing the refrigerant vapor generated in 1) and which is regenerated by the high-temperature side generator 3 to generate the refrigerant from the intermediate concentration solution after passing through the high-temperature heat exchanger 27.
And provided in the same container 50 as the low temperature side generator 4,
The condenser 2 is provided with a condenser 5 for condensing the refrigerant vapor generated in each of the generators 3 and 4 by a cooling water pipe 24 continuously provided after the cooling water pipe 23 of the absorber 2.

【0016】又、気液分離器91とパージタンク92と
を配管93で連結した抽気装置90を設けており、吸収
器2の内部から延設する排気管94を、溶液ポンプ25
の下流側から分岐する分岐管95の枝管95aとエゼク
タ96aを介して接続し、その合流管96bを気液分離
器91に開放させていると共に、蒸発器1及び凝縮器5
の内部からそれぞれ延設する排気管97a,97bを統
合して、これらを、分岐管95の枝管95bとエゼクタ
98aを介して接続し、その合流管98bを気液分離器
91に開放させており、気液分離器91で分離した吸収
液は戻し管99を介して吸収器2に戻し、水素ガスは配
管93並びにパージタンク92及び接続管92aを経て
パラジウムセル部100から大気に開放させている。
尚、図2において、95cは、冷却水を通す熱交換器で
ある。
Further, there is provided a bleeding device 90 in which a gas-liquid separator 91 and a purge tank 92 are connected by a pipe 93, and an exhaust pipe 94 extending from the inside of the absorber 2 is connected to the solution pump 25.
Is connected to the branch pipe 95a of the branch pipe 95 branching from the downstream side of the pipe via the ejector 96a, and the joining pipe 96b is opened to the gas-liquid separator 91, and the evaporator 1 and the condenser 5 are connected.
The exhaust pipes 97a and 97b extending from the inside of the pipe are integrated and connected to each other via the branch pipe 95b of the branch pipe 95 and the ejector 98a, and the joining pipe 98b is opened to the gas-liquid separator 91. The absorption liquid separated by the gas-liquid separator 91 is returned to the absorber 2 via the return pipe 99, and the hydrogen gas is released from the palladium cell portion 100 to the atmosphere through the pipe 93, the purge tank 92 and the connecting pipe 92a. There is.
In addition, in FIG. 2, 95c is a heat exchanger which lets cooling water pass.

【0017】パラジウムセル部100は、図1に明示す
るように、水素ガスを透過させて排出する板状のパラジ
ウムセル101を備えており、このパラジウムセル10
1は、パージタンク92と接続管92aを介して結ぶ密
閉チャンバー92bの一側開口部に取り付けている。密
閉チャンバー92bは、半割り構造とした本体ケーシン
グ102,103の内部に収容しており、密閉チャンバ
ー92bの中央部には電気ヒータから成るパラジウムセ
ルヒータ106を嵌入させており、このヒータ106に
よりパラジウムセル101を約400℃程度に加熱し、
パラジウムセル101からの水素ガスの排出を促進でき
るようにしている。
As shown in FIG. 1, the palladium cell portion 100 is provided with a plate-shaped palladium cell 101 which allows hydrogen gas to pass through and is discharged.
No. 1 is attached to one side opening of a closed chamber 92b connected to the purge tank 92 via a connection pipe 92a. The closed chamber 92b is housed inside main body casings 102 and 103 having a halved structure, and a palladium cell heater 106 composed of an electric heater is fitted in the central portion of the closed chamber 92b. The cell 101 is heated to about 400 ° C.,
The discharge of hydrogen gas from the palladium cell 101 can be promoted.

【0018】以上の構成において、図1及び図2に示す
ように、パラジウムセル101の出口側に位置する大気
中に、排出する水素ガスの濃度を検出する水素濃度検出
器から成る水素ガス検出手段8を設ける。
In the above structure, as shown in FIGS. 1 and 2, hydrogen gas detecting means comprising a hydrogen concentration detector for detecting the concentration of hydrogen gas discharged into the atmosphere located on the outlet side of the palladium cell 101. 8 is provided.

【0019】具体的には、パラジウムセル101の出口
側に、通路の横断面に送風ファン105を配した矩形筒
形の通風筒104を設けて、この通風筒104における
送風ファン105の二次側に、水素ガス検出手段8を配
設する。送風ファン105は、ファンモータ107によ
り所定の回転数で回転駆動するものである。
Specifically, on the outlet side of the palladium cell 101, there is provided a ventilation pipe 104 having a rectangular tube shape in which a ventilation fan 105 is arranged in the cross section of the passage, and the ventilation pipe 104 has a secondary side of the ventilation fan 105. The hydrogen gas detection means 8 is provided in the. The blower fan 105 is rotationally driven by a fan motor 107 at a predetermined rotation speed.

【0020】そして、パージタンク92に、パラジウム
セル101の入口側の圧力を検出する圧力検出手段92
cを設け(図4参照)、水素ガス検出手段8で検出する
水素ガスの排出速度に対し、圧力検出手段92cで検出
する内部圧力の上昇速度が所定以上に大きいとき、パラ
ジウムセル101の異常と判定する劣化判定手段108
を設けると共に、この劣化判定手段108で異常を判定
したとき、警報ブザーや警報ランプ等により警報を発す
る警報手段109を設ける。
Then, the pressure detecting means 92 for detecting the pressure on the inlet side of the palladium cell 101 in the purge tank 92.
c is provided (see FIG. 4), and when the increase rate of the internal pressure detected by the pressure detection means 92c is higher than a predetermined rate with respect to the discharge rate of hydrogen gas detected by the hydrogen gas detection means 8, it is determined that the palladium cell 101 is abnormal. Deterioration determination means 108 for determination
In addition to the above, an alarm unit 109 is provided for issuing an alarm by an alarm buzzer, an alarm lamp, or the like when the deterioration determining unit 108 determines an abnormality.

【0021】劣化判定手段108は、マイクロコンピュ
ータを用いて構成するものであり、図3に示す手順によ
り処理するものである。
The deterioration determining means 108 is constituted by using a microcomputer, and performs processing according to the procedure shown in FIG.

【0022】先ず、ステップaで、水素ガス検出手段8
により水素濃度を検出し、ステップbで、圧力検出手段
92cによりパージタンク92の圧力を検出する。
First, in step a, the hydrogen gas detecting means 8
The hydrogen concentration is detected by the pressure detecting means 92c, and the pressure in the purge tank 92 is detected by the pressure detecting means 92c in step b.

【0023】続いて、ステップcで、水素ガス検出手段
8による検出濃度から水素ガスの排出量つまり系内で発
生した水素ガス量を求め、前回の水素ガス量に順次積算
していくと共に、前回の水素ガス量と今回の水素ガス量
とから水素ガスの排出速度を算出する。通風筒104に
おける単位時間あたりの通過ガス量は送風ファン105
による強制送風により一定しているから、検出濃度から
通過ガス量に占める水素ガス量を正確に求めることがで
きる。
Then, in step c, the discharge amount of hydrogen gas, that is, the amount of hydrogen gas generated in the system is obtained from the concentration detected by the hydrogen gas detecting means 8, and is sequentially added to the previous amount of hydrogen gas. The discharge rate of the hydrogen gas is calculated from the hydrogen gas amount and the current hydrogen gas amount. The amount of gas passing through the ventilation tube 104 per unit time is determined by the blower fan 105.
Since it is constant by forced air blowing by, the amount of hydrogen gas in the amount of passing gas can be accurately obtained from the detected concentration.

【0024】次に、ステップdで、圧力検出手段92c
による検出圧力から、パージタンク92内の圧力上昇速
度を算出する。
Next, in step d, the pressure detecting means 92c
The pressure rise rate in the purge tank 92 is calculated from the pressure detected by.

【0025】そして、ステップeで、水素ガスの排出速
度に対し、圧力上昇速度が所定以上に大きいとき、ステ
ップfで警報手段109から警報ブザーや警報ランプに
よりアラームを出し、ステップgで、冷凍機の運転を非
常停止させる。
Then, in step e, when the rate of pressure increase is greater than a predetermined rate with respect to the discharge rate of hydrogen gas, an alarm is issued from the alarm means 109 by an alarm buzzer or an alarm lamp in step f, and a refrigerator is operated in step g. Stop the operation of.

【0026】これにより、パラジウムセル101の劣化
を検出でき、新しいパラジウムセル101と交換するこ
とにより、再び、適正な水素ガスの排出を行わせること
ができる。
As a result, the deterioration of the palladium cell 101 can be detected, and by exchanging the palladium cell 101 with a new one, the hydrogen gas can be properly discharged again.

【0027】尚、ステップcによる水素ガス排出量の積
算により、その積算量が所定量を越える場合には、ステ
ップhからステップiを経て、同じく警報手段109に
よりアラームを出し、ステップjで冷凍機の運転を非常
停止させている。これは、系内の腐食の進行が大きく、
水素の発生量が多いことから、回復不能な故障に陥るの
を未然に防止するためである。
If the integrated amount of hydrogen gas discharged in step c exceeds a predetermined amount, an alarm is also issued by the alarm means 109 from step h to step i, and the refrigerator is operated in step j. Has stopped the operation of. This is because the progress of corrosion in the system is large,
This is because a large amount of hydrogen is generated to prevent an unrecoverable failure.

【0028】又、以上のものでは、図1に示すように、
充填用バルブ61及び液面検出器62をもち、内部に腐
食抑制剤を溜める補充タンク6と、このタンク6から系
内に腐食抑制剤を供給する電磁弁から成る開閉バルブ7
1及び送液ポンプ72をもつ供給手段7と、水素ガス検
出手段8による検出結果に基づいて開閉バルブ71及び
送液ポンプ72を作動させて供給管70から系内に腐食
抑制剤を自動供給する制御手段9とを設けており、水素
ガスの発生により消費された腐食抑制剤を系内に自動供
給できるようにしている。
Further, in the above, as shown in FIG.
A refill tank 6 having a filling valve 61 and a liquid level detector 62 and storing a corrosion inhibitor inside, and an opening / closing valve 7 comprising an electromagnetic valve for supplying the corrosion inhibitor into the system from the tank 6.
1 and a feed pump 7 having a liquid feed pump 72, and an opening / closing valve 71 and a liquid feed pump 72 are operated based on the detection result by the hydrogen gas detection device 8 to automatically feed the corrosion inhibitor from the feed pipe 70 into the system. The control means 9 is provided so that the corrosion inhibitor consumed by the generation of hydrogen gas can be automatically supplied into the system.

【0029】[0029]

【発明の効果】請求項1記載の発明によれば、水素ガス
検出手段8はパラジウムセル101の出口側である大気
中に設けるため、構造簡易で、しかも、系内の密閉状態
を良好に保つことができながら、系内で発生する水素ガ
スを検出することができる。
According to the invention described in claim 1, since the hydrogen gas detecting means 8 is provided in the atmosphere on the outlet side of the palladium cell 101, the structure is simple and the sealed state in the system is kept good. While being able to do so, the hydrogen gas generated in the system can be detected.

【0030】請求項2記載の発明によれば、通風筒10
4の内部における単位時間あたりの通過ガス量は送風フ
ァン105による強制送風によりほぼ一定しているか
ら、この通風筒104における送風ファン105の二次
側に水素ガス検出手段8を配設することにより、水素ガ
スの検出精度を向上することができる。
According to the second aspect of the invention, the ventilation tube 10
Since the amount of passing gas per unit time inside 4 is almost constant due to forced air blowing by the blower fan 105, by providing the hydrogen gas detecting means 8 on the secondary side of the blower fan 105 in this ventilation tube 104. Therefore, the detection accuracy of hydrogen gas can be improved.

【0031】請求項3記載の発明によれば、劣化判定手
段108により、水素ガスの透過に伴うパラジウムセル
101の劣化を判定することができる。
According to the third aspect of the invention, the deterioration determining means 108 can determine the deterioration of the palladium cell 101 due to the permeation of hydrogen gas.

【0032】請求項4記載の発明によれば、警報手段1
09の発令により、パラジウムセル101の交換時期を
知ることができる。
According to the invention described in claim 4, the alarm means 1
From the announcement of 09, it is possible to know when to replace the palladium cell 101.

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

【図1】本発明に係る吸収式冷凍機の要部を示す側面
図。
FIG. 1 is a side view showing a main part of an absorption refrigerator according to the present invention.

【図2】同図1における要部平面図。FIG. 2 is a plan view of relevant parts in FIG.

【図3】同制御フローチャート。FIG. 3 is a control flowchart of the same.

【図4】同冷凍機の全体を示す配管図。FIG. 4 is a piping diagram showing the entire refrigerator.

【図5】従来例の配管図。FIG. 5 is a piping diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1;蒸発器、2;吸収器、3,4;発生器、5;凝縮
器、8;水素ガス検出手段、101;パラジウムセル、
104;通風筒、105;送風ファン、92c;圧力検
出手段、108;劣化判定手段、109;警報手段
1; evaporator, 2; absorber, 3, 4; generator, 5; condenser, 8; hydrogen gas detecting means, 101; palladium cell,
104; Ventilation tube, 105; Blower fan, 92c; Pressure detecting means, 108; Degradation judging means, 109; Warning means

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−1058(JP,A) 特開 平6−288890(JP,A) 特開 平3−51681(JP,A) 特開 平5−87421(JP,A) (58)調査した分野(Int.Cl.7,DB名) F25B 49/04 F25B 43/04 F25B 15/06 F25B 15/00 306 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-3-1058 (JP, A) JP-A-6-288890 (JP, A) JP-A-3-51681 (JP, A) JP-A-5- 87421 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) F25B 49/04 F25B 43/04 F25B 15/06 F25B 15/00 306

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 蒸発器(1)、吸収器(2)、発生器
(3,4)、及び凝縮器(5)を備え、系内で発生する
水素ガスをパラジウムセル(101)を介して大気に排
出するようにした吸収式冷凍機において、パラジウムセ
ル(101)の出口側に位置する大気中に、排出する水
素ガスを検出する水素ガス検出手段(8)を設けたこと
を特徴とする吸収式冷凍機。
1. An evaporator (1), an absorber (2), a generator (3, 4), and a condenser (5) are provided, and hydrogen gas generated in the system is passed through a palladium cell (101). An absorption refrigerator that discharges to the atmosphere is characterized in that hydrogen gas detection means (8) for detecting hydrogen gas to be discharged is provided in the atmosphere located on the outlet side of the palladium cell (101). Absorption refrigerator.
【請求項2】 パラジウムセル(101)の出口側に、
通路の横断面に送風ファン(105)を配した通風筒
(104)を設けて、この通風筒(104)における送
風ファン(105)の二次側に、水素ガス検出手段
(8)を配設した請求項1記載の吸収式冷凍機。
2. The outlet side of the palladium cell (101),
A ventilation tube (104) in which a ventilation fan (105) is arranged is provided in the cross section of the passage, and a hydrogen gas detection means (8) is disposed on the secondary side of the ventilation fan (105) in the ventilation tube (104). The absorption refrigerator according to claim 1.
【請求項3】 パラジウムセル(101)の入口側の圧
力を検出する圧力検出手段(92c)を設け、水素ガス
検出手段(8)で検出する水素ガスの排出速度に対し、
圧力検出手段(92c)で検出する内部圧力の上昇速度
が所定以上に大きいとき、パラジウムセル(101)の
異常と判定する劣化判定手段(108)を設けた請求項
1又は請求項2記載の吸収式冷凍機。
3. A pressure detection means (92c) for detecting the pressure on the inlet side of the palladium cell (101) is provided, and the discharge rate of hydrogen gas detected by the hydrogen gas detection means (8) is
The absorption according to claim 1 or claim 2, further comprising deterioration determining means (108) for determining that the palladium cell (101) is abnormal when the rising speed of the internal pressure detected by the pressure detecting means (92c) is higher than a predetermined value. Refrigerator.
【請求項4】 劣化判定手段(108)で異常を判定し
たとき、警報を発する警報手段(109)を設けた請求
項3記載の吸収式冷凍機。
4. The absorption refrigerator according to claim 3, further comprising alarm means (109) for issuing an alarm when the deterioration determining means (108) determines an abnormality.
JP12336794A 1994-06-06 1994-06-06 Absorption refrigerator Expired - Fee Related JP3384111B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12336794A JP3384111B2 (en) 1994-06-06 1994-06-06 Absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12336794A JP3384111B2 (en) 1994-06-06 1994-06-06 Absorption refrigerator

Publications (2)

Publication Number Publication Date
JPH07332819A JPH07332819A (en) 1995-12-22
JP3384111B2 true JP3384111B2 (en) 2003-03-10

Family

ID=14858832

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12336794A Expired - Fee Related JP3384111B2 (en) 1994-06-06 1994-06-06 Absorption refrigerator

Country Status (1)

Country Link
JP (1) JP3384111B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7204308B2 (en) * 2020-08-17 2023-01-16 矢崎エナジーシステム株式会社 judgment device

Also Published As

Publication number Publication date
JPH07332819A (en) 1995-12-22

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