JPH06170357A - Method for stabilizing dissolved oxygen concentration in deaerator - Google Patents

Method for stabilizing dissolved oxygen concentration in deaerator

Info

Publication number
JPH06170357A
JPH06170357A JP34976592A JP34976592A JPH06170357A JP H06170357 A JPH06170357 A JP H06170357A JP 34976592 A JP34976592 A JP 34976592A JP 34976592 A JP34976592 A JP 34976592A JP H06170357 A JPH06170357 A JP H06170357A
Authority
JP
Japan
Prior art keywords
water
water supply
deaerator
dissolved oxygen
oxygen concentration
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
JP34976592A
Other languages
Japanese (ja)
Other versions
JP2737586B2 (en
Inventor
Kazuhiro Tateno
一博 舘野
Yasuhiro Miyagawa
泰寛 宮川
Kenichiro Takematsu
賢一郎 竹松
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.)
Miura Co Ltd
Original Assignee
Miura 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 Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP34976592A priority Critical patent/JP2737586B2/en
Priority to CA002141612A priority patent/CA2141612C/en
Priority to US08/381,863 priority patent/US5584914A/en
Priority to PCT/JP1993/000138 priority patent/WO1994003397A1/en
Publication of JPH06170357A publication Critical patent/JPH06170357A/en
Application granted granted Critical
Publication of JP2737586B2 publication Critical patent/JP2737586B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To stabilize the concentration of dissolved oxygen in deaerated water to be treated at a specified level in a deaeration. CONSTITUTION:A deaerated water supply line 3 consisting of a temperature sensor 4, a water supply pump 5 and a deaerator 6 which removes dissolved air from untreated water, all introduced into the line 3, is connected between an untreated water supply part 1 and a deaerated water tank 2 with a water level detector. Further, a controller 8 is provided which controls the operation of the water supply pump 4 and the deaerator 6. Further, the supply amount of untreated water to be supplied to the deaerator 6 is adjusted based on signals on the temperature of untreated water from the temperature sensor 4 and from the water level detector in the deaerated water tank 2. Thus the deaerated water of a specified concentration of dissolved oxygen is obtained.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、ボイラ等の熱機器や
ビル、マンション等への給水ライン中に適用される脱気
装置における溶存酸素濃度一定化方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for stabilizing the dissolved oxygen concentration in a deaerator applied to a heat equipment such as a boiler or a water supply line to a building, a condominium or the like.

【0002】[0002]

【従来の技術】周知のように、ボイラ、温水器あるいは
冷却器等の冷熱機器類への給水ライン中には、これら機
器類の内部腐食防止を目的とした脱気装置が組み込まれ
ている。又、近年ではビル、マンション等の建造物にお
ける給配水管の赤水防止対策としても脱気装置が用いら
れるようになってきている。この脱気装置は、使用機器
等への給水ライン中に膜式脱酸素モジュールを接続して
おき、この脱酸素モジュール内に原水(水道水、井戸
水、その他工業用水)を通水し、この通水過程において
前記脱酸素モジュール内を真空引きして、前記原水中の
溶存気体を脱気除去する構成のものである。
2. Description of the Related Art As is well known, a water supply line for cooling and heating equipment such as a boiler, a water heater or a cooler is equipped with a deaerator for the purpose of preventing internal corrosion of these equipment. Further, in recent years, deaeration devices have come to be used as a measure for preventing red water in water supply and distribution pipes in buildings, condominiums, and other structures. In this deaerator, a membrane deoxygenation module is connected in the water supply line to the equipment used, and raw water (tap water, well water, other industrial water) is passed through this deoxidation module, In the water process, the inside of the deoxygenation module is evacuated to degas the dissolved gas in the raw water.

【0003】ところで、前記脱気装置は、図2に示すよ
うに処理水量が一定であれば、供給する原水の温度が低
いほど処理水の溶存酸素濃度が高くなるという特性があ
る。そのため、水温の高い夏季では溶存酸素濃度は低
く、水温の低い冬季では溶存酸素濃度は高くなり、した
がって、脱気装置で処理した脱気水も、その原水温度に
より溶存酸素濃度にバラツキが出るため問題となってい
る。
By the way, the deaerator has a characteristic that, as shown in FIG. 2, if the amount of treated water is constant, the dissolved oxygen concentration of the treated water increases as the temperature of the raw water supplied decreases. Therefore, the dissolved oxygen concentration is low in the summer when the water temperature is high, and the dissolved oxygen concentration is high in the winter when the water temperature is low. It's a problem.

【0004】[0004]

【発明が解決しようとする課題】この発明は、上記課題
に鑑み、供給する原水の水温を検知し、該水温を判別し
て脱気装置へ供給する原水の供給量を調整し、脱気水中
の溶存酸素濃度を一定化する方法を提供することを目的
とする。
In view of the above problems, the present invention detects the water temperature of the raw water to be supplied, determines the water temperature and adjusts the supply amount of the raw water to be supplied to the degassing device, It is an object of the present invention to provide a method for stabilizing the dissolved oxygen concentration of.

【0005】[0005]

【課題を解決するための手段】即ち、この発明は、原水
供給部と、水位検出器を備えた脱気水タンクとの間に、
温度センサ、給水ポンプおよび原水中の溶存気体を取り
除く脱気装置を挿入してなる脱気水供給ラインを接続
し、前記給水ポンプおよび脱気装置の運転を制御する制
御器を設け、前記温度センサよりの原水温度と脱気水タ
ンク内の水位検出器からの信号に基づいて、前記脱気装
置に供給する原水の供給量を調整し、所定溶存酸素濃度
の脱気水を確保することを特徴としている。
That is, according to the present invention, between a raw water supply section and a degassed water tank equipped with a water level detector,
A temperature sensor, a water supply pump, and a degassing water supply line for removing dissolved gas in raw water are connected to the degassed water supply line, and a controller for controlling the operation of the water supply pump and the degassing device is provided. Based on the raw water temperature and the signal from the water level detector in the degassed water tank, the amount of raw water supplied to the degassing device is adjusted to ensure degassed water with a predetermined dissolved oxygen concentration. I am trying.

【0006】[0006]

【作用】この発明によれば、温度センサが原水の水温を
検知し制御器へ通報するとともに、脱気水タンク内の水
位検出器が水位信号を制御器へ通報し、制御器は、予め
設定した脱気水中の溶存酸素濃度を確保するため水温と
処理水量および水位信号とを判別して給水ポンプの流量
を制御し、脱気装置へ供給する原水の供給量を調整して
所定溶存酸素濃度の脱気水を供給する。
According to the present invention, the temperature sensor detects the water temperature of the raw water and reports it to the controller, and the water level detector in the degassed water tank reports the water level signal to the controller, and the controller presets. In order to ensure the dissolved oxygen concentration in the degassed water, the flow rate of the feed water pump is controlled by distinguishing the water temperature, the treated water amount and the water level signal, and the amount of raw water to be supplied to the deaerator is adjusted to obtain the predetermined dissolved oxygen concentration. Supply deaerated water.

【0007】[0007]

【実施例】以下、この発明の実施例を図面に基づいて詳
細に説明する。図1は、この発明を実施した脱気水供給
ライン3における各機器の配置を示す説明図である。こ
の脱気水供給ライン3の原水供給部1と脱気水タンク2
との間に、温度センサ4、給水ポンプ5および脱気装置
6を接続してある。前記脱気水タンク2内には、水位検
出用の下位電極棒L、中位電極棒M、上位電極棒Sをそ
れぞれ挿設してあって、各電極棒L,M,Sは回線7を
介して水位検出信号を制御器8へ通報する。前記温度セ
ンサ4は、原水の水温を検知して回線7を介して制御器
8へ電気信号を出力するようになっている。又、前記給
水ポンプ5は可変流量型式のものが設けてあって、前記
温度センサ4よりの原水温度信号を制御器8が判別し、
予め設定した溶存酸素濃度に対応する原水供給量(処理
水量)(図3参照)を制御器8の信号により脱気装置6
へ供給する。
Embodiments of the present invention will be described in detail below with reference to the drawings. FIG. 1 is an explanatory view showing the arrangement of each device in a degassed water supply line 3 embodying the present invention. The raw water supply unit 1 and the deaerated water tank 2 of the deaerated water supply line 3
A temperature sensor 4, a water supply pump 5 and a deaerator 6 are connected between the and. In the degassed water tank 2, a lower electrode rod L, a middle electrode rod M, and an upper electrode rod S for water level detection are inserted, and each electrode rod L, M, S connects a line 7. A water level detection signal is sent to the controller 8 via the above. The temperature sensor 4 detects the temperature of raw water and outputs an electric signal to the controller 8 via the line 7. Further, the water supply pump 5 is of a variable flow type, and the controller 8 determines the raw water temperature signal from the temperature sensor 4,
The raw water supply amount (processed water amount) (see FIG. 3) corresponding to the preset dissolved oxygen concentration is degassed by the signal from the controller 8
Supply to.

【0008】前記脱気装置6は、前記脱気水供給ライン
3中に脱酸素モジュールを接続しておき、この脱酸素モ
ジュール内に原水を通水し、その通水過程において前記
脱酸素モジュール内を真空引きして原水中の溶存気体を
脱気除去する構成のものである。この種の脱気装置6に
おいては、真空引き処理のための手段として構造が簡単
で安価な水封式真空ポンプ(図示省略)が用いられてい
る。尚、脱気処理した脱気水は脱気水タンク2に流入
し、脱気水タンク2の底部より処理水供給ライン9を介
して各機器へ供給される。
The deaerator 6 has a deoxygenation module connected in the deaerated water supply line 3 and allows raw water to pass through the deoxygenation module. Is evacuated to remove the dissolved gas in the raw water by degassing. In this type of deaerator 6, a water-sealed vacuum pump (not shown), which has a simple structure and is inexpensive, is used as a means for vacuuming. The degassed water that has been degassed flows into the degassed water tank 2 and is supplied to each device from the bottom of the degassed water tank 2 through the treated water supply line 9.

【0009】次に、この脱気装置における溶存酸素濃度
一定化方法の作用を説明する。給水ポンプ5を駆動して
原水供給部1(例えば原水タンク)より脱気水供給ライ
ン3に原水が通水すると、温度センサ4は原水の温度を
検知し電気信号を回線7を介して制御器8へ出力する。
制御器8は、温度センサ4よりの原水温度信号を判別
し、予め設定した脱気水中の溶存酸素濃度(0.5pp
m)を確保するため、脱気装置6が処理できる原水の処
理水量を、予め設定した原水温度と処理水量(図2、図
3参照)との関係数値に基づいて、前記給水ポンプ5の
流量を調整し所定溶存酸素濃度の脱気水を脱気水タンク
2へ供給する。そして、脱気水が脱気水タンク2の上位
電極棒Sまで達すると給水ポンプ5および脱気装置6を
停止する。又、各機器への脱気水の供給は、タンクの底
部に接続した処理水供給ライン9を介して供給し、脱気
水タンク2内の水位が中位電極棒Mを切ると、給水ポン
プ5および脱気装置6を駆動し、当初の手順により脱気
水を脱気水タンク2へ補給する。尚、一時的に脱気水の
補給よりも脱気水の供給が増加し下位電極棒Lを切る
と、制御器8は、原水の水温に関係なく給水ポンプ5を
最大流量で運転し緊急補水する。そして、水位が下位電
極棒Lに達すると従来の正常運転に復帰し、所定溶存酸
素濃度の処理水を供給できるようにしている。
Next, the operation of the method for stabilizing the dissolved oxygen concentration in this deaerator will be described. When the raw water is supplied from the raw water supply unit 1 (for example, the raw water tank) to the degassed water supply line 3 by driving the water supply pump 5, the temperature sensor 4 detects the temperature of the raw water and an electric signal is sent via the line 7 to the controller. Output to 8.
The controller 8 determines the raw water temperature signal from the temperature sensor 4, and determines the dissolved oxygen concentration (0.5 pp) in the degassed water set in advance.
m), the amount of raw water that can be treated by the deaerator 6 is set based on the preset numerical value of the relation between the raw water temperature and the amount of treated water (see FIGS. 2 and 3). Is adjusted to supply degassed water having a predetermined dissolved oxygen concentration to the degassed water tank 2. Then, when the deaerated water reaches the upper electrode S of the deaerated water tank 2, the water supply pump 5 and the deaeration device 6 are stopped. Degassed water is supplied to each device through a treated water supply line 9 connected to the bottom of the tank. When the water level in the degassed water tank 2 cuts off the middle electrode rod M, a water pump 5 and the deaerator 6 are driven to supply deaerated water to the deaerated water tank 2 according to the initial procedure. When the supply of degassed water is temporarily increased compared to the supply of degassed water and the lower electrode rod L is cut off, the controller 8 operates the water supply pump 5 at the maximum flow rate regardless of the water temperature of the raw water to perform emergency water replenishment. To do. Then, when the water level reaches the lower electrode rod L, the normal operation is restored to the conventional one so that the treated water having a predetermined dissolved oxygen concentration can be supplied.

【0010】尚、前述の実施例では、給水ポンプ5を可
変流量型式としたが、これを通常の市販ポンプとし、制
御器8内に温度センサ4の電気信号により周波数を変換
できるインバータを内設し、このインバータに回線7を
介してポンプを接続し、このポンプのモータ回転数を変
換することにより脱気装置6への原水の供給量を調整す
ることもできる。
In the above-described embodiment, the water supply pump 5 is of a variable flow rate type, but this is an ordinary commercial pump, and an inverter capable of converting the frequency by the electric signal of the temperature sensor 4 is provided in the controller 8. However, it is also possible to adjust the amount of raw water supplied to the deaerator 6 by connecting a pump to the inverter via the line 7 and converting the motor speed of the pump.

【0011】次に、上記実施例にかわる実施例を図3に
より説明する。図3に示すように、脱気水供給ライン3
に挿入した給水ポンプ5を挟んでバイパスライン10を設
け、このバイパスライン10に電動式操作弁11を挿入し、
この操作弁11を回線7を介して制御器8に接続した構成
としている。前記給水ポンプ5は、通常の市販ポンプと
し、前記温度センサ4の電気信号により、予め設定した
脱気水の所定溶存酸濃度(0.5ppm)を確保するた
め、原水温度と脱気装置6の処理水量との関係数値に基
づいて、制御器8は、前記操作弁11に信号を送って開弁
し、原水の一部をバイパスライン10に流入させることに
より、脱気装置6に供給する原水を所定水量に調整して
供給する。尚、上記以外の構成および作用は前述の実施
例と同様であるので説明を省略する。
Next, an embodiment replacing the above embodiment will be described with reference to FIG. As shown in FIG. 3, the degassed water supply line 3
A bypass line 10 is provided with the water supply pump 5 inserted between the bypass line 10 and the electric operation valve 11 inserted into the bypass line 10.
The operation valve 11 is connected to the controller 8 via the line 7. The water supply pump 5 is an ordinary commercially available pump, and in order to secure a predetermined dissolved acid concentration (0.5 ppm) of the degassed water preset by the electric signal of the temperature sensor 4, the raw water temperature and the deaerator 6 are set. The controller 8 sends a signal to the operation valve 11 to open the valve based on the relational value with the amount of treated water, and causes a part of the raw water to flow into the bypass line 10 to supply the raw water to the deaerator 6. Is adjusted to a predetermined amount of water and supplied. The structure and operation other than those described above are the same as those of the above-described embodiment, and thus the description thereof is omitted.

【0012】[0012]

【発明の効果】この発明は、以上説明したように、予め
設定した脱気水中の溶存酸素濃度(0.5ppm)を確
保するため、脱気水供給ラインに温度センサを挿入し、
この温度センサが原水の水温を検知して制御器に通報
し、予め設定した原水温度と脱気装置の処理水量との関
係数値に基づいて、制御器は給水ポンプの流量を調整し
脱気装置へ所定処理量の原水を供給するので所定濃度の
脱気水を得ることができる。又、一時的な脱気水の増加
要求に対しては、給水ポンプを一時的にフル運転して緊
急補水できるので安全である。
As described above, according to the present invention, in order to secure a preset dissolved oxygen concentration (0.5 ppm) in degassed water, a temperature sensor is inserted in the degassed water supply line,
This temperature sensor detects the water temperature of raw water and reports it to the controller.The controller adjusts the flow rate of the water supply pump based on the preset numerical value of the relation between the raw water temperature and the treated water amount of the deaerator. Since a prescribed amount of raw water is supplied to the degassed water, a prescribed concentration of deaerated water can be obtained. In addition, in case of a temporary increase in degassed water, it is safe because the water supply pump can be temporarily fully operated for emergency water supply.

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

【図1】この発明の一実施例を示す脱気水供給ラインに
おける各機器の配置を示す説明図である。
FIG. 1 is an explanatory view showing the arrangement of each device in a degassed water supply line showing an embodiment of the present invention.

【図2】脱気装置における原水温度と処理水溶存酸素濃
度および処理水量の関係を示す線図である。
FIG. 2 is a diagram showing a relationship between raw water temperature, treated water-soluble oxygen concentration and treated water amount in a deaerator.

【図3】溶存酸素濃度0.5ppm処理における原水水
温の影響を示す線図である。
FIG. 3 is a diagram showing the effect of raw water temperature on treatment with a dissolved oxygen concentration of 0.5 ppm.

【図4】図1の実施例にかわる実施例を示す脱気水供給
ラインにおける各機器の配置を示す説明図である。
FIG. 4 is an explanatory diagram showing an arrangement of each device in a degassed water supply line showing an embodiment replacing the embodiment of FIG.

【符号の説明】[Explanation of symbols]

1…原水供給部 2…脱気水タンク 3…脱気水供給ライン 4…温度センサ 5…給水ポンプ 6…脱気装置 8…制御器 L…下位電極棒 M…中位電極棒 S…下位電極棒 1 ... Raw water supply part 2 ... Deaerated water tank 3 ... Deaerated water supply line 4 ... Temperature sensor 5 ... Water supply pump 6 ... Deaeration device 8 ... Controller L ... Lower electrode rod M ... Middle electrode rod S ... Lower electrode rod

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 原水供給部1と、水位検出器を備えた脱
気水タンク2との間に、温度センサ4、給水ポンプ5お
よび原水中の溶存気体を取り除く脱気装置6を挿入して
なる脱気水供給ライン3を接続し、前記給水ポンプ4お
よび脱気装置6の運転を制御する制御器8を設け、前記
温度センサ4よりの原水温度と脱気水タンク2内の水位
検出器からの信号に基づいて、前記脱気装置6に供給す
る原水の供給量を調整し、所定溶存酸素濃度の脱気水を
確保することを特徴とする脱気装置における溶存酸素濃
度一定化方法。
1. A temperature sensor 4, a water supply pump 5, and a degassing device 6 for removing dissolved gas in raw water are inserted between a raw water supply unit 1 and a degassing water tank 2 equipped with a water level detector. Is connected to the deaerated water supply line 3 and a controller 8 for controlling the operation of the water supply pump 4 and the deaeration device 6 is provided, and the raw water temperature from the temperature sensor 4 and the water level detector in the deaerated water tank 2 are provided. A method for stabilizing the dissolved oxygen concentration in a degassing device, characterized in that the amount of raw water supplied to the degassing device 6 is adjusted based on a signal from the device to ensure degassed water having a predetermined dissolved oxygen concentration.
JP34976592A 1992-08-07 1992-12-01 Method for stabilizing dissolved oxygen concentration in deaerator Expired - Lifetime JP2737586B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP34976592A JP2737586B2 (en) 1992-12-01 1992-12-01 Method for stabilizing dissolved oxygen concentration in deaerator
CA002141612A CA2141612C (en) 1992-08-07 1993-02-04 Improvement to membrane type deaerator
US08/381,863 US5584914A (en) 1992-08-07 1993-02-04 Membrane deaerator apparatus
PCT/JP1993/000138 WO1994003397A1 (en) 1992-08-07 1993-02-04 Improvement to membrane type deaerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34976592A JP2737586B2 (en) 1992-12-01 1992-12-01 Method for stabilizing dissolved oxygen concentration in deaerator

Publications (2)

Publication Number Publication Date
JPH06170357A true JPH06170357A (en) 1994-06-21
JP2737586B2 JP2737586B2 (en) 1998-04-08

Family

ID=18405962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34976592A Expired - Lifetime JP2737586B2 (en) 1992-08-07 1992-12-01 Method for stabilizing dissolved oxygen concentration in deaerator

Country Status (1)

Country Link
JP (1) JP2737586B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007216122A (en) * 2006-02-15 2007-08-30 E's Inc Degassing apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007216122A (en) * 2006-02-15 2007-08-30 E's Inc Degassing apparatus
JP4714597B2 (en) * 2006-02-15 2011-06-29 株式会社イーズ Deaerator

Also Published As

Publication number Publication date
JP2737586B2 (en) 1998-04-08

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