JPH0842809A - Treating method for boiler feed water - Google Patents

Treating method for boiler feed water

Info

Publication number
JPH0842809A
JPH0842809A JP19586294A JP19586294A JPH0842809A JP H0842809 A JPH0842809 A JP H0842809A JP 19586294 A JP19586294 A JP 19586294A JP 19586294 A JP19586294 A JP 19586294A JP H0842809 A JPH0842809 A JP H0842809A
Authority
JP
Japan
Prior art keywords
water
boiler
softening
bypass pipe
chemical
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
JP19586294A
Other languages
Japanese (ja)
Other versions
JP2853098B2 (en
Inventor
Shigeru Kuroki
茂 黒木
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.)
Samson Co Ltd Japan
Original Assignee
Samson Co Ltd Japan
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
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Application filed by Samson Co Ltd Japan filed Critical Samson Co Ltd Japan
Priority to JP19586294A priority Critical patent/JP2853098B2/en
Publication of JPH0842809A publication Critical patent/JPH0842809A/en
Application granted granted Critical
Publication of JP2853098B2 publication Critical patent/JP2853098B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Degasification And Air Bubble Elimination (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Physical Water Treatments (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

PURPOSE:To hold down an increase in running cost by a method wherein a water quality inspection device is provided downstream of a water softening device and, when the hardness components are detected, a chemical introducing device is operated. CONSTITUTION:A water feed pipe 1 to a boiler 4 is provided with a deaerating bypass pipe 8, a softening bypass pipe 7 and chemical introducing devices A6 and B5 by inserting a membrane deaerator 3 and a water sofetening device 2. The water softening device 2 and the membrane deaerator 3 respectively are provided downstream with a hardness leak sensor 13 and a dissolved oxygen concentration meter 16. The feed water is normally treated by the membrane deaerator 3 and the water sofetening device 2 and then fed to a boiler 4 and, when the membrane deaerator 3 is cleaned, the water is passed through the deaerating bypass pipe 8 and a deoxidizing agent is introduced into the water from the chemical introducing device B5 for the water treatment. When the water softening device is regenerated, the water is passed through the sofetening bypass pipe 7 and a scale dispersing agent is introduced into the water from the chemicak introducing device A6 for the water treatment. The aforesaid arrangement eliminates the need for a simultaneous provision of a plurality of the water treating devices, thereby contriving the saving of space and the reduction of costs.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はボイラー供給水の水処理
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 treating boiler feed water.

【0002】[0002]

【従来の技術】原水中には硬度成分や溶存酸素が含まれ
ており、原水をそのままボイラーに使用するとスケール
の堆積や腐食を引き起こすために、予め軟化処理や脱気
処理を行う必要がある。一般的な水処理の方法として、
イオン交換樹脂を充填した樹脂層へ通水することによっ
て硬度成分を除去する硬水軟化装置や、気液分離膜の一
方の側に通水し、他方の側を真空にすることで脱気を行
う膜脱気装置が使用されている。上記硬水軟化装置は、
定期的に塩水を通して再生することが必要であり、膜脱
気装置の場合も逆洗を行って目詰まりを防止する必要が
あるため、連続して処理し続けることができない。さら
に、硬度漏れに対し厳重な管理が必要な場合もあるた
め、特許公告平5−64276に記載されているよう
に、同じ処理装置を複数使用し、少なくとも一方は稼働
することができるよう設置されるが、その場合、コスト
やスペースの増大を招いていた。また、他の水処理方法
として薬品による水処理があり、薬注装置を使用する場
合は、前記水処理装置に比べて小さな薬注装置で行え、
かつ停止させる必要が無いが、薬品を使用するためにラ
ンニングコストが大きいという問題があった。
2. Description of the Related Art Raw water contains hardness components and dissolved oxygen, and if the raw water is used as it is in a boiler, it causes scale accumulation and corrosion. Therefore, it is necessary to perform softening treatment or degassing treatment in advance. As a general water treatment method,
A water softening device that removes hardness components by passing water through a resin layer filled with an ion exchange resin, or water is passed through one side of a gas-liquid separation membrane and the other side is evacuated to perform deaeration. Membrane deaerators are used. The water softening device,
It is necessary to periodically regenerate it through salt water, and even in the case of a membrane degassing device, it is necessary to perform backwashing to prevent clogging, and therefore continuous treatment cannot be continued. Further, since there are cases where strict control of hardness leakage is required, as described in Japanese Patent Publication No. 5-64276, a plurality of the same processing devices are used and at least one of them is installed so that they can operate. However, in that case, the cost and the space are increased. Further, there is water treatment by chemicals as another water treatment method, and when using a chemical injection device, it can be performed with a chemical injection device smaller than the water treatment device,
Moreover, it is not necessary to stop, but there is a problem that running cost is high because a chemical is used.

【0003】[0003]

【発明が解決しようとする課題】本発明が解決しようと
する課題は、同じ水処理装置を複数台設置しなくとも処
理を行った水を常時供給することができるようにするも
のである。
The problem to be solved by the present invention is to make it possible to always supply treated water without installing a plurality of the same water treatment devices.

【0004】[0004]

【課題を解決するための手段】給水配管途中に、給水の
水質を調整する水処理装置を設けたボイラーへの給水系
統に、水処理装置の前後を結ぶバイパス配管、バイパス
配管と水処理装置のそれぞれへの通水を制御する通水制
御装置、給水配管中に水処理薬品を注入する薬注装置を
設けておき、装置による水処理が行えないとき、バイパ
ス配管へ通水を行い、薬注装置を稼働させ、水処理装置
の代わりに薬品による水処理を行う。また、水処理装置
の下流に水質を検査する検査装置を設けておき、装置に
よる水処理が十分に行えていないことが検出された時、
薬注装置を稼働させる。
[Means for Solving the Problems] In a water supply system for a boiler, which is provided with a water treatment device for adjusting the water quality of the feed water in the middle of the water supply pipe, a bypass pipe connecting the front and rear of the water treatment device, and a bypass pipe and a water treatment device A water flow control device that controls water flow to each of them, and a chemical injection device that injects water treatment chemicals into the water supply pipe are provided.When water treatment by the device cannot be performed, water is passed to the bypass pipe to perform chemical injection. Operate the equipment and perform chemical water treatment instead of the water treatment equipment. In addition, an inspection device for inspecting water quality is provided downstream of the water treatment device, and when it is detected that the water treatment by the device is not sufficiently performed,
Operate the dosing device.

【0005】[0005]

【作用】装置による水処理と、薬品による水処理を併設
し、装置による水処理が行えないときは通水を処理装置
をバイパスさせ、給水中に薬品を注入することで薬品に
よる水処理を行うので処理されないまま給水されること
がなくなり、処理装置を並列に設置する必要がなくな
る。また、処理装置を通っていても十分に水処理が行え
ていない場合、処理装置下流に設けた検出装置によって
検出し、薬品注入を行うので処理されていない水が給水
されることが無くなり、処理装置を直列に設置する必要
が無くなる。薬品は一時的に使用するだけなので、薬品
使用量は低く保て、ランニングコストの増大を抑えるこ
とができる。
[Function] Water treatment by the equipment and water treatment by chemicals are provided side by side. When water treatment by the equipment cannot be performed, water is bypassed by the treatment equipment and chemicals are injected into the water supply to perform water treatment by chemicals. Therefore, water is not supplied without being treated, and it is not necessary to install treatment devices in parallel. If water is not sufficiently treated even though it passes through the treatment equipment, it is detected by a detector installed downstream of the treatment equipment, and chemicals are injected, so untreated water is no longer supplied. Eliminates the need to install devices in series. Since the chemicals are only used temporarily, the amount of chemicals used can be kept low and the increase in running cost can be suppressed.

【0006】[0006]

【実施例】本発明の一実施例を図面を用いて説明する。
図1はボイラーへの給水経路を示したフロー図である。
ボイラー(4)への給水配管(1)途中には、膜脱気装
置(3)、硬水軟化装置(2)が挿入されており、膜脱
気装置(3)をバイパスする脱気バイパス配管(8)、
硬水軟化装置(2)をバイパスする軟化バイパス配管
(7)が設けられ、スケール分散剤を注入する薬注装置
A(6)と、脱酸素剤を注入する薬注装置B(5)が給
水配管(1)に接続されている。また、給水配管(1)
と脱気バイパス配管(8)の分岐点と膜脱気装置(3)
の間に脱気装置通水制御弁(11)、脱気バイパス配管
(8)途中に脱気バイパス配管制御弁(12)、給水配
管(1)と軟化バイパス配管(7)の分岐点と硬水軟化
装置(2)の間に軟化装置通水制御弁(9)、軟化バイ
パス配管(7)途中には軟化バイパス配管制御弁(1
0)をそれぞれ設ける。硬水軟化装置(2)の下流には
硬度リークセンサー(13)、膜脱気装置(3)の下流
には溶存酸素濃度計(16)を設け、薬注装置A(6)
に接続された軟化制御装置(14)に硬度リークセンサ
ー(13)、軟化装置通水制御弁(9)、軟化バイパス
配管制御弁(10)、硬水軟化装置(2)に信号線にて
接続し、薬注装置B(5)に接続された脱気制御装置
(15)に脱気装置通水制御弁(11)、脱気バイパス
配管制御弁(12)、膜脱気装置(3)、溶存酸素濃度
計(16)を信号線にて接続する。
An embodiment of the present invention will be described with reference to the drawings.
FIG. 1 is a flow chart showing a water supply route to a boiler.
A membrane degassing device (3) and a water softening device (2) are inserted in the water supply pipe (1) to the boiler (4), and a degassing bypass pipe (bypassing the membrane degassing device (3) ( 8),
A softening bypass pipe (7) for bypassing the water softening device (2) is provided, and a chemical injection device A (6) for injecting a scale dispersant and a chemical injection device B (5) for injecting a deoxidant are provided in the water supply pipe. It is connected to (1). In addition, water supply pipe (1)
And branch point of degassing bypass pipe (8) and membrane degasser (3)
Between the deaerator water flow control valve (11), the degassing bypass pipe (8), the degassing bypass pipe control valve (12), the branch point of the water supply pipe (1) and the softening bypass pipe (7), and hard water. The softening device water flow control valve (9) between the softening device (2) and the softening bypass pipe control valve (1) in the middle of the softening bypass pipe (7).
0) are provided respectively. A hardness leak sensor (13) is provided downstream of the water softening device (2), a dissolved oxygen concentration meter (16) is provided downstream of the membrane degassing device (3), and a chemical injection device A (6) is provided.
The softening control device (14) connected to the device is connected to the hardness leak sensor (13), the softening device water flow control valve (9), the softening bypass piping control valve (10), and the water softening device (2) by signal lines. , A degassing control device (15) connected to the chemical injection device B (5), a degassing device water flow control valve (11), a degassing bypass piping control valve (12), a membrane degassing device (3), a dissolved gas The oxygen concentration meter (16) is connected by a signal line.

【0007】通常時の水処理は硬水軟化装置および膜脱
気装置によって行われ、軟化制御装置と脱気制御装置
は、脱気装置通水制御弁、軟化装置通水制御弁を開き、
脱気バイパス配管制御弁、軟化バイパス配管制御弁を閉
じ、硬水軟化装置および膜脱気装置にて水処理を行い、
薬注装置A・Bは稼働させずにおく。通水される水は膜
脱気装置、硬水軟化装置を通り、ボイラーに適した水に
処理されてボイラーへ給水される。
Normal water treatment is performed by a water softening device and a membrane degassing device, and the softening control device and the degassing control device open the degassing device water flow control valve and the softening device water flow control valve,
Close the degassing bypass piping control valve and the softening bypass piping control valve, perform water treatment with the water softening device and the membrane degassing device,
Do not operate the chemical injection devices A and B. The water to be passed passes through a membrane degassing device and a water softening device, is treated into water suitable for the boiler, and is supplied to the boiler.

【0008】膜脱気装置を洗浄する場合など脱気処理を
行うことができない場合、脱気制御装置は、脱気装置通
水制御弁を閉じ、脱気バイパス配管制御弁を開いて通水
を脱気バイパス配管を通して行い、薬注装置Bより脱酸
素剤を注入することで、薬品による水処理を行う。硬水
軟化装置が再生などで軟化処理を行うことができない場
合、軟化制御装置は、軟化装置通水制御弁を閉じ、軟化
バイパス配管制御弁を開いて通水を軟化バイパス配管を
通して行い、薬注装置Aよりスケール分散剤を注入する
ことで、薬品による水処理を行う。
When deaerating cannot be performed, such as when cleaning the membrane deaerator, the deaerator controller closes the deaerator water flow control valve and opens the degassing bypass piping control valve to allow water flow. Water treatment by chemicals is performed by injecting a deoxidizer from the chemical injection device B through the degassing bypass pipe. When the water softening device cannot perform softening treatment such as regeneration, the softening control device closes the softening device water flow control valve and opens the softening bypass pipe control valve to pass water through the softening bypass pipe, and then the chemical injection device. By injecting the scale dispersant from A, water treatment with chemicals is performed.

【0009】硬水軟化装置にて水の軟化を行っている場
合であっても、硬水軟化装置が硬度漏れを起こした場
合、硬度リークセンサーより軟化制御装置に硬度漏れ信
号が送られ、軟化制御装置は薬注装置Aの薬注を開始す
ることで薬品による水処理を行う。また、膜脱気装置に
て溶存酸素の除去を行っている場合であっても、脱気処
理が不十分で溶存酸素濃度が高い場合、溶存酸素濃度計
より脱気制御装置へ信号が送られ、脱気制御装置は薬注
装置Bの薬注を開始することで薬品による水処理を行
う。
Even when water is softened by the water softening device, if the water softening device leaks hardness, a hardness leak signal is sent from the hardness leak sensor to the softening control device, and the softening control device is sent. Starts the chemical injection of the chemical injection device A to perform water treatment with chemicals. Even if the dissolved oxygen is removed by the membrane degasser, if the degassing process is insufficient and the dissolved oxygen concentration is high, the dissolved oxygen concentration meter sends a signal to the degassing controller. The deaeration control device starts the chemical injection of the chemical injection device B to perform water treatment with chemicals.

【0010】[0010]

【発明の効果】本発明を実施することで、給水が常時必
要で、水質管理を厳重に行う必要がある場合であって
も、同じ水処理装置を複数設置する必要が無くなり、ス
ペース、コストの低減をはかることができる。
By implementing the present invention, it is not necessary to install a plurality of the same water treatment devices even if water supply is always required and water quality control is strictly required, which saves space and cost. It can be reduced.

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

【図1】 本発明の一実施例のフロー図FIG. 1 is a flow chart of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 給水配管 2 膜脱気装置 3 硬水軟化装置 4 ボイラー 5 薬注装置B 6 薬注装置A 7 軟化バイパス配管 8 脱気バイパス配管 9 軟化装置通水制御弁 10 軟化バイパス配管制御弁 11 脱気装置通水制御弁 12 脱気バイパス配管制御弁 13 硬度リークセンサー 14 軟化制御装置 15 脱気制御装置 16 溶存酸素濃度計 1 Water Supply Pipe 2 Membrane Deaerator 3 Hard Water Softener 4 Boiler 5 Chemical Dosing Device B 6 Chemical Dosing Device A 7 Softening Bypass Piping 8 Degassing Bypass Piping 9 Softening Device Water Flow Control Valve 10 Softening Bypass Piping Control Valve 11 Degassing Device Water flow control valve 12 Degassing bypass piping control valve 13 Hardness leak sensor 14 Softening control device 15 Degassing control device 16 Dissolved oxygen concentration meter

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 5/08 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display C02F 5/08

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ボイラーへ給水するために、給水配管途
中で水質の調整を行っているボイラーの給水系統におい
て、給水系統中に設けた硬水軟化装置の下流に硬度成分
の有無を検出する硬度リークセンサー、さらに下流にス
ケール付着を防止する薬品を注入する薬注装置を設けて
おき、硬度リークセンサーにて硬度成分を検出したと
き、薬注装置を作動させることを特徴とするボイラー供
給水の水処理方法。
1. In a water supply system of a boiler in which water quality is adjusted in the middle of a water supply pipe to supply water to the boiler, a hardness leak for detecting the presence or absence of a hardness component downstream of a water softening device provided in the water supply system. A sensor, and a chemical injection device for injecting a chemical that prevents scale adhesion is provided further downstream, and when a hardness component is detected by a hardness leak sensor, the chemical injection device is activated to supply water to the boiler supply water. Processing method.
【請求項2】 ボイラーへ給水するために、給水配管途
中で水質の調整を行っているボイラーの給水系統におい
て、給水系統中に設けた膜脱気装置の下流に溶存酸素濃
度を検出する溶存酸素濃度計、さらに下流に溶存酸素を
除去する薬品を注入する薬注装置を設けておき、溶存酸
素濃度計にて溶存酸素濃度が高濃度であると検出された
とき、薬注装置を作動させることを特徴とするボイラー
供給水の水処理方法。
2. Dissolved oxygen for detecting a dissolved oxygen concentration downstream of a membrane degassing device provided in a water supply system in a water supply system of a boiler in which water quality is adjusted in the middle of a water supply pipe to supply water to the boiler. A concentration meter and a chemical injection device for injecting a chemical that removes dissolved oxygen are provided further downstream, and the chemical injection device is activated when the dissolved oxygen concentration is detected to be high. A water treatment method for boiler feed water, characterized by:
【請求項3】 ボイラーへ給水するために、給水配管途
中で水質の調整を行っているボイラーの給水系統におい
て、給水系統中に設けた硬水軟化装置の前後を結ぶバイ
パス配管、バイパス配管と硬水軟化装置のそれぞれへの
通水を制御する通水制御装置、硬水軟化装置を通過しな
かった水へスケール付着を防止する薬品を注入する薬注
装置を設けておき、硬水軟化装置を再生する場合、給水
を硬水軟化装置へ送らずバイパス配管へ送り、硬水軟化
装置による硬度成分の除去は行わず、薬注装置を作動さ
せて薬品による水処理を行うことを特徴とするボイラー
供給水の水処理方法。
3. In a water supply system of a boiler in which water quality is adjusted in the middle of the water supply pipe for supplying water to the boiler, a bypass pipe connecting the front and rear of a water softening device provided in the water supply system, a bypass pipe and water softening A water flow control device that controls water flow to each of the devices, a chemical injection device that injects a chemical that prevents scale adhesion to water that has not passed through the water softening device is provided, and when regenerating the water softening device, A water treatment method for boiler feed water, characterized in that the feed water is not sent to the water softening device but is sent to the bypass pipe, the hardness component is not removed by the water softening device, and the chemical injection device is operated to perform water treatment with chemicals. .
【請求項4】 ボイラーへ給水するために、給水配管途
中で水質の調整を行っているボイラーの給水系統におい
て、給水系統中に設けた膜脱気装置の前後を結ぶバイパ
ス配管、バイパス配管と膜脱気装置のそれぞれへの通水
を制御する通水制御装置、膜脱気装置を通過しなかった
水へ溶存酸素を除去する薬品を注入する薬注装置を設け
ておき、膜脱気装置の洗浄を行う場合、給水を膜脱気装
置へ送らずバイパス配管へ送り、膜脱気装置による溶存
酸素の除去は行わず、薬注装置を作動させて薬品による
水処理を行うことを特徴とするボイラー供給水の水処理
方法。
4. In a water supply system of a boiler in which the water quality is adjusted in the middle of the water supply pipe for supplying water to the boiler, a bypass pipe connecting the front and rear of a membrane deaerator provided in the water supply system, a bypass pipe and a membrane. A water flow control device that controls water flow to each of the degassing devices, and a chemical injection device that injects a chemical that removes dissolved oxygen into water that has not passed through the membrane degassing device is provided in advance. When cleaning, the feed water is not sent to the membrane degassing device but to the bypass pipe, the dissolved oxygen is not removed by the membrane degassing device, and the chemical injection device is operated to perform water treatment with chemicals. Water treatment method for boiler feed water.
JP19586294A 1994-07-27 1994-07-27 Water treatment method for boiler feed water Expired - Lifetime JP2853098B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19586294A JP2853098B2 (en) 1994-07-27 1994-07-27 Water treatment method for boiler feed water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19586294A JP2853098B2 (en) 1994-07-27 1994-07-27 Water treatment method for boiler feed water

Publications (2)

Publication Number Publication Date
JPH0842809A true JPH0842809A (en) 1996-02-16
JP2853098B2 JP2853098B2 (en) 1999-02-03

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002174402A (en) * 2000-08-07 2002-06-21 Katayama Chem Works Co Ltd Method and system for treating boiler water
JP2005334798A (en) * 2004-05-28 2005-12-08 Miura Co Ltd Water supply system
JP2007007651A (en) * 2005-02-23 2007-01-18 Kuritakku Kk Water quality regulating device
JP2009228991A (en) * 2008-03-24 2009-10-08 Kurita Water Ind Ltd Boiler system and operating method of boiler system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002174402A (en) * 2000-08-07 2002-06-21 Katayama Chem Works Co Ltd Method and system for treating boiler water
JP2005334798A (en) * 2004-05-28 2005-12-08 Miura Co Ltd Water supply system
JP2007007651A (en) * 2005-02-23 2007-01-18 Kuritakku Kk Water quality regulating device
JP2009228991A (en) * 2008-03-24 2009-10-08 Kurita Water Ind Ltd Boiler system and operating method of boiler system

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