JP2853098B2 - Water treatment method for boiler feed water - Google Patents

Water treatment method for boiler feed water

Info

Publication number
JP2853098B2
JP2853098B2 JP19586294A JP19586294A JP2853098B2 JP 2853098 B2 JP2853098 B2 JP 2853098B2 JP 19586294 A JP19586294 A JP 19586294A JP 19586294 A JP19586294 A JP 19586294A JP 2853098 B2 JP2853098 B2 JP 2853098B2
Authority
JP
Japan
Prior art keywords
water
boiler
chemical
water supply
chemical injection
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
Application number
JP19586294A
Other languages
Japanese (ja)
Other versions
JPH0842809A (en
Inventor
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.)
SAMUSON KK
Original Assignee
SAMUSON KK
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 SAMUSON KK filed Critical SAMUSON KK
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)

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 a hardness component and dissolved oxygen, and if raw water is used as it is in a boiler, scale deposition and corrosion will occur. Therefore, it is necessary to perform a softening treatment and a degassing treatment in advance. As a general water treatment method,
Dewatering is performed by passing water through one side of a gas-liquid separation membrane and applying vacuum to the other side, or a water softening device that removes hardness components by passing water through a resin layer filled with ion exchange resin. A membrane deaerator is used. The above water softener,
It is necessary to periodically regenerate through salt water, and also in the case of a membrane deaerator, it is necessary to perform backwashing to prevent clogging, so that the treatment cannot be continued continuously. In addition, since strict control may be required for hardness leakage, as described in Japanese Patent Publication No. 5-64276, a plurality of the same processing apparatuses are used, and at least one of the processing apparatuses is installed so that it can be operated. However, in that case, cost and space are increased. Another water treatment method is water treatment by chemicals, and when using a chemical injection device, it can be performed with a small chemical injection device as compared to the water treatment device,
In addition, there is no need to stop the operation, but there is a problem that the running cost is high because the 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。
An object of the present invention is to make it possible to always supply treated water without installing a plurality of the same water treatment apparatuses.

【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 A water supply system for a boiler provided with a water treatment device for adjusting the quality of water supply in the middle of the water supply piping is provided with a bypass piping connecting the front and rear of the water treatment device, a bypass piping and a water treatment device. A water flow control device that controls the flow of water to each, and a chemical injection device that injects water treatment chemicals into the water supply piping are provided. When water treatment by the device cannot be performed, water is supplied to the bypass piping, and chemical injection is performed. The apparatus is operated, and water treatment using chemicals is performed instead of the water treatment apparatus. 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,
Activate 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 a device and water treatment by a chemical are installed in parallel, and when water treatment by the device cannot be performed, water treatment is performed by bypassing the water flow and injecting the chemical into the supply water. Therefore, water is not supplied without being treated, and it is not necessary to install treatment devices in parallel. In addition, when the water treatment is not sufficiently performed even though the water passes through the treatment device, the detection is performed by the detection device provided downstream of the treatment device, and the chemical is injected. There is no need to install devices in series. Since the chemical is only used temporarily, the amount of chemical 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 flowchart showing a water supply path to a boiler.
In the middle of the water supply pipe (1) to the boiler (4), a membrane deaerator (3) and a water softener (2) are inserted, and a deaeration bypass pipe () that bypasses the membrane deaerator (3). 8),
A softening bypass pipe (7) for bypassing the water softener (2) is provided, and a chemical injection device A (6) for injecting the scale dispersant and a chemical injection device B (5) for injecting the oxygen scavenger are provided by water supply piping. It is connected to (1). In addition, water supply piping (1)
And deaeration bypass pipe (8) junction and membrane deaerator (3)
Between the deaeration device water flow control valve (11), the deaeration bypass piping (8), the deaeration bypass piping control valve (12), the water supply piping (1) and the branch point of the softening bypass piping (7) and hard water. A softening device flow control valve (9) is provided between the softening devices (2), and a softening bypass piping control valve (1) is provided in the middle of the softening bypass piping (7).
0) are provided. A hardness leak sensor (13) is provided downstream of the water softener (2), and a dissolved oxygen concentration meter (16) is provided downstream of the membrane deaerator (3).
Connected to the softening control device (14) connected to the hardening leak sensor (13), the softening device water flow control valve (9), the softening bypass pipe control valve (10), and the water softening device (2) by signal lines. , A deaeration device water flow control valve (11), a deaeration bypass pipe control valve (12), a membrane deaeration device (3), and a dissolution to a deaeration control device (15) connected to a chemical injection device B (5). The oximeter (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。
[0007] Normal water treatment is performed by a water softening device and a membrane deaerator, and the softening control device and the deaeration controller open the deaerator water control valve and the softener water control valve,
Close the deaeration bypass pipe control valve and the softening bypass pipe control valve, perform water treatment with a water softener and a membrane deaerator,
The chemical injection devices A and B are not operated. The water passed is passed through a membrane deaerator and a water softener, processed into water suitable for the boiler, and 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 deaeration cannot be performed, such as when cleaning the membrane deaerator, the deaeration controller closes the deaerator flow control valve and opens the deaeration bypass pipe control valve to release water. The treatment is performed through a degassing bypass pipe, and a deoxidizer is injected from the chemical injection device B to perform water treatment with a chemical. When the water softening device cannot perform the softening treatment due to regeneration or the like, the softening control device closes the softening device water flow control valve, opens the softening bypass pipe control valve, performs water flow through the softening bypass pipe, and performs the chemical injection device. Water treatment with a chemical is performed by injecting a scale dispersant from A.

【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。
[0009] Even if the water is softened by the water softening device, if the water softening device leaks the hardness, a hardness leak signal is sent from the hardness leak sensor to the softening control device, and the softening control device Performs water treatment with chemicals by starting chemical injection of the chemical injection device A. Even when the dissolved oxygen is removed by the membrane deaerator, if the deaeration is insufficient and the dissolved oxygen concentration is high, a signal is sent from the dissolved oxygen concentration meter to the deaeration controller. The degassing control device performs water treatment with a chemical by starting the chemical injection of the chemical injection device B.

【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。
According to the present invention, even when water supply is always required and water quality control must be strictly performed, it is not necessary to install a plurality of the same water treatment devices, and space and cost can be reduced. Reduction can be achieved.

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

【図1】 本発明の一実施例のフロー図FIG. 1 is a flowchart 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 DESCRIPTION OF SYMBOLS 1 Water supply pipe 2 Membrane deaerator 3 Water softening device 4 Boiler 5 Chemical injection device B 6 Chemical injection device A 7 Softening bypass piping 8 Deaeration bypass piping 9 Softening device flow control valve 10 Softening bypass piping control valve 11 Deaerator Flow control valve 12 Deaeration bypass pipe control valve 13 Hardness leak sensor 14 Softening control device 15 Deaeration control device 16 Dissolved oxygen concentration meter

Claims (4)

(57)【特許請求の範囲】(57) [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漏れ
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漏れを検出したと
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。
In a water supply system of a boiler for adjusting water quality in the middle of a water supply pipe in order to supply water to a boiler, a hardness leak for detecting the presence or absence of a hardness leak downstream of a water softening device provided in the water supply system. A boiler feed water is provided, in which a sensor and a chemical injection device for injecting a chemical for preventing scale adhesion are further provided downstream, and when a hardness leak is detected by a hardness leak sensor, the chemical injection device is operated. 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. A system for detecting dissolved oxygen concentration downstream of a membrane deaerator provided in a water supply system in a water supply system of a boiler for adjusting water quality in a water supply pipe to supply water to the boiler. A concentration meter and a chemical injection device for injecting a chemical for removing dissolved oxygen are provided further downstream, and when the dissolved oxygen concentration is detected as high by the dissolved oxygen concentration meter, the chemical injection device is operated. A method for treating boiler feed water.
【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 for adjusting water quality in the middle of a water supply pipe in order to supply 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 hardening. 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-supplied water, wherein the water supply is sent to a bypass pipe without being sent to the water softening device, and the water component is not removed by the water softening device, but the chemical injection device is operated to perform water treatment with a chemical. .
【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 for adjusting water quality in the middle of a water supply pipe to supply 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 deaerators and a chemical injection device that injects a chemical that removes dissolved oxygen into water that has not passed through the membrane deaerator are provided. In the case of washing, feed water is sent to a bypass pipe without being sent to a membrane deaerator, and dissolved oxygen is not removed by the membrane deaerator, but a chemical injection device is operated to perform water treatment with a chemical. 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 JPH0842809A (en) 1996-02-16
JP2853098B2 true JP2853098B2 (en) 1999-02-03

Family

ID=16348230

Family Applications (1)

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

Country Status (1)

Country Link
JP (1) JP2853098B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4654392B2 (en) * 2000-08-07 2011-03-16 株式会社片山化学工業研究所 Boiler water treatment system and blow water management method using the same
JP4631313B2 (en) * 2004-05-28 2011-02-16 三浦工業株式会社 Water supply system
JP4842056B2 (en) * 2005-02-23 2011-12-21 クリタック株式会社 Water quality control device
JP5190674B2 (en) * 2008-03-24 2013-04-24 栗田工業株式会社 Operation method of boiler system

Also Published As

Publication number Publication date
JPH0842809A (en) 1996-02-16

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