JPH09243013A - Steam boiler with drain treatment device - Google Patents

Steam boiler with drain treatment device

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Publication number
JPH09243013A
JPH09243013A JP7833196A JP7833196A JPH09243013A JP H09243013 A JPH09243013 A JP H09243013A JP 7833196 A JP7833196 A JP 7833196A JP 7833196 A JP7833196 A JP 7833196A JP H09243013 A JPH09243013 A JP H09243013A
Authority
JP
Japan
Prior art keywords
water
wastewater treatment
blow
boiler
treatment tank
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
JP7833196A
Other languages
Japanese (ja)
Other versions
JP2987323B2 (en
Inventor
Tomizo Okada
富造 岡田
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
Original Assignee
SAMSON 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 SAMSON CO Ltd filed Critical SAMSON CO Ltd
Priority to JP8078331A priority Critical patent/JP2987323B2/en
Publication of JPH09243013A publication Critical patent/JPH09243013A/en
Application granted granted Critical
Publication of JP2987323B2 publication Critical patent/JP2987323B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a steam boiler having a small-sized drain treatment device for performing a neutralization of blow water by feeding combustion discharged gas in blow water in a steam boiler while a proper blowing operation is being carried out. SOLUTION: This is a drain treatment device for a steam boiler in which boiler water condensed by evaporation is discharged regularly and combustion discharged gas after heating boiler water is discharged through a flue 5, an upper part of a drain treatment tank 10 for use in accumulating drain water from the boiler 1 is made to communicate with the flue 5 by an aeration port 3 and then the drain water treatment device is integrally assembled with the flue.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、ボイラから排出さ
れるアルカリ性の排水を中和する排水処理装置の付いた
ボイラに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a boiler equipped with a wastewater treatment device for neutralizing alkaline wastewater discharged from the boiler.

【0002】[0002]

【従来の技術】蒸気ボイラの缶水はボイラの腐食を抑制
するため、pHが高くなるように調整されている。蒸気
ボイラは蒸発により減少した分だけ給水を行うため、蒸
気を発生させるごとに水中の不純物が濃縮される。濃縮
が進行するとキャリオーバ等の障害が発生するので、濃
縮を抑えるために定期的に缶水を排水する濃縮ブローが
必要となる。また、缶水が濃縮すると缶体底部に釜泥
(スラッジ)が堆積するため、缶底から釜泥を排出する
全ブローも必要である。
2. Description of the Related Art Can water of a steam boiler is adjusted to have a high pH in order to suppress corrosion of the boiler. Since the steam boiler supplies water by the amount reduced by evaporation, impurities in water are concentrated each time steam is generated. As the concentration progresses, problems such as carryover will occur, so it is necessary to periodically perform a concentration blow to drain the can water in order to suppress the concentration. Further, when the can water is concentrated, the sludge (sludge) accumulates on the bottom of the can body, so it is necessary to completely blow the sludge from the bottom of the can.

【0003】缶水のブロー水はpH11〜12程度であ
るため、ブロー水は中和する必要がある。排水を中和す
る方法の一つに、ブロー水を排水処理タンクにためてお
き、ボイラからの燃焼排ガスをブロー水中に送り吹き込
むことで、ブロー水中の水酸化物イオンと燃焼排ガス中
の二酸化炭素や微量の窒素酸化物等を反応させ、タンク
内のpHを低下させることが行われている。上記方法に
よりブロー水の中和を行う場合、中和剤は不用であるが
排水処理タンクと中和のための装置が必要であり、その
分ボイラ全体の大きさが大型化していた。
Since the pH of blow water for canned water is about 11 to 12, it is necessary to neutralize the blow water. One of the methods to neutralize wastewater is to store blow water in a wastewater treatment tank and blow the combustion exhaust gas from the boiler into the blow water, so that hydroxide ions in the blow water and carbon dioxide in the combustion exhaust gas are blown. It has been practiced to lower the pH in the tank by reacting a small amount of nitrogen oxide or the like. When the blow water is neutralized by the above method, a neutralizing agent is not required, but a wastewater treatment tank and a neutralizing device are required, and the size of the entire boiler is increased accordingly.

【0004】[0004]

【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、適正なブローを行いながら蒸気ボイラのブ
ロー水中に燃焼排ガスを送り込むことでブロー水の中和
を行う小型の排水処理装置を持った蒸気ボイラを提供す
ることにある。
SUMMARY OF THE INVENTION The problem to be solved by the present invention is to provide a small waste water treatment device for neutralizing blow water by sending combustion exhaust gas into the blow water of a steam boiler while performing proper blow. It is to provide the steam boilers that they have.

【0005】[0005]

【課題を解決するための手段】ボイラの炉内で燃焼を行
うことで蒸気を発生させ、蒸発によって濃縮される缶水
は定期的に排水を行い、缶水を加熱した後の燃焼排ガス
は煙道を通して排気している蒸気ボイラの排水処理装置
であって、ボイラから排水されるアルカリ性のブロー水
をためる排水処理タンク、ボイラの缶水を排水処理タン
クに送るブロー水配管、弁の開閉によって排水処理タン
クへ缶水を送るブロー制御を行うブロー弁、一端は煙道
の燃焼排ガス流動部に接続され、他端は排水処理タンク
の水中部に接続されている排ガス配管、排ガス配管途中
に燃焼排ガスを排水処理タンク内へ送り込む排ガス圧送
装置、排水処理タンクに接続された排水処理タンク内の
水を排水する処理水排水管、ボイラの運転やブロー弁の
開閉を行う制御装置を設け、排水処理タンク上部と煙道
を連通させ、排水処理タンク内の水位を検出する水位検
出器を設けて、水位検出器と制御装置を接続しておき、
水位検出器によって排水処理タンク内の水位が一定の水
位よりも高くなったことが検出されたとき、ブロー弁の
閉制御を行う。また、制御装置にブロー時間を設定し、
ブロー弁を開いた場合のブロー弁開時間を検出してお
き、設定しておいたブロー時間経過しても水位検出器に
よって排水処理タンク内の水位が一定の水位より高くな
ったことが検出されなかった時、ブロー異常の警報を出
力する。
[Means for solving the problems] Steam is generated by burning in a furnace of a boiler, and can water concentrated by evaporation is drained periodically, and combustion exhaust gas after heating the can water is smoke. A wastewater treatment device for steam boilers exhausting through a road.A wastewater treatment tank that stores alkaline blow water discharged from the boiler, a blowwater pipe that sends boiler boiler water to the wastewater treatment tank, and drainage by opening and closing valves. Blow valve for blow control that sends canned water to the treatment tank, one end is connected to the combustion exhaust gas flow section of the flue, and the other end is connected to the underwater portion of the wastewater treatment tank. Exhaust gas pumping device that sends water into the wastewater treatment tank, treated water drainage pipe that drains water in the wastewater treatment tank connected to the wastewater treatment tank, control device that operates the boiler and opens and closes the blow valve. The provided, communicates the wastewater treatment tank upper flue, provided the water level detector for detecting the water level in the waste water treatment tank in advance by connecting the control device and the water level detector,
When the water level detector detects that the water level in the wastewater treatment tank is higher than a certain level, the blow valve is closed. Also, set the blow time in the control device,
The blow valve opening time when the blow valve is opened is detected, and even after the set blow time has elapsed, the water level detector detects that the water level in the wastewater treatment tank is higher than a certain level. If not, a blow abnormality alarm is output.

【0006】[0006]

【発明の実施の形態】本発明の一実施例を図面を用いて
説明する。蒸気ボイラ1は、上部にボイラ内の缶水を加
熱するための火炎を発生させる燃焼装置2、側部に蒸気
と缶水を分離する気水分離器4、缶水を加熱した後の燃
焼排ガスを通す煙道5が設けられており、煙道5に設け
たエコノマイザ7で予熱された水をボイラへ給水するた
めの給水配管6、濃縮の進んだ缶水を取り出す濃縮ブロ
ー水配管8、ボイラ下部から缶水を排出する全ブロー配
管11が接続されている。濃縮ブロー水配管8の途中に
濃縮ブロー弁9、全ブロー配管11の途中に全ブロー弁
12が設けられており、濃縮ブロー水配管8と全ブロー
配管11は合流してブロー水配管15となる。濃縮ブロ
ー弁9および全ブロー弁12の開閉制御はボイラの制御
装置21からの信号にて行われており、濃縮ブロー弁9
または全ブロー弁12を開いたとき、ブロー水をためる
排水処理タンク10上部よりブロー水が噴射される様に
なっている。排水処理タンク10の内部は仕切板13で
2部屋に分割され、タンク上部と底部のタンク連絡口1
4のみで連通されており、ブロー水配管15によってブ
ロー水が供給される部屋を第1室16、他方の部屋を第
2室17としておく。第2室17の側面には、水位が設
定水位Lの高さよりも高くなったときに第2室17内の
水を排水する処理水排水管18、処理水排水管18の途
中に通常時開である処理水排水電動弁24が設けられて
おり、また設定水位Lよりも高い設定水位Hでの水の有
無を検出する水位検出器19を設ける。排水処理タンク
10の底部にも処理水排水管が接続されており、途中に
通常時閉である処理タンクブロー用電動弁23を設け
る。排水処理タンク10の上部では、排水処理タンク1
0と煙道5を連通する通気口3を設け、排水処理タンク
10と煙道5を一体化する。煙道5と第1室16および
第2室17内の底部を排ガス配管20で接続し、排ガス
配管20途中に排ガス圧送装置(図示せず)を設け、排
水処理タンク10内には熱交換器22を設けておき、熱
交換器22で予熱を行った水を給水配管6を通して蒸気
ボイラ1へ給水する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to the drawings. The steam boiler 1 includes a combustion device 2 for generating a flame for heating canned water in the boiler at an upper part, a steam separator 4 for separating steam and canned water at a side, and a combustion exhaust gas after heating the canned water. A flue 5 for passing through is provided, and a water supply pipe 6 for supplying water preheated by an economizer 7 provided in the flue 5 to a boiler, a concentrated blow water pipe 8 for taking out highly concentrated can water, a boiler All blow pipes 11 for discharging canned water from the lower part are connected. A concentrated blow valve 9 is provided in the middle of the concentrated blow water pipe 8, and an all blow valve 12 is provided in the middle of all blow pipes 11. The concentrated blow water pipe 8 and all the blow pipes 11 merge to form a blow water pipe 15. . Opening / closing control of the enrichment blow valve 9 and all the blow valves 12 is performed by a signal from the control device 21 of the boiler.
Alternatively, when all the blow valves 12 are opened, the blow water is sprayed from the upper part of the wastewater treatment tank 10 that stores the blow water. The inside of the wastewater treatment tank 10 is divided into two rooms by a partition plate 13, and the tank connection port 1 at the top and bottom of the tank 1
The room which is communicated with only 4 and is supplied with the blow water by the blow water pipe 15 is the first chamber 16 and the other room is the second chamber 17. On the side surface of the second chamber 17, the treated water drain pipe 18 for draining the water in the second chamber 17 when the water level becomes higher than the set water level L, and the normally open midway of the treated water drain pipe 18. And a water level detector 19 for detecting the presence or absence of water at a set water level H higher than the set water level L. A treated water drainage pipe is also connected to the bottom of the drainage treatment tank 10, and an electrically operated valve 23 for blowing the treated tank, which is normally closed, is provided on the way. At the upper part of the wastewater treatment tank 10, the wastewater treatment tank 1
0 is provided with a ventilation port 3 communicating with the flue 5, and the wastewater treatment tank 10 and the flue 5 are integrated. The flue 5 and the bottoms of the first chamber 16 and the second chamber 17 are connected by an exhaust gas pipe 20, an exhaust gas pumping device (not shown) is provided in the exhaust gas pipe 20, and a heat exchanger is provided in the wastewater treatment tank 10. 22 is provided and the water preheated by the heat exchanger 22 is supplied to the steam boiler 1 through the water supply pipe 6.

【0007】蒸気ボイラ1は缶内水位が一定の範囲を保
つように給水配管6を通じて給水されており、燃焼装置
2によって火炎を発生させることで缶水を加熱し、蒸気
を発生させる。缶水を沸騰させると蒸気とともに缶水が
持ち上げられるが、蒸気と缶水は気水分離器4で分離さ
れて、蒸気のみが取り出され、缶水は気水分離器4から
ボイラ内へ戻される。缶水を加熱した後の燃焼排ガス
は、煙道5へ送られ、エコノマイザ7によって給水を予
熱した後で排気される。
The steam boiler 1 is supplied with water through a water supply pipe 6 so that the water level in the can is maintained within a certain range. The combustion device 2 causes a flame to be generated to heat the can water to generate steam. When boiling the canned water, the canned water is lifted together with the steam, but the steam and the canned water are separated by the steam-water separator 4, only steam is taken out, and the steamed water is returned from the steam-water separator 4 into the boiler. . The combustion exhaust gas after heating the canned water is sent to the flue 5, and is preheated by the economizer 7 to be exhausted.

【0008】蒸気ボイラ1は缶水が蒸発するごとに給水
が行われており、水中に含まれている不純物は蒸発と給
水が繰り返されることで濃縮されるため、濃縮が進まな
いように濃縮ブロー弁9を定期的に開く濃縮ブローが行
われる。また、濃縮によって不純物が固定化したものが
底部に堆積し、釜泥となるため全ブロー弁12を開き、
底部より缶水を排水する全ブローを行うことで釜泥の排
出を行う。ブロー水はブロー水配管15を通して排水処
理タンク10へ送られており、濃縮ブローの実施間隔は
狭く、1回あたりの排水量は少量であり、全ブローの場
合は実施間隔が広く、一度に多量の排水が行われる。
The steam boiler 1 is supplied with water every time the canned water evaporates, and impurities contained in the water are concentrated by repeating evaporation and water supply. A concentration blow is performed in which the valve 9 is opened periodically. In addition, since impurities that have been fixed by concentration are deposited on the bottom and become kettle mud, all blow valves 12 are opened.
Kama mud is discharged by fully blowing the can water from the bottom. The blow water is sent to the wastewater treatment tank 10 through the blow water pipe 15, and the concentration interval of the concentration blow is narrow, and the amount of drainage per time is small. Drainage is done.

【0009】煙道5へ送られた燃焼排ガスの一部を、煙
道5に接続された排ガス配管20の途中に設けた排ガス
圧送装置によって排ガス配管20へ吸引し、第1室16
および第2室17内の処理水中に送り込む。処理水中に
送り込まれた燃焼排ガスは燃焼排ガス中の二酸化炭素な
どと処理水中の水酸化物イオンで中和反応し、処理水の
pHを低下させる。排水処理タンク上部に達した燃焼排
ガスは通気口3によって煙道5へ戻され、排気される。
A part of the combustion exhaust gas sent to the flue 5 is sucked into the exhaust gas pipe 20 by an exhaust gas pumping device provided in the middle of the exhaust gas pipe 20 connected to the flue 5, and the first chamber 16
And it is sent into the treated water in the second chamber 17. The flue gas discharged into the treated water undergoes a neutralization reaction with carbon dioxide in the flue gas with hydroxide ions in the treated water to lower the pH of the treated water. The combustion exhaust gas reaching the upper part of the wastewater treatment tank is returned to the flue 5 by the ventilation port 3 and exhausted.

【0010】排水処理タンク10へ送られたブロー水
は、まず第1室16で燃焼排ガスによって中和処理が行
われ、pHが低下させられる。第1室16と第2室17
はタンク連絡口14で連通されているため、排水処理タ
ンク10内の処理水は第1室16から第2室17へ徐々
に移動し、第2室17へ達した処理水は第2室17内で
再度中和処理が行われ、第2室内で処理の行われた処理
水は、設定水位Lの高さに設けた処理水排水管18を通
じて排水される。排水処理タンク10内を第1室16と
第2室17に分割し、第1室16で中和処理後、第2室
17で再度中和処理が行われるので、排水処理タンク1
0へ送られたブロー水が中和されないまますぐに排水さ
れることはなく、処理水のpHを十分に低下させること
ができる。
The blow water sent to the waste water treatment tank 10 is first subjected to a neutralization treatment by the combustion exhaust gas in the first chamber 16 to lower the pH. First chamber 16 and second chamber 17
Are communicated with each other through the tank communication port 14, the treated water in the wastewater treatment tank 10 gradually moves from the first chamber 16 to the second chamber 17, and the treated water reaching the second chamber 17 is treated in the second chamber 17. The treated water that has been subjected to the neutralization treatment again inside and is treated inside the second chamber is drained through the treated water drain pipe 18 provided at the height of the set water level L. Since the inside of the wastewater treatment tank 10 is divided into a first chamber 16 and a second chamber 17, and the neutralization process is performed again in the second chamber 17 after the neutralization process in the first chamber 16, the wastewater treatment tank 1
The blow water sent to No. 0 is not immediately drained without being neutralized, and the pH of the treated water can be sufficiently lowered.

【0011】濃縮ブローの場合、1回当たりのブロー水
量が少ないために排水処理タンク10内水位の変動は僅
かであるが、全ブローの場合、1度に多量のブロー水が
排水処理タンク10へ送られることとなる。しかし、全
ブローの目的は釜泥の排出であるため、一定量のブロー
が確実に行われるのであれば缶水を全て排水する必要は
ないため、全ブロー実施の前に処理タンクブロー用電動
弁23を開いて排水処理タンク内の処理水を排水してお
き、処理タンクブロー用電動弁23を閉じた後で全ブロ
ー弁12を開き、排水処理タンク10内に設けた水位検
出器19によって設定水位Hまで水位変化があったこと
が検出されると、全ブロー弁12を閉じて全ブローを停
止させる。この場合、排水処理タンク10の容量を必要
以上に大きくしなくても一定量のブローを確実に行える
ので、排水処理タンク10の容量を小型化することがで
き、排水処理タンク10内水位の上昇によって通気口3
より煙道5内へブロー水が流入するおそれも無くなり、
排水処理タンク10から排水される水は半ばまででも中
和処理が行われているので、ボイラからのブロー水が未
処理のまま排出されることはない。
In the case of the concentrated blow, the fluctuation of the water level in the wastewater treatment tank 10 is small because the amount of blown water per time is small, but in the case of the full blow, a large amount of blown water flows to the wastewater treatment tank 10 at one time. Will be sent. However, since the purpose of full blow is to discharge the mud, it is not necessary to drain all the can water if a certain amount of blow can be reliably performed. 23 is opened to drain the treated water in the wastewater treatment tank, the electric motor 23 for blowing the treatment tank is closed, and then all the blow valves 12 are opened to set by the water level detector 19 provided in the wastewater treatment tank 10. When it is detected that the water level has changed to the water level H, all blow valves 12 are closed to stop all blows. In this case, a certain amount of blow can be reliably performed without increasing the capacity of the wastewater treatment tank 10 more than necessary, so that the capacity of the wastewater treatment tank 10 can be downsized and the water level in the wastewater treatment tank 10 rises. By vent 3
There is no fear that blow water will flow into the flue 5,
Since the water discharged from the waste water treatment tank 10 has been neutralized even in the middle, the blow water from the boiler is not discharged untreated.

【0012】また、制御装置21には、全ブローを行っ
た場合に排水処理タンク10内の水位が設定水位Hまで
上昇する時間が設定時間として入力されており、全ブロ
ー弁12を開いてからの時間の検出を行う。全ブロー弁
12の開時間が設定時間に達しても設定水位Hまで水位
が上昇しなかった場合にはブロー異常の出力を行う。
Further, the control device 21 is input with a set time period in which the water level in the wastewater treatment tank 10 rises to the set water level H when all the blows are performed, and after all the blow valves 12 are opened. The time is detected. If the water level does not rise to the set water level H even when the opening time of all the blow valves 12 reaches the set time, the blow abnormality is output.

【0013】[0013]

【発明の効果】本発明を実施することにより、排水処理
タンクと煙道は一体化され、排水処理タンクの容量が小
さくなるので蒸気ボイラの排水処理装置を小型化するこ
とができ、適正なブローを行うことができる。
By implementing the present invention, since the wastewater treatment tank and the flue are integrated and the capacity of the wastewater treatment tank is reduced, the wastewater treatment apparatus of the steam boiler can be downsized and the proper blow can be performed. It can be performed.

【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 蒸気ボイラ 2 燃焼装置 3 通気口 4 気水分離器 5 煙道 6 給水配管 7 エコノマイザ 8 濃縮ブロー水配管 9 濃縮ブロー弁 10 排水処理タンク 11 全ブロー配管 12 全ブロー弁 13 仕切板 14 タンク連絡口 15 ブロー水配管 16 第1室 17 第2室 18 処理水排水管 19 水位検出器 20 排ガス配管 21 制御装置 22 熱交換器 23 処理タンクブロー用電動弁 24 処理水排水電動弁 H・L 設定水位 1 Steam Boiler 2 Combustor 3 Vent 4 Gas / Water Separator 5 Flue 6 Water Supply Pipe 7 Economizer 8 Concentrated Blow Water Pipe 9 Concentrated Blow Valve 10 Waste Water Treatment Tank 11 All Blow Pipe 12 All Blow Valve 13 Partition Plate 14 Tank Connection Port 15 Blow water pipe 16 1st chamber 17 2nd chamber 18 Treated water drainage pipe 19 Water level detector 20 Exhaust gas pipe 21 Control device 22 Heat exchanger 23 Treatment tank blow motor valve 24 Treated water drain motor valve H / L set water level

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 ボイラの炉内で燃焼を行うことで蒸気を
発生させ、蒸発によって濃縮される缶水は定期的に排水
を行い、缶水を加熱した後の燃焼排ガスは煙道を通して
排気している蒸気ボイラの排水処理装置であって、ボイ
ラから排水されるアルカリ性のブロー水をためる排水処
理タンク、ボイラの缶水部を排水処理タンクに送るブロ
ー水配管、弁の開閉によって排水処理タンクへ缶水を送
るブロー制御を行うブロー弁、一端は煙道の燃焼排ガス
流動部に接続され、他端は排水処理タンクの水中部に接
続されている排ガス配管、排ガス配管途中に燃焼排ガス
を排水処理タンク内へ送り込む排ガス圧送装置、排水処
理タンクに接続された排水処理タンク内の水を排水する
処理水排水管、ボイラの運転やブロー弁の開閉を行う制
御装置を設け、排水処理タンク上部と煙道を連通させた
ことを特徴とする排水処理装置付き蒸気ボイラ。
Claims: 1. Steam is generated by performing combustion in a furnace of a boiler, and can water concentrated by evaporation is periodically discharged, and combustion exhaust gas after heating the can water is exhausted through a flue. Waste water treatment equipment for steam boilers that stores alkaline blow water discharged from the boiler, blow water piping that sends the boiler's can water to the waste water treatment tank, and opens and closes the valve to reach the waste water treatment tank. Blow valve for blow control to send canned water, one end is connected to the flue gas flow section of the flue, and the other end is connected to the underwater section of the waste water treatment tank. Exhaust gas pumping device for sending into the tank, treated water drainage pipe for draining water in the wastewater treatment tank connected to the wastewater treatment tank, control device for operating the boiler and opening and closing the blow valve are installed. A steam boiler with a wastewater treatment device, characterized in that the upper part of the treatment tank is connected to the flue.
【請求項2】 請求項1に記載の排水処理装置付き蒸気
ボイラにおいて、排水処理タンク内の水位を検出する水
位検出器を設け、水位検出器と制御装置を接続してお
き、水位検出器によって排水処理タンク内の水位が一定
の水位よりも高くなったことが検出されたとき、ブロー
弁の閉制御を行うことを特徴とする排水処理装置付き蒸
気ボイラ。
2. The steam boiler with a wastewater treatment device according to claim 1, further comprising a water level detector for detecting the water level in the wastewater treatment tank, the water level detector and the control device being connected to each other by the water level detector. A steam boiler with a wastewater treatment device, which performs a closing control of a blow valve when it is detected that the water level in the wastewater treatment tank is higher than a certain level.
【請求項3】 請求項2に記載の排水処理装置付き蒸気
ボイラにおいて、ブロー弁を開いてから一定時間経過し
ても排水処理タンク内の水位が一定以上とならなかった
場合、ブロー異常の警報を出力することを特徴とする排
水処理装置付き蒸気ボイラ。
3. The steam boiler with wastewater treatment device according to claim 2, wherein when the water level in the wastewater treatment tank does not reach a certain level or more even after a certain time has elapsed since the blow valve was opened, a blow abnormality alarm is issued. Is a steam boiler with a wastewater treatment device.
【請求項4】 請求項1に記載の排水処理装置付き蒸気
ボイラにおいて、排水処理タンク内に熱交換器を設け、
ボイラへの給水配管を前記熱交換器の前後に接続してお
き、排水処理タンク内で予熱された水をボイラへ供給す
る構成としたことを特徴とする排水処理装置付き蒸気ボ
イラ。
4. The steam boiler with wastewater treatment device according to claim 1, wherein a heat exchanger is provided in the wastewater treatment tank,
A steam boiler with a wastewater treatment device, characterized in that water supply pipes to the boiler are connected before and after the heat exchanger to supply water preheated in the wastewater treatment tank to the boiler.
【請求項5】 請求項2に記載の排水処理装置付き蒸気
ボイラにおいて、ブロー弁の開制御を行う際、排水処理
タンク内の水を排水処理配管を通じて排水しておき、そ
の後にブロー弁を開制御することを特徴とする排水処理
装置付き蒸気ボイラ。
5. In the steam boiler with wastewater treatment device according to claim 2, when controlling the opening of the blow valve, the water in the wastewater treatment tank is drained through the wastewater treatment pipe, and then the blow valve is opened. A steam boiler with a wastewater treatment device that is controlled.
JP8078331A 1996-03-05 1996-03-05 Steam boiler with wastewater treatment equipment Expired - Fee Related JP2987323B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8078331A JP2987323B2 (en) 1996-03-05 1996-03-05 Steam boiler with wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8078331A JP2987323B2 (en) 1996-03-05 1996-03-05 Steam boiler with wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPH09243013A true JPH09243013A (en) 1997-09-16
JP2987323B2 JP2987323B2 (en) 1999-12-06

Family

ID=13659001

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8078331A Expired - Fee Related JP2987323B2 (en) 1996-03-05 1996-03-05 Steam boiler with wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JP2987323B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001293484A (en) * 2000-04-17 2001-10-23 Miura Co Ltd Method and device for neutralizing boiler waste water
KR100332695B1 (en) * 1999-12-15 2002-04-17 손재익 Apparatus for Neutralizing of Condensate for Anti-corrosion of Heat Exchanger Surface and Method Theirof
KR100361315B1 (en) * 2000-07-10 2002-11-18 주식회사 경동보일러 Corr0sion inhibit and neutralization units of gas boiler
JP2002364806A (en) * 2001-06-12 2002-12-18 Samson Co Ltd Boiler conducting control for performing no concentration blow immediately after can bottom blow
JP2014105953A (en) * 2012-11-29 2014-06-09 Takasago Thermal Eng Co Ltd Heat exchange device of blow waste water
JP2015111016A (en) * 2013-12-06 2015-06-18 三浦工業株式会社 Boiler apparatus
CN104913323A (en) * 2015-06-23 2015-09-16 丹东蓝天环保锅炉制造有限公司 Flue gas purifying and waste heat recovering boiler
JP2016095091A (en) * 2014-11-14 2016-05-26 株式会社サムソン Boiler with thermal management device
CN111855331A (en) * 2020-08-07 2020-10-30 江苏省特种设备安全监督检验研究院 Boiler detection sampling device convenient to adjust

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100332695B1 (en) * 1999-12-15 2002-04-17 손재익 Apparatus for Neutralizing of Condensate for Anti-corrosion of Heat Exchanger Surface and Method Theirof
JP2001293484A (en) * 2000-04-17 2001-10-23 Miura Co Ltd Method and device for neutralizing boiler waste water
KR100361315B1 (en) * 2000-07-10 2002-11-18 주식회사 경동보일러 Corr0sion inhibit and neutralization units of gas boiler
JP2002364806A (en) * 2001-06-12 2002-12-18 Samson Co Ltd Boiler conducting control for performing no concentration blow immediately after can bottom blow
JP4566462B2 (en) * 2001-06-12 2010-10-20 株式会社サムソン Boiler that controls to not perform the concentration blow immediately after the bottom blow
JP2014105953A (en) * 2012-11-29 2014-06-09 Takasago Thermal Eng Co Ltd Heat exchange device of blow waste water
JP2015111016A (en) * 2013-12-06 2015-06-18 三浦工業株式会社 Boiler apparatus
JP2016095091A (en) * 2014-11-14 2016-05-26 株式会社サムソン Boiler with thermal management device
CN104913323A (en) * 2015-06-23 2015-09-16 丹东蓝天环保锅炉制造有限公司 Flue gas purifying and waste heat recovering boiler
CN111855331A (en) * 2020-08-07 2020-10-30 江苏省特种设备安全监督检验研究院 Boiler detection sampling device convenient to adjust
CN111855331B (en) * 2020-08-07 2023-03-10 江苏省特种设备安全监督检验研究院 Boiler detection sampling device convenient to adjust

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