JPH07313993A - Apparatus and method for treating boiler supply water - Google Patents

Apparatus and method for treating boiler supply water

Info

Publication number
JPH07313993A
JPH07313993A JP10926394A JP10926394A JPH07313993A JP H07313993 A JPH07313993 A JP H07313993A JP 10926394 A JP10926394 A JP 10926394A JP 10926394 A JP10926394 A JP 10926394A JP H07313993 A JPH07313993 A JP H07313993A
Authority
JP
Japan
Prior art keywords
water
silica
boiler
alkali
softened
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.)
Pending
Application number
JP10926394A
Other languages
Japanese (ja)
Inventor
Masato Tanaka
政人 田中
Shigeru Matsugami
茂 松上
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.)
Takuma Co Ltd
Original Assignee
Takuma 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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP10926394A priority Critical patent/JPH07313993A/en
Publication of JPH07313993A publication Critical patent/JPH07313993A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To reduce the carry-over of silica and to prevent the adhesion of scale to steam piping by softening raw water and polymerizing silica in softened water and adding a predetermined amt. of alkali to the treated softened water to prepare boiler supply water. CONSTITUTION:At first, raw water supplied from raw water piping 1 is introduced into a softening device 2 utilizing an ion exchange agent and a magnesium ion or a calcium ion is removed to soften raw water. Next, softened water is treated in a silica polymerizing device 3 and silica in the softened water is polymerized to be suspended and dispersed in water. Continuously, the treated softened water is supplied to a low pressure boiler 7 heretofore as supply water from a storage tank 4 by a pump 5 but, in this case, a chemical injection device 6 is used to add a predetermined amt. of alkali to the supply water. At this time, alkali is added so that the acid consumption amt. of boiler water becomes at least 1.7 times the content of silica. By this constitution, the carry-over of silica is reduced and the adhesion of scale is prevented.

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、ボイラ補給水の処理装
置および処理方法に関し、とくに、シリカ含有量の多い
原水を処理してボイラ補給水を得るのに好適である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for treating boiler makeup water, and is particularly suitable for treating raw water having a high silica content to obtain boiler makeup water.

【0002】[0002]

【従来の技術】わが国は一般に原水(工業用水など)の
硬度が低いので、多くのボイラでは、イオン交換剤を充
填した硬水軟化装置を用いて原水を処理し、軟化水にし
て補給水に使用していた。最近、ボイラの高温高圧化が
進み、陽・陰イオン両交換樹脂樹脂を用いた純水装置で
処理するイオン交換水が補給水に利用されるようになっ
たが、多くのボイラ、とくに低圧ボイラでは、依然、上
記の軟化水が用いられている。
BACKGROUND ART In Japan, the hardness of raw water (industrial water, etc.) is generally low, so in many boilers, the raw water is treated with a water softening device filled with an ion exchange agent and used as makeup water. Was. Recently, as the temperature and pressure of boilers have increased, ion-exchanged water treated with a deionizer using both cation and anion exchange resin has come to be used as makeup water, but many boilers, especially low-pressure boilers. However, the above softened water is still used.

【0003】[0003]

【発明が解決しようとする課題】ところで、わが国の天
然水は一般にシリカ濃度が高く、従って原水中のシリカ
濃度も高い。この内、懸濁状やコロイド状のシリカは、
凝集沈殿・ろ過処理で分離することができるし、高温で
アルカリ性のボイラ水中では加水分解してイオン状シリ
カに変化する。イオン状になって水中に溶存するシリカ
は、純水装置を用いれば、強塩基性陰イオン交換樹脂に
吸着させ、分離することができるが、硬水軟化装置に使
用している陽イオン交換樹脂などでは分離できない。シ
リカは水に対する溶解度が比較的低いので、ボイラ補給
水中のシリカ濃度が高いと、ボイラ水中のシリカ濃度も
高くなり、ボイラドラムや水管にスケールを付着させや
すくなる。さらに、ボイラ水のキャリオーバによって蒸
気配管に硬質のスケールを付着させやすくなる。このた
め、軟化水を利用しているボイラでは、生成したスケー
ルがボイラの熱効率を低下させ、閉塞事故の原因などに
もなっていた。
By the way, natural water in Japan generally has a high silica concentration, and therefore the silica concentration in raw water is also high. Of these, suspended and colloidal silica is
It can be separated by coagulation-sedimentation and filtration, and hydrolyzes in alkaline boiler water at high temperature to change to ionic silica. Silica, which becomes ionic and dissolves in water, can be adsorbed on a strongly basic anion exchange resin and separated by using a pure water device, but cation exchange resin used in a water softening device, etc. Can't separate. Since silica has a relatively low solubility in water, if the silica concentration in the boiler make-up water is high, the silica concentration in the boiler water will also be high, and the scale will be easily attached to the boiler drum and the water pipe. Further, the carry-over of boiler water facilitates the attachment of hard scale to the steam pipe. For this reason, in a boiler that uses softened water, the generated scale reduces the thermal efficiency of the boiler, which is also a cause of a blockage accident.

【0004】軟化水を補給水として使用するボイラのシ
リカスケール生成防止には、実用的に2つの方法が利用
されている。その第1は、シリカを可溶性化合物に変換
して析出を防止する、たとえばJIS B8223−1
989に記載の方法であって、次式に示す反応を利用
し、アルカリを添加してボイラ水中のシリカが可溶性の
メタけい酸ナトリウムになるように、ボイラ水の酸消費
量(pH8.3、以下同じ)を調節する。
Two methods are practically used to prevent the formation of silica scale in a boiler using softening water as makeup water. The first is to convert silica to a soluble compound to prevent precipitation, for example JIS B8223-1.
989, using the reaction shown in the following formula, so that alkali in the boiler water so that the silica in the boiler water becomes soluble sodium metasilicate, acid consumption of the boiler water (pH 8.3, The same applies hereinafter).

【0005】 SiO2 +2NaOH=Na2 SiO3 +H2 O 第2は、シリカを析出しないよう多量体化し、浮遊・分
散化させてブローし、排出する方法である。浮遊・分散
化させるには、たとえば、ボイラ研究No.251(ボ
イラ協会)などに記載されている合成高分子電解質を使
用する方法や、「水の磁気処理」(ヴェ・イ・クラッセ
ン)などに紹介されている高周波磁場(電場を含む、以
下同じ)内で補給水を処理する方法があげられる。高周
波磁場内でシリカを多量体化する方法は、最近開発され
その原理はまだ十分に解明されていないが、簡単な装置
でボイラドラムや水管へのシリカのスケール化を防止で
きるので、各所で採用されるようになってきた。
SiO 2 + 2NaOH = Na 2 SiO 3 + H 2 O The second is a method in which silica is polymerized so as not to be precipitated, suspended and dispersed, blown, and discharged. In order to float and disperse, for example, boiler research No. 251 (Boiler Association) and other methods using synthetic polymer electrolytes, and "Magnetic treatment of water" (Ve Krassen) and other high frequency magnetic fields (including electric fields, the same applies below) There is a method of treating makeup water inside. A method for polymerizing silica in a high-frequency magnetic field has been recently developed and its principle has not been fully clarified, but it is adopted in various places because it can prevent silica from scaling on the boiler drum and water pipe with a simple device. It has started to be done.

【0006】ところで、前記第1の方法によれば、上式
によってシリカをメタけい酸ナトリウムに保つのに必要
なボイラ水の酸消費量を、少なくとも1.7倍(1mg
のシリカに対し、水酸化ナトリウム1.33mg、炭酸
カルシウム換算約1.7mg)に保つ必要がある。しか
し、ボイラ水の酸消費量には障害を防止するためJIS
などに目標値が設けられており、シリカ濃度の高い補給
水では、薬剤を添加してボイラ水の酸消費量を1.7倍
以上に維持することが困難になるという欠点がある。一
方、これに代えて用いられるようになってきた高周波磁
場を利用する方法では、意外にもボイラ水のシリカ濃度
が高いと予想を遥かに超えるシリカが蒸気側にキャリオ
ーバし、蒸気配管にスケールを形成して閉塞させるとい
う問題のあることが判明してきた。
By the way, according to the first method, the acid consumption of boiler water required to keep silica in sodium metasilicate according to the above formula is at least 1.7 times (1 mg).
It is necessary to keep 1.33 mg of sodium hydroxide and about 1.7 mg of calcium carbonate based on the above silica. However, in order to prevent obstacles to acid consumption of boiler water, JIS
There is a drawback that it is difficult to add chemicals to maintain the acid consumption of boiler water to 1.7 times or more in makeup water having a high silica concentration. On the other hand, in the method using a high-frequency magnetic field that has been used instead of this, surprisingly, when the silica concentration in the boiler water is high, silica far exceeding the expectation is carried over to the steam side, and a scale is added to the steam pipe. It has been found that there is a problem of forming and blocking.

【0007】本発明は、これらの問題、とくに高周波磁
場内で処理したシリカのキャリオーバ問題を解決し、長
期にわたって安定したボイラ操業を可能にする、ボイラ
補給水の処理装置および処理方法の提供を目的にするも
のである。
The present invention solves these problems, particularly the carryover problem of silica treated in a high frequency magnetic field, and provides a treatment apparatus and a treatment method for boiler make-up water, which enables stable boiler operation for a long period of time. It is something to do.

【0008】[0008]

【課題を解決するための手段】本発明は、前記の目的を
達成するために、原水を軟化水化する軟化装置と、軟化
装置で処理された軟化水中のシリカを高周波を用いて多
量体化するシリカ多量体化装置と、シリカ多量体化装置
で処理された軟化水に所定量のアルカリを添加してボイ
ラ補給水とする薬注装置とからなることを特徴とする、
ボイラ補給水の処理装置を提供する。また、原水をイオ
ン交換剤を用いて軟化水化し、得られた軟化水を高周波
磁場内を通過させて含有するシリカを多量体化し、高周
波磁場内を通過させた軟化水に、ボイラ水の酸消費量が
シリカ含有量の少なくとも1.7倍になるようにアルカ
リを添加して、ボイラ補給水を得ることを特徴とする、
ボイラ補給水の処理方法を提供する。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention multimerizes a softening device for softening raw water and silica in the softened water treated by the softening device by using high frequency. Characterized in that it comprises a silica multimerizing device, and a chemical dosing device that makes a boiler makeup water by adding a predetermined amount of alkali to the softening water treated by the silica multimerizing device.
A treatment device for boiler makeup water is provided. Further, the raw water is softened using an ion exchange agent, the resulting softened water is passed through a high-frequency magnetic field to polymerize silica contained therein, and the softened water passed through the high-frequency magnetic field is added to the acid of the boiler water. Characterized in that an alkali is added so that the consumption is at least 1.7 times the silica content to obtain boiler make-up water.
A method for treating boiler makeup water is provided.

【0009】[0009]

【作用と実施態様例】本発明のボイラ補給水処理装置お
よび処理方法について、図面を参照しながら実施態様例
をあげて説明する。図1は、本発明の実施態様例を示す
フローシートである。
Actions and Examples of Embodiments A boiler makeup water treatment apparatus and a treatment method of the present invention will be described with reference to the drawings by way of example embodiments. FIG. 1 is a flow sheet showing an embodiment of the present invention.

【0010】本発明においては、原水配管1から供給さ
れる原水を、まず、イオン交換剤を利用した軟化装置2
に送入し、主にマグネシウムイオンとカルシウムイオン
とを除去して軟化水化する。本発明には、通常の陽イオ
ン交換樹脂を用いた軟化装置の利用が一般的であるが、
ゼオライトなどの無機交換剤を用いることもできる。供
給する原水に固形成分が含まれる場合には、凝集沈殿装
置やろ過装置を用いて予め除去しておく。
In the present invention, the raw water supplied from the raw water pipe 1 is first treated by the softening device 2 using an ion exchange agent.
And removes mainly magnesium ions and calcium ions to soften and water. In the present invention, it is general to use a softening device using an ordinary cation exchange resin,
It is also possible to use an inorganic exchange agent such as zeolite. When the raw water to be supplied contains solid components, it is removed in advance by using a coagulating sedimentation device or a filtration device.

【0011】次に、軟化装置2で処理された軟化水を、
シリカ多量体化装置3を用いて処理し、含まれるシリカ
を多量体化して、水中の浮遊・分散させる。シリカ多量
体化装置3は、理論的説明は確立されてはいないが、シ
リカの固有振動に同調するとされる共振高周波によって
発信装置中で水を処理するもので、モノマーのシリカが
振動され、固有振動と共振、活性化して多量体化(ポリ
マ化)するとされている。このシリカ多量体化装置3
は、水処理用装置として市中で容易に入手できる。4は
貯槽である。
Next, the softening water treated by the softening device 2 is
The treatment is performed by using the silica multimerization apparatus 3, and the silica contained therein is polymerized to be suspended / dispersed in water. Although the theoretical explanation has not been established, the silica multimerization device 3 treats water in the transmitter by a resonance high frequency that is supposed to be tuned to the natural vibration of silica. It is said that it is resonated with vibration and activated to become a polymer (polymer). This silica multimerizer 3
Is easily available in the city as a water treatment device. 4 is a storage tank.

【0012】シリカ多量体化装置3で処理された軟化水
は、従来、補給水として貯槽4からポンプ5により低圧
ボイラ7に補給されていたが、本発明においては薬注装
置6を用い、補給水には所定量のアルカリを添加する。
添加するアルカリとしては、経済性の点で水酸化ナトリ
ウム水溶液が好ましく使用されるが、これに限定される
ものではなく、水酸化カリウム水溶液などを使用しても
よい。アルカリは、ボイラ水の酸消費量がシリカ含有量
の少なくとも約1.7倍になるように添加する。1.7
倍を下回る量であると、キャリオーバして蒸気配管など
に付着し、スケール化するシリカが増大する。ボイラ水
の酸消費量はJIS B8224−1993に記載の方
法で測定し、アルカリ注入量を調整するとよい。薬注装
置としては、補給水中に定量的にアルカリを供給できれ
ばよく、特別な制限はない。8は気水分離器、9は蒸気
配管である。
Conventionally, the softening water treated by the silica multimerization apparatus 3 was replenished to the low-pressure boiler 7 from the storage tank 4 by the pump 5 as make-up water. A predetermined amount of alkali is added to water.
As the alkali to be added, an aqueous sodium hydroxide solution is preferably used in terms of economy, but the alkali is not limited to this, and an aqueous potassium hydroxide solution or the like may be used. The alkali is added so that the acid consumption of the boiler water is at least about 1.7 times the silica content. 1.7
If the amount is less than double, the amount of silica that is scaled up increases due to carryover and adhesion to steam pipes. The acid consumption of boiler water may be measured by the method described in JIS B8224-1993, and the alkali injection amount may be adjusted. The chemical injection device is not particularly limited as long as it can quantitatively supply the alkali into the makeup water. Reference numeral 8 is a steam separator, and 9 is a steam pipe.

【0013】[0013]

【実施例】つぎに、従来の方法で処理した補給水を用い
て運転していたボイラに、本発明のボイラ補給水の処理
装置と処理方法とを適用して運転したので、実施例とし
てその結果を説明する。
EXAMPLES Next, the boiler make-up water treatment apparatus and the treatment method of the present invention were applied to the boiler which was operated by using the make-up water treated by the conventional method. The results will be explained.

【0014】蒸発量1000kg/h、最高圧力1MP
a、常用圧力0.7MPaの小型貫流ボイラ(TW−1
000型:(株)タクマ製)に、軟化装置(樹脂量54
リットル:TS−54BF:(株)タクマ製)と高周波
磁場を用いた市販のシリカ多量体化装置を用いて原水を
処理し、補給水としてし運転していた。運転状況を表1
に示す。表1に示すように、ボイラ水中のシリカ濃度が
高く、約2500時間経過後に運転を中止して、蒸気配
管に付着したシリカスケールを除去しなければならなか
った。
Evaporation rate 1000 kg / h, maximum pressure 1MP
a, a small once-through boiler with a normal pressure of 0.7 MPa (TW-1
Type 000: Takuma Co., Ltd., softening device (resin amount 54
Lithium: TS-54BF: manufactured by Takuma Co., Ltd.) and a commercially available silica multimerization apparatus using a high frequency magnetic field were used to treat the raw water and use it as make-up water for operation. Table 1 of driving situation
Shown in. As shown in Table 1, the silica concentration in the boiler water was high, and the operation had to be stopped after about 2500 hours to remove the silica scale adhering to the steam pipe.

【0015】[0015]

【表1】ボイラ水 pH 10〜10.3 酸消費量(pH4.8) 300〜500mg/l 酸消費量(pH8.3) 280〜470mg/l シリカ 200〜300mg/l 電気伝導率 500〜1000μS/c
m 酸消費量(pH8.3)/シリカ 約1.5 水管へのスケール付着 なし 蒸気配管へのシリカ付着 運転約2500時間で閉塞 そこで、アルカリ注入装置を設け、ボイラ水の酸消費量
がシリカ濃度の約2倍になるように、48重量%水酸化
ナトリウム水溶液を約5倍の軟化水で希釈し、市販の電
磁ポンプ注入装置を用い、平均2ml/minで補給水
中に添加した。ボイラ水の酸消費量は、JIS B82
24に記載の方法で当初7日ごとに測定し、アルカリ注
入量を確認し、その後は1月ごとに水質分析を実施して
いる。測定結果を表2に示す。運転開始約1000時間
後に内部を点検したが、蒸気配管にスケール付着の徴候
は全くはなく、また、ボイラ本体の水管や上下のヘッダ
などにもスケール付着はなく腐食の進行も見られなかっ
た。なお、現在も引続き運転を実施して本発明の効果を
さらに確認中であるが、スケールの付着を類推させるよ
うな徴候は見られず、良好な運転状態を継続している。
[Table 1] Boiler water pH 10 to 10.3 Acid consumption (pH 4.8) 300 to 500 mg / l Acid consumption (pH 8.3) 280 to 470 mg / l Silica 200 to 300 mg / l Electrical conductivity 500 to 1000 μS / C
m Acid consumption (pH 8.3) / silica Approx. 1.5 No scale adhesion to water pipe No silica adhesion to steam pipe Approximately 2500 hours of operation blockage Therefore, an alkali injection device was installed and the acid consumption of boiler water was silica concentration. 48% by weight aqueous solution of sodium hydroxide was diluted with about 5 times the softening water, and the resulting solution was added to the makeup water at an average of 2 ml / min using a commercially available electromagnetic pump injection device. The acid consumption of boiler water is JIS B82.
Initially, the method described in 24 is used to measure every 7 days, the amount of alkali injection is confirmed, and thereafter, water quality analysis is performed every month. The measurement results are shown in Table 2. When the inside was inspected about 1000 hours after the start of operation, there was no sign of scale adhesion on the steam piping, and there was no scale adhesion on the water pipe of the boiler body or the upper and lower headers, and no progress of corrosion was observed. It should be noted that although the operation of the present invention is still being carried out and the effects of the present invention are still being confirmed, no sign of analogy to scale adhesion is observed and the good operation state is continued.

【0016】[0016]

【表2】ボイラ水 pH 11〜11.5 酸消費量(pH4.8) 520〜700mg/l 酸消費量(pH8.3) 400〜600mg/l シリカ 200〜300mg/l 電気伝導率 1100〜1700μS/c
m 酸消費量(pH8.3)/シリカ 約2 水管へのスケール付着 なし 蒸気配管へのシリカ付着 なし
[Table 2] Boiler water pH 11 to 11.5 Acid consumption (pH 4.8) 520 to 700 mg / l Acid consumption (pH 8.3) 400 to 600 mg / l Silica 200 to 300 mg / l Electrical conductivity 1100 to 1700 μS / C
m Acid consumption (pH 8.3) / silica About 2 No scale adhered to water pipe No silica adhered to steam pipe

【0017】[0017]

【発明の効果】本発明のボイラ補給水の処理装置、ある
いは処理方法を利用すると、シリカ濃度の高い原水をボ
イラ補給水に処理しても、ボイラ水のアルカリ濃度が高
く保持されてシリカが可溶化し、現時点では理論的に必
ずしも明解に説明できないが、シリカのキャリオーバが
減少し、蒸気配管などのスケール付着を防止する顕著な
効果がある。また、ボイラ水処理のために清缶剤や脱酸
素剤などの薬剤を使用すると、蒸気に混入するおそれが
あるが、本発明では、通常、脱気塔の設置や脱酸素剤の
注入などの必要がない。水酸化ナトリウムなどのアルカ
リを使用するのみであるので、蒸気の安全性が高い。ま
た、排水問題への影響も少ないという効果がある。ま
た、最近、ボイラ水の濃縮管理に、ボイラ水の電気伝導
度を測定して行なう例が増加している。不溶のシリカが
多いとシリカが濃縮されているにも拘らず、電気伝導度
が上昇しにくいが、アルカリ添加によって、安定して濃
縮管理することができる。したがって、シリカ濃度の高
い原水を安心して使用できるという効果を奏する。簡易
な装置で経済的に処理できる。
EFFECTS OF THE INVENTION By using the boiler makeup water treatment apparatus or treatment method of the present invention, even if raw water having a high silica concentration is treated as boiler makeup water, the alkali concentration of the boiler water is kept high and silica can be treated. Although it cannot be clearly explained theoretically at present at the time of solubilization, the carry-over of silica is reduced, and there is a remarkable effect of preventing scale adhesion on steam pipes and the like. Further, if a chemical such as a boiler agent or an oxygen scavenger is used for treating boiler water, it may be mixed in the steam, but in the present invention, normally, a degassing tower is installed or an oxygen scavenger is injected. No need. Since only alkali such as sodium hydroxide is used, the safety of steam is high. In addition, the effect on the drainage problem is small. Further, recently, there is an increasing number of cases in which the electric conductivity of boiler water is measured to control the concentration of boiler water. If the amount of insoluble silica is large, the electrical conductivity is unlikely to increase even though the silica is concentrated, but the addition of alkali enables stable concentration management. Therefore, there is an effect that the raw water having a high silica concentration can be used without anxiety. Can be processed economically with a simple device.

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

【図1】 本発明の実施態様例を示すフローシート。FIG. 1 is a flow sheet showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:原水供給配管 2:軟化装置 3:シリカの多量体化装置 4:貯槽 5:給水ポ
ンプ 6:アルカリ注入装置 7:ボイラ本体 8:気水
分離器 9:蒸気配管
1: Raw water supply pipe 2: Softening device 3: Silica multimerization device 4: Storage tank 5: Water supply pump 6: Alkali injection device 7: Boiler main body 8: Steam separator 9: Steam pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】原水を軟化水化する軟化装置と、軟化装置
で処理された軟化水中のシリカを高周波を用いて多量体
化するシリカ多量体化装置と、シリカ多量体化装置で処
理された軟化水に所定量のアルカリを添加してボイラ補
給水とする薬注装置とからなることを特徴とする、ボイ
ラ補給水の処理装置。
1. A softening device for softening raw water, a silica multimerizing device for polymerizing silica in softened water treated by the softening device by using high frequency, and a silica multimerizing device for treating. A treatment device for boiler make-up water, comprising a chemical injection device for adding a predetermined amount of alkali to softened water to make boiler make-up water.
【請求項2】原水をイオン交換剤を用いて軟化水化し、 得られた軟化水を高周波磁場内を通過させて含有するシ
リカを多量体化し、 高周波磁場内を通過させた軟化水に、ボイラ水の酸消費
量(pH8.3)がシリカ含有量の少なくとも1.7倍
になるようにアルカリを添加して、 ボイラ補給水を得ることを特徴とする、ボイラ補給水の
処理方法。
2. Raw water is softened using an ion exchange agent, and the obtained softened water is passed through a high frequency magnetic field to polymerize silica contained therein. The softened water passed through the high frequency magnetic field is then converted into a boiler. A method for treating boiler make-up water, which comprises adding an alkali so that the acid consumption amount (pH 8.3) of water is at least 1.7 times the silica content to obtain boiler make-up water.
JP10926394A 1994-05-24 1994-05-24 Apparatus and method for treating boiler supply water Pending JPH07313993A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10926394A JPH07313993A (en) 1994-05-24 1994-05-24 Apparatus and method for treating boiler supply water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10926394A JPH07313993A (en) 1994-05-24 1994-05-24 Apparatus and method for treating boiler supply water

Publications (1)

Publication Number Publication Date
JPH07313993A true JPH07313993A (en) 1995-12-05

Family

ID=14505744

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10926394A Pending JPH07313993A (en) 1994-05-24 1994-05-24 Apparatus and method for treating boiler supply water

Country Status (1)

Country Link
JP (1) JPH07313993A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006192424A (en) * 2005-05-09 2006-07-27 Kansai Toshi Kyoju Service:Kk A method for treating silica-containing water and an open circulation type cooling water system using the treated water.
JP2007255838A (en) * 2006-03-24 2007-10-04 Kurita Water Ind Ltd Boiler equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006192424A (en) * 2005-05-09 2006-07-27 Kansai Toshi Kyoju Service:Kk A method for treating silica-containing water and an open circulation type cooling water system using the treated water.
JP2007255838A (en) * 2006-03-24 2007-10-04 Kurita Water Ind Ltd Boiler equipment

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