JPS627489A - Method for treating waste water of protein foam fire extinguishing solution - Google Patents
Method for treating waste water of protein foam fire extinguishing solutionInfo
- Publication number
- JPS627489A JPS627489A JP14668485A JP14668485A JPS627489A JP S627489 A JPS627489 A JP S627489A JP 14668485 A JP14668485 A JP 14668485A JP 14668485 A JP14668485 A JP 14668485A JP S627489 A JPS627489 A JP S627489A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- filtrate
- added
- fire extinguishing
- foam fire
- 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
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Removal Of Specific Substances (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は蛋白泡消火液の廃水処理方法に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) This invention relates to a method for treating wastewater using protein foam fire extinguishing liquid.
(従来の技術)
危険物施設としての屋外タンクや、石油プラント等に付
設される固定式泡消火設備には、タンパク泡消火薬剤が
使用されており、火災の際、この消火剤は消火設備によ
って水と混合され、史に空気と混合され泡となって放出
される。(Prior art) Protein foam fire extinguishing agents are used in outdoor tanks as hazardous materials facilities and fixed foam fire extinguishing equipment attached to petroleum plants, etc. In the event of a fire, this extinguishing agent is used by the fire extinguishing equipment. It is mixed with water and then mixed with air and released as bubbles.
従来こうした泡消火設備については、薬液放出試鹸にお
いて、泡消火液に代えて水を放出していた。そのため火
災時以外は、泡消火液が放出されることがないので、特
に泡消火液の廃水処理を考慮する必要がなく、その処理
方法についても開発がなされていない。Conventionally, such foam fire extinguishing equipment has discharged water instead of foam extinguishing liquid in the chemical discharge test soap. Therefore, since the foam fire extinguishing fluid is not released except in the event of a fire, there is no need to particularly consider wastewater treatment of the foam fire extinguishing fluid, and no development has been made on the treatment method.
(発明が解決しようとする問題点)
最近になって、固定式泡消火設備は、作動機能試験と併
せて、発泡性能試験が毎年1回課せられ、この発泡性能
試験の際、多量の泡栗剤水溶液が排出される。この廃水
を河川に放流する場合、河川を汚染する為公害問題とな
りている。(Problem to be solved by the invention) Recently, fixed foam fire extinguishing equipment is required to undergo a foaming performance test once a year in addition to an operational function test. The aqueous solution is discharged. When this wastewater is discharged into rivers, it becomes a pollution problem because it pollutes the rivers.
(間過を解決する几めめ手段)
この発明はこうした問題点を解決するために、新しく開
発したもので、すなわち、蛋白泡消火剤を含有する液に
、高分子凝集剤、ポリ塩化アルミニウム、及び水酸化ナ
トリウムを加え、凝集沈澱及び濾過し、その濾液に過酸
化水素と、硫醒第1鉄を加え、酸化処理し、濾過し、更
にその濾液に活性炭を加え吸着処理し濾過して、COD
値を下げること1c特徴とする蛋白泡消火液の廃水処理
方法である。(Measures to solve the problem) This invention was newly developed to solve these problems. Namely, a solution containing a protein foam extinguishing agent, a polymer flocculant, polyaluminum chloride, and sodium hydroxide, coagulated and precipitated and filtered, hydrogen peroxide and sulfurized ferrous iron added to the filtrate, oxidized and filtered, activated carbon added to the filtrate for adsorption treatment and filtered, COD
This is a method for treating wastewater using protein foam fire extinguishing fluid, which is characterized by reducing the value of fire extinguishing fluid.
(実施例)
この処理方法について、A社製蛋白泡(5−型)を処理
した例を挙ける。(Example) Regarding this treatment method, an example will be given in which protein foam manufactured by Company A (5-type) was treated.
試料液COD 6000PPMに、ポリ塩化アルミニウ
ム2%を加え攪拌し、さらに水酸化ナトリウム1俤を添
加し、PR&Qにした後、高分子凝集剤を101s添加
し、生成した70、り全階5Aの濾紙で窄過する。次に
過酸化水素水8%添加処即し、その処理液に活性炭(5
0% Wet粉)2チ加え攪拌する。その結果COD値
は+40PPMKなった。Add 2% polyaluminum chloride to sample solution COD 6000PPM, stir, add 1 ton of sodium hydroxide to make PR&Q, add polymer flocculant for 101s, and create 70ml filter paper on all floors 5A. It narrows down. Next, 8% hydrogen peroxide solution was added to the treated solution, and activated carbon (5%
Add 2 g (0% wet powder) and stir. As a result, the COD value was +40 PPMK.
これ以外に考えられる廃水処理方法として、例えば次の
処理方法を比較1c挙げる。As a possible wastewater treatment method other than this, for example, the following treatment method is listed as Comparison 1c.
試料液(同様COD 6000PPM )にポリ塩化ア
ルミニウム5慢を加え、水酸化ナトリウムを加えてPB
&0にし、随5Aの濾紙にて嘘過し、次にイオン交換樹
脂(−I R+20BNa型)によって処理する。この
例でtjcODは2100となった。Add polyaluminum chloride to the sample solution (also COD 6000PPM), add sodium hydroxide, and make PB.
&0, passed through a 5A filter paper, and then treated with an ion exchange resin (-IR+20BNa type). In this example, tjcOD was 2100.
以上のようにこの発明による処理方法では、COD値は
大きく下げることができる。As described above, with the processing method according to the present invention, the COD value can be greatly reduced.
この発明の処理方法を実際の処理装置によって実施する
例を説明すると、図において、蛋白泡消火剤を含有する
廃水を、ポンプ1にて処理槽2へ送り、攪拌機3で攪拌
しながら、ポリ塩化アルミニウム槽4よりポリ塩化アル
ミニウムを添加する。次に水酸化ナトリウム槽5より水
酸化ナトリウムを添加し、PHf60位に1t144I
すると、フコツクが発生する。To explain an example in which the treatment method of the present invention is implemented using an actual treatment device, as shown in the figure, wastewater containing a protein foam fire extinguisher is sent to a treatment tank 2 with a pump 1, and while being stirred with a stirrer 3, polychloride Add polyaluminum chloride from aluminum tank 4. Next, add sodium hydroxide from the sodium hydroxide tank 5, and add 1t144I to pHf 60.
Then, a fukotsuk occurs.
このフロック中に廃水中の発泡成分が凝集されている。Foaming components in wastewater are aggregated in this floc.
さらに攪拌を続けながら、高分子凝集剤槽6から高分子
凝集剤を添加する。この高分子凝集剤によって、フロッ
クは大盤化し清適可能な状態となる。Further, while continuing stirring, a polymer flocculant is added from the polymer flocculant tank 6. This polymer flocculant makes the flocs large and ready for cleaning.
次に70ツクを、スラリーポンプ8にて流量計9で流量
を測定しながら、遠心分離機10に送る。そしてこの遠
心分離機10に入ったスラリーを、1液とスラッジに分
離する。スラッジはスラッジ受槽11にて回収する。一
方遠心分離機10によって分離した濾液は、酸化槽15
に送り、攪拌機14で攪拌しながら過酸化水素槽15、
及び硫酸第1鉄注入槽16より過酸化水素水、及び@L
酸第1鉄fI:添加し反応させる。Next, 70 pieces are sent to a centrifuge 10 using a slurry pump 8 while measuring the flow rate with a flow meter 9. The slurry entering the centrifugal separator 10 is separated into a liquid and sludge. Sludge is collected in a sludge receiving tank 11. On the other hand, the filtrate separated by the centrifuge 10 is transferred to an oxidation tank 15.
and hydrogen peroxide tank 15 while stirring with a stirrer 14.
and hydrogen peroxide solution from the ferrous sulfate injection tank 16, and @L
Ferrous acid fI: Add and react.
この反応は7エントン酸化と一般に呼び、濾液を強力に
酸化し、COD成分を減少する。This reaction, commonly called 7-entone oxidation, strongly oxidizes the filtrate and reduces COD components.
次に7エントン酸化により着色した1液を炭酸カルシウ
ム4917より炭酸カリシクムを添加し7脱色する。Next, the first solution colored by 7-enton oxidation is decolorized by adding calicicum carbonate from calcium carbonate 4917.
脱色後の処理液は杏度スラリーボング8にて遠心+ms
+oへ送り、遠心分離機10によって過酸化水素処理滴
液と、スラッジに分離する。スラ、ジはスラジ受槽11
1C回収する。また過酸化水素処理濾液は、処理槽2に
送り、攪拌機5にて攪拌しながら活性炭槽7より活性炭
を添加する。このよりに各工程においてCOD成分を吸
着されながら、処理液は再びスラリーポンプ8にて遠心
分離機10に送り、処理滴液と活性炭に分離される。そ
して活性炭は活性炭受槽12にて回収する。そして処理
濾液は規定の廃水処理基準を満たす。After decolorization, the treatment solution is centrifuged in an apricot slurry bong 8 for +ms.
+o, and separated into hydrogen peroxide treated droplets and sludge by a centrifuge 10. Sludge, ji is sludge receiving tank 11
Collect 1C. Further, the hydrogen peroxide treated filtrate is sent to the treatment tank 2, and activated carbon is added from the activated carbon tank 7 while stirring with the stirrer 5. As a result, while the COD components are adsorbed in each step, the treated liquid is again sent to the centrifugal separator 10 by the slurry pump 8, where it is separated into treated droplets and activated carbon. The activated carbon is then collected in an activated carbon receiving tank 12. The treated filtrate then meets prescribed wastewater treatment standards.
(発明の効果)
この発明による蛋白泡消火液の廃水処理方法によれば、
C0D一度の高い汚水を、特別な処理装置を使わずに処
理でき、C0D一度を大巾に下けることができ、安全か
つ優れた方法である。(Effects of the Invention) According to the method for treating wastewater using protein foam fire extinguishing liquid according to the present invention,
It is a safe and excellent method that can treat wastewater with a high COD value without using special treatment equipment, and can significantly lower the COD value.
図にこの発明の方法を実施するための処理装置の系統図
である。
1.8 ・・・ポンプ、2・・・処理槽。
4・・・ポリ塩化アルミニウム槽、5・・・水酸化ナト
リウム権、6・・・高分子凝集槽、7・・・活性炭槽、
10・・・遠心分離機、11・・・スラッジ受槽。1 is a system diagram of a processing device for carrying out the method of the present invention. 1.8...pump, 2...processing tank. 4... Polyaluminum chloride tank, 5... Sodium hydroxide tank, 6... Polymer coagulation tank, 7... Activated carbon tank,
10... Centrifugal separator, 11... Sludge receiving tank.
Claims (1)
え、凝集沈澱及び濾過し、その濾液に過酸化水素と、硫
酸第1鉄を加え酸化処理し濾過し、更にその濾液に活性
炭を加え吸着処理し、濾過し、COD値を下げることを
特徴とする蛋白泡消火液の廃水処理方法。[Claims] A polymer flocculant, polyaluminum chloride, and sodium hydroxide are added to a liquid containing a protein fire extinguishing foam, and the mixture is coagulated and precipitated and filtered, and hydrogen peroxide and ferrous sulfate are added to the filtrate. A method for treating wastewater using protein foam fire extinguishing fluid, which comprises adding activated carbon to the filtrate, performing adsorption treatment, and filtering to lower the COD value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14668485A JPS627489A (en) | 1985-07-05 | 1985-07-05 | Method for treating waste water of protein foam fire extinguishing solution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14668485A JPS627489A (en) | 1985-07-05 | 1985-07-05 | Method for treating waste water of protein foam fire extinguishing solution |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS627489A true JPS627489A (en) | 1987-01-14 |
Family
ID=15413245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14668485A Pending JPS627489A (en) | 1985-07-05 | 1985-07-05 | Method for treating waste water of protein foam fire extinguishing solution |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS627489A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0519682A (en) * | 1991-07-11 | 1993-01-29 | Ebara Infilco Co Ltd | Educational material and educational kit for water treatment |
US6808481B1 (en) | 1996-10-15 | 2004-10-26 | Erth Technologies, Inc. | Concentric tubular centrifuge |
US6966874B2 (en) | 1997-10-14 | 2005-11-22 | Erth Technologies, Inc. | Concentric tubular centrifuge |
GB2418373A (en) * | 2004-12-07 | 2006-03-29 | Abc Macintosh Ltd | Method and apparatus for processing waste fluorinated products |
US7241256B2 (en) | 2003-08-30 | 2007-07-10 | Erth Technologies, Inc. | Centrifuge |
JP2016022407A (en) * | 2014-07-17 | 2016-02-08 | 日本ドライケミカル株式会社 | Waste disposal system for fire-extinction liquid emitted from foam fire-extinguishment equipment |
-
1985
- 1985-07-05 JP JP14668485A patent/JPS627489A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0519682A (en) * | 1991-07-11 | 1993-01-29 | Ebara Infilco Co Ltd | Educational material and educational kit for water treatment |
US6808481B1 (en) | 1996-10-15 | 2004-10-26 | Erth Technologies, Inc. | Concentric tubular centrifuge |
US6966874B2 (en) | 1997-10-14 | 2005-11-22 | Erth Technologies, Inc. | Concentric tubular centrifuge |
US7189196B2 (en) | 1997-10-14 | 2007-03-13 | Erth Technologies, Inc. | Method of separating materials with a concentric tubular centrifuge |
US7241256B2 (en) | 2003-08-30 | 2007-07-10 | Erth Technologies, Inc. | Centrifuge |
GB2418373A (en) * | 2004-12-07 | 2006-03-29 | Abc Macintosh Ltd | Method and apparatus for processing waste fluorinated products |
WO2006061408A1 (en) * | 2004-12-07 | 2006-06-15 | Abc Macintosh Ltd | Method of processing waste products |
JP2016022407A (en) * | 2014-07-17 | 2016-02-08 | 日本ドライケミカル株式会社 | Waste disposal system for fire-extinction liquid emitted from foam fire-extinguishment equipment |
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