JPS6023871B2 - How to remove arsenic in water - Google Patents
How to remove arsenic in waterInfo
- Publication number
- JPS6023871B2 JPS6023871B2 JP15565977A JP15565977A JPS6023871B2 JP S6023871 B2 JPS6023871 B2 JP S6023871B2 JP 15565977 A JP15565977 A JP 15565977A JP 15565977 A JP15565977 A JP 15565977A JP S6023871 B2 JPS6023871 B2 JP S6023871B2
- Authority
- JP
- Japan
- Prior art keywords
- arsenic
- water
- furnace
- iron
- iron catalyst
- 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
Links
Landscapes
- Removal Of Specific Substances (AREA)
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】
この発明は、水中に漆存するヒ素(批素)を除去するに
際し、鉄塩注入及び凝集沈殿操作を省略し、炉過処理に
よってその目的を達成させる方法を要旨とするものであ
る。[Detailed Description of the Invention] The gist of the present invention is a method for removing arsenic present in water by omitting iron salt injection and coagulation-sedimentation operations and achieving the objective by furnace overtreatment. It is something.
深井戸水、鋼鉱山が上流にある表流水などにはヒ素が含
まれていることがあるが、従来はその除去のために、ヒ
素含有量の2所音程度の鉄塩を硫酸バンドと共に注入し
て中性付近で凝集沈殿処理を行い、ヒ素を鉄フロックに
吸着させ、炉過操作を加えて除去処理を行なっていた。Deep well water, surface water from steel mines, etc. may contain arsenic, but conventionally, to remove it, iron salts with an arsenic content of about 20% are injected together with sulfuric acid. The arsenic was adsorbed onto the iron flocs by coagulation and sedimentation near neutrality, and then removed through a furnace filtration operation.
このため、凝集沈殿操作が煩わしいばかりでなく、ヒ素
を含有した多量の沈殿汚泥が生成され、その処理が大変
であり、かつ、沈殿装置の分だけ広い設置面積を必要と
するという欠点があった。この発明は、炉村粒子の表面
に、水酸化第二鉄を加熱処理して鉄触媒被膜を形成させ
、中性付近のpH値でヒ素含有の原水をこの炉材で炉過
し、前記鉄触媒被膜によってヒ素を吸着除去すると共に
ヒ素吸着によって除去能力が低下した炉材を再生させる
方法を提案するものである。For this reason, not only is the coagulation-sedimentation operation cumbersome, but also a large amount of settled sludge containing arsenic is produced, which is difficult to dispose of, and it also requires a large installation area for the settling equipment. . This invention heat-treats ferric hydroxide to form an iron catalyst coating on the surface of Romura particles, and filters raw water containing arsenic at a pH value near neutrality through this furnace material. This paper proposes a method of adsorbing and removing arsenic using a catalyst coating and regenerating furnace materials whose removal ability has decreased due to arsenic adsorption.
次にこの発明を実施例によって説明する。Next, the present invention will be explained with reference to examples.
先ず、炉過材の作成であるが、例えば炉過砂のような核
となる炉材粒子をえらび、ボーメ42度の塩化第二鉄溶
液中に浸潰し、よく混合して粒子に液を付着させてから
、更に、この液中にソーダ灰を粉末のま)散布してかく
浮浪合する。First, to create the furnace material, select the core material particles such as furnace sand, immerse them in a Baume 42 degree ferric chloride solution, mix well, and attach the liquid to the particles. After this, soda ash (in powder form) is further sprinkled into this liquid and allowed to float.
その際、炭酸ガスの発明があり、pH8に至らせて水酸
化第こ鉄を生成させ、炉村粒子にこの水酸化第二鉄を付
着させてから取り出し、300〜400℃で約1時間加
熱処理を行なえば、炉材粒子表面を鉄触媒被膜で被覆さ
れた炉過材ができる。これを内蓬約125仇の炉過槽内
に10比又の高さに充填して炉過層を形成するものであ
る。実施例 1
ある火山地帯の井戸水を10の/時揚水して試験したの
であるが、その水質は、原水水室 掛値
7.0総アルカリ度 9&餌
アンモニア性窒素 微量
鉄 0.3血
ヒ素 0.範風
であった。At that time, carbon dioxide gas was invented, and the pH was raised to 8 to produce ferric hydroxide, which was then attached to the Romura particles, taken out, and heated at 300 to 400°C for about 1 hour. By carrying out the treatment, a furnace material whose surface of the furnace material particles is coated with an iron catalyst film is produced. This is filled into a furnace tank with an internal capacity of about 125 m2 to a height of 10% to form a furnace bed. Example 1 Water from a well in a volcanic area was pumped 10 times per hour for testing, and the quality of the water was found to be
7.0 Total alkalinity 9 & feed ammonia nitrogen Trace iron 0.3 Blood arsenic 0. It was Hanfu.
この場合、原水中に溶存鉄がわずかながらも溶存するの
で、これも除去するため、処理水量とほゞ同量の空気を
コンブレッサで送り、電気操作を行なってから、200
のノ日の炉過速度で炉過を行った結果、次の水質の処理
水が得られた。In this case, there is a small amount of dissolved iron in the raw water, so in order to remove this as well, a compressor is used to send approximately the same amount of air as the amount of treated water, and after electrical operation,
As a result of furnace filtration at a furnace overspeed of 2 days, treated water with the following water quality was obtained.
処理水水室 pH値 7.3鉄
0.0敦風ヒ素 痕跡
であった。Treated water chamber pH value 7.3 iron
There was a trace of 0.0 Atsushi arsenic.
実施例 2
前記実施例1で使用した原水は徴量ながら鉄が藩存して
いるので、水例は水道水中にヒ素を0.6柳加えて試験
したが、ヒ素は除去されていた。Example 2 The raw water used in Example 1 contained some iron, so the water sample was tested by adding 0.6 liters of arsenic to the tap water, but the arsenic was removed.
原水 処理水pH 値 7.0
70総アルカリ度 43.0
43.1鉄 痕跡 痕跡ヒ 素
0.6ppm 不榛出そして、ヒ素吸着が
飽和に達した炉材は、1〜2%程度の苛性ソーダ溶液を
通過させ、吸着ヒ素を脱着再生させれば、繰り返し使用
することができる。Raw water Treated water pH value 7.0
70 Total alkalinity 43.0
43.1 Trace of iron Trace of arsenic
0.6 ppm The furnace material whose arsenic adsorption has reached saturation can be used repeatedly by passing a caustic soda solution of about 1 to 2% to desorb and regenerate the adsorbed arsenic.
この発明は上記のようにして実施できるから、広い面積
の平地が少し、狭溢な山地の施設において、特に有用で
ある。Since the present invention can be carried out as described above, it is particularly useful in facilities located in mountainous areas, where a large area of flat land is limited to a small area.
Claims (1)
水酸化第二鉄被膜を加熱処理して鉄触媒被膜が形成され
た濾過材とし、この濾過材による濾暦によつて、ほゞ中
性領域でヒ素含有水を濾過し、水中のヒ素を前記鉄触媒
被膜で吸着除去すると共に、鉄触媒被膜にヒ素を吸着す
ることによつてヒ素除去能力が低下した濾材に対しアル
カリ溶液でヒ素を脱着し、濾材を再生させることを特徴
とする水中のヒ素を除去する方法。1. A ferric hydroxide film is formed on the surface of the filter medium particles, and this ferric hydroxide film is heat-treated to obtain a filter medium with an iron catalyst film formed thereon. Arsenic-containing water is filtered in a neutral region, and the arsenic in the water is adsorbed and removed by the iron catalyst coating, and arsenic is removed using an alkaline solution for filter media whose arsenic removal ability has decreased due to the adsorption of arsenic to the iron catalyst coating. A method for removing arsenic in water, which is characterized by desorbing arsenic and regenerating a filter medium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15565977A JPS6023871B2 (en) | 1977-12-26 | 1977-12-26 | How to remove arsenic in water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15565977A JPS6023871B2 (en) | 1977-12-26 | 1977-12-26 | How to remove arsenic in water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5499349A JPS5499349A (en) | 1979-08-06 |
JPS6023871B2 true JPS6023871B2 (en) | 1985-06-10 |
Family
ID=15610787
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15565977A Expired JPS6023871B2 (en) | 1977-12-26 | 1977-12-26 | How to remove arsenic in water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6023871B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4652380A (en) * | 1985-07-05 | 1987-03-24 | Stauffer Chemical Company | Method of treating the arsenic containing filter media from phosphoric acid purification |
CN1292990C (en) * | 2004-11-25 | 2007-01-03 | 上海自来水市北科技有限公司 | Prepn and application of iron-coating aluminium sand capable of eliminating organic matter from water |
JP4527584B2 (en) * | 2005-03-30 | 2010-08-18 | 株式会社神戸製鋼所 | Preparation of arsenic remover in contaminated water |
-
1977
- 1977-12-26 JP JP15565977A patent/JPS6023871B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5499349A (en) | 1979-08-06 |
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