JPH0135714B2 - - Google Patents
Info
- Publication number
- JPH0135714B2 JPH0135714B2 JP1883882A JP1883882A JPH0135714B2 JP H0135714 B2 JPH0135714 B2 JP H0135714B2 JP 1883882 A JP1883882 A JP 1883882A JP 1883882 A JP1883882 A JP 1883882A JP H0135714 B2 JPH0135714 B2 JP H0135714B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- manganese
- agent
- chromaticity
- 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
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
従来井戸水等におけるフミン酸、フルボ酸等に
よる天然色素の除去に当つて、アルミニウム塩等
の凝集剤の大量添加によるPH降下と凝集効果とに
よつて処理をしてきたが、膨大な量の汚泥の発生
と、コスト増の欠点があり、天然着色水の色度除
去は水処理中の難題であつた。
この発明は深井戸水などに溶存する鉄、マンガ
ンを除去する際に、活性度の高いマンガン酸化物
を触媒として塩素等の酸化剤の存在のもとにこれ
らを酸化不溶物として除去する操作に着目し、特
にマンガン触媒として電解二酸化マンガンがすぐ
れた活性度を有しているので、これがフミン質系
の色度除去に応用の可能性を検討し、その成果を
得たものである。
この発明の方法に使用する電解二酸化マンガン
は、周知のようにマンガン鉱から製する硫酸マン
ガン又は塩化マンガンを電解して製造したもので
純度が高くγタイプの二酸化マンガンからなりた
ち、結合水を含んで非常に活性度の高い化合物で
ある。
次にこの発明の方法を天然着色水において在来
のマンガン砂による方法と比較して説明する。
装置としては添付図面に示すような過筒1を
主体とするものであつて、色度の負荷が非常に高
い場合はオゾン処理を行うこともあるので過筒
1の前に一応、オゾン反応塔2が設けられている
が、これは以下に示す実施データには関係はな
い。
原水タンク3から前記過筒1に至る系路4内
において、加圧空気注入部5、NaClO添加部6、
凝集剤添加部7が設けられ、前記過筒1内には
接触触媒剤8が装填されている。
上記過筒1の内径100mm、剤高1500cmとし、
剤として
電解二酸化マンガン マンガン砂
有効径 0.43mm 0.59mm
均等係数 1.40 1.60
通水条件 SV=2l/Hh LV=30m/Hh
試水(原水)はフミン酸系着色水で鉄、マンガ
ンを僅かに含有しているが、色度として影響する
程の量ではない。
先ず、原水に酸化剤として次亜塩素酸ソーダ
2ppm、凝水剤としてポリ塩化アルミニウム5ppm
を添加する。
これを電解二酸化マンガン触媒剤と在来のマ
ンガン砂剤とで処理比較したものが表1及び表
2である。なお過水には残留塩素0.5〜1.0mg/
存在するようにした。
Conventionally, natural pigments such as humic acid and fulvic acid in well water have been removed by adding large amounts of flocculants such as aluminum salts to lower the pH and have a flocculating effect. Removal of color from naturally colored water has been a challenge during water treatment due to the drawbacks of color generation and increased cost. This invention focuses on an operation in which iron and manganese dissolved in deep well water are removed as oxidized insoluble substances in the presence of an oxidizing agent such as chlorine using highly active manganese oxide as a catalyst. However, since electrolytic manganese dioxide has particularly excellent activity as a manganese catalyst, we investigated the possibility of applying this to the removal of color in humic substances, and the results were obtained. As is well known, the electrolytic manganese dioxide used in the method of this invention is produced by electrolyzing manganese sulfate or manganese chloride produced from manganese ore, and is made of highly pure γ-type manganese dioxide and does not contain bound water. It is a highly active compound. Next, the method of this invention will be explained in comparison with a conventional method using manganese sand in naturally colored water. The apparatus is mainly composed of a overcoat 1 as shown in the attached drawing, and if the chromaticity load is very high, ozone treatment may be performed, so an ozone reaction tower is installed before the overcoat 1. 2 is provided, but this is not relevant to the implementation data presented below. In the system 4 leading from the raw water tank 3 to the overtube 1, a pressurized air injection section 5, a NaClO addition section 6,
A coagulant adding section 7 is provided, and a contact catalyst agent 8 is loaded into the overtube 1 . The inner diameter of the above tube 1 is 100 mm, the agent height is 1500 cm,
As agent Electrolytic manganese dioxide Manganese sand Effective diameter 0.43mm 0.59mm Uniformity factor 1.40 1.60 Water flow conditions SV = 2l/Hh LV = 30m/Hh The test water (raw water) is humic acid colored water and contains a small amount of iron and manganese. However, the amount is not large enough to affect the chromaticity. First, add sodium hypochlorite to raw water as an oxidizing agent.
2ppm, polyaluminum chloride 5ppm as a coagulant
Add. Tables 1 and 2 compare the treatments using an electrolytic manganese dioxide catalyst agent and a conventional manganese sand agent. In addition, residual chlorine is 0.5 to 1.0 mg/
Made it exist.
【表】【table】
【表】
なお上記実施例では酸化剤として次亜塩素酸ソ
ーダを用いているが、酸化剤としてオゾンを用い
ることにより、トリハロメタン生成の懸念はなく
なつて有利となり、あるいは水中の溶存酸素増加
をはかるために、加圧空気注入を行う場合もあ
る。
この発明は上記のようにして実施するものであ
るが、これを従来の凝集剤と比較すると、薬注量
にしてほぼ1/100、したがつて汚泥量も1/100以
下、その他溶存鉄、マンガンの除去効果も当然の
結果ながらすぐれており、天然着色水の処理方法
として極めて有効なものである。[Table] In the above example, sodium hypochlorite is used as the oxidizing agent, but by using ozone as the oxidizing agent, there is no concern about trihalomethane formation, which is advantageous, or it is possible to increase dissolved oxygen in water. For this purpose, pressurized air injection may be performed. This invention is implemented as described above, but when compared with conventional flocculants, the amount of chemical injection is approximately 1/100, the amount of sludge is also less than 1/100, and the amount of dissolved iron, etc. As a matter of course, the effect of removing manganese is also excellent, making it an extremely effective method for treating naturally colored water.
添付図面はこの発明の方法を実施すべき装置の
系統図である。
なお図において、1……過筒、2……オゾン
反応塔、3……原水タンク、4……系路、5……
加圧空気導入部、6……NaClO添加部、7……
凝集剤添加部、8……接触触媒剤である。
The accompanying drawing is a system diagram of an apparatus for carrying out the method of the invention. In the figure, 1...transfer cylinder, 2...ozone reaction tower, 3...raw water tank, 4...system line, 5...
Pressurized air introduction part, 6...NaClO addition part, 7...
Flocculant addition part, 8... contact catalyst agent.
Claims (1)
中の溶存物等を除去する方法において、前記マン
ガン酸化物として電解二酸化マンガン粒子を使用
し、フミン酸、フルボ酸による天然着色水の色度
除去を行うことを特徴とする水の色度除去方法。1. In a method for removing dissolved substances in water using highly active manganese oxide as a catalyst, electrolytic manganese dioxide particles are used as the manganese oxide, and the chromaticity of naturally colored water is removed using humic acid and fulvic acid. A method for removing chromaticity of water, which is characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1883882A JPS58137492A (en) | 1982-02-10 | 1982-02-10 | Method for removing color of water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1883882A JPS58137492A (en) | 1982-02-10 | 1982-02-10 | Method for removing color of water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58137492A JPS58137492A (en) | 1983-08-15 |
| JPH0135714B2 true JPH0135714B2 (en) | 1989-07-26 |
Family
ID=11982694
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1883882A Granted JPS58137492A (en) | 1982-02-10 | 1982-02-10 | Method for removing color of water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58137492A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60190290A (en) * | 1984-03-13 | 1985-09-27 | Mitsui Mining & Smelting Co Ltd | Treatment of organic waste water |
| JPS6490092A (en) * | 1987-09-30 | 1989-04-05 | Suido Kiko Kk | Method for removing trihalomethane precursor in water |
| JPH0199689A (en) * | 1987-10-09 | 1989-04-18 | Suido Kiko Kk | Method for removing organic matter in water |
| US6810100B2 (en) * | 2001-11-22 | 2004-10-26 | Organo Corporation | Method for treating power plant heater drain water |
| CN105174565B (en) * | 2015-10-13 | 2018-05-15 | 辽宁石油化工大学 | Acrylic fiber wastewater deep treatment method |
| WO2024070733A1 (en) * | 2022-09-27 | 2024-04-04 | パナソニックIpマネジメント株式会社 | Water purification device |
-
1982
- 1982-02-10 JP JP1883882A patent/JPS58137492A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58137492A (en) | 1983-08-15 |
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