JPS58137492A - Method for removing color of water - Google Patents

Method for removing color of water

Info

Publication number
JPS58137492A
JPS58137492A JP1883882A JP1883882A JPS58137492A JP S58137492 A JPS58137492 A JP S58137492A JP 1883882 A JP1883882 A JP 1883882A JP 1883882 A JP1883882 A JP 1883882A JP S58137492 A JPS58137492 A JP S58137492A
Authority
JP
Japan
Prior art keywords
water
flocculant
filtering
filtering tube
agent
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
JP1883882A
Other languages
Japanese (ja)
Other versions
JPH0135714B2 (en
Inventor
Yuriko Hagimori
萩森 由利子
Kazumasa Kasakura
笠倉 和昌
Takahiko Saito
隆彦 斉藤
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.)
Suido Kiko Kaisha Ltd
Original Assignee
Suido Kiko Kaisha 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 Suido Kiko Kaisha Ltd filed Critical Suido Kiko Kaisha Ltd
Priority to JP1883882A priority Critical patent/JPS58137492A/en
Publication of JPS58137492A publication Critical patent/JPS58137492A/en
Publication of JPH0135714B2 publication Critical patent/JPH0135714B2/ja
Granted legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To efficiently remove the coloration of water and to remove dissolved iron, manganese, etc., by using the particles of electrolytic manganese dioxide as the catalyst to remove the color of naturally colored water derived from humic acid, fulvic acid, etc. CONSTITUTION:An ozone-reacting column 2 is provided in front of a filtering tube 1, a part 5 for injecting pressurized air, a part 6 for adding NaClO and a part 7 for adding a flocculant are provided in a line 4 leading to the filtering tube 1, and the filtering tube 1 is packed with a catalytic filtering agent (particles of electrolytic manganese dioxide) 8. If the load of the color of raw water is very high, the raw water is treated in the ozone-reacting column 2, mixed with 2ppm NaClO as an oxidizing agent and 5ppm poly(aluminum chloride) as a flocculant and then let flow through the catalytic filtering agent in the filtering tube 1. According to this method, the amount of chemical agents to be injected can be saved by about 1/100, and the amount of sludge is made small below 1/100 as compared with a conventional method using a flocculant.

Description

【発明の詳細な説明】 従来井戸水等におけるフミン酸、フルボ酸等による天然
色度の除去に当って、アルミニウム塩等の凝集剤の大量
添加によるI)H降下と凝集効禿と7より下処理ケして
きたが、膨大な量の汚(1) 泥の発生と、コスト増の欠点があり、天然着色水の色に
除去は水処理中の難題であった。
[Detailed Description of the Invention] Conventionally, in removing natural chromaticity due to humic acid, fulvic acid, etc. in well water, etc., I) H reduction and coagulation effect by adding a large amount of flocculant such as aluminum salt and pretreatment from 7. However, it has the disadvantage of generating a huge amount of dirt (1) and increasing cost, and removing the color of naturally colored water has been a challenge during water treatment.

この発明は深井戸水などに溶存する鉄、マンガン全除去
する際に、活性度のh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ケ酸化不溶物として
除去する操作に看目し、特にマンガン触媒として電解二
酸化マンガンが丁ぐtz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。
This invention is applicable to the operation of completely removing iron and manganese dissolved in deep well water, etc., by using highly active manganese oxide as a catalyst and in the presence of an oxidizing agent such as chlorine. Apparently, electrolytic manganese dioxide has a particularly high activity as a manganese catalyst, so we investigated the possibility of applying this to the removal of color in humic substances, and obtained the results. .

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Kが高くγタイプの
二酸化マンガンがらなりたち、結合水を含んで非常に活
性度の高「  9  ) い化合物である。
As is well known, the electrolytic manganese dioxide used in the method of this invention is produced by electrolyzing manganese sulfate or manganese chloride made from manganese ore, and is composed of γ-type manganese dioxide with high pure K and free of bound water. It is a highly active compound containing ``9''.

次にこの発明の方法ケ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。
Next, the method of this invention will be explained in comparison with a conventional method using manganese sand using naturally colored water.

装置としては添付図面に示すように沖過筒1を主体とす
るものであって、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沖過筒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。
As shown in the attached drawing, the equipment is mainly composed of the offshore tube 1, and if the chromaticity load is extremely high, ozone treatment may be performed, so the ozone treatment is carried out before the offshore tube 1. A reaction column 2 is provided, but this is not relevant to the practical data presented below.

原水タンク3から前記濾過筒1に至る糸路4内において
、加圧空気注入部5 、NaC10添加部6、凝集剤添
加部7が設けられ、前記濾過筒l内には接触触媒F剤8
が装填されている。
A pressurized air injection section 5, a NaC10 addition section 6, and a flocculant addition section 7 are provided in the thread path 4 leading from the raw water tank 3 to the filter tube 1, and a contact catalyst F agent 8 is provided in the filter tube 1.
is loaded.

上記濾過筒lの内径100脇、戸剤高1500 cmと
し、p剤として 電解二酸化マンガン   マンガン砂 有効径  0.4.3牌   059結均等係数   
1.40     1.60通水条件 S V= 21
/HhLV=3(1m/H5試水(原水用よフミン酸系
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。
The inner diameter of the above filter cylinder L is 100 mm, the door height is 1500 cm, electrolytic manganese dioxide is used as the p agent, manganese sand effective diameter is 0.4.3 tiles, and the coagulation uniformity coefficient is 059.
1.40 1.60 Water flow condition S V = 21
/HhLV=3 (1m/H5 test water (for raw water) Humic acid-based colored water contains a small amount of iron and manganese, but the amount is not large enough to affect the chromaticity.

先ず、原水に酸化剤として次亜塩素酸ソーダ2pprl
、凝水剤としてポリ塩化アルミニウム5ppmを添加す
る。
First, add 2 pprl of sodium hypochlorite to raw water as an oxidizing agent.
, 5 ppm of polyaluminum chloride is added as a coagulant.

こrL2電解二酸化マンガン触媒沖剤と在来のマンガン
砂P剤とで処理比較したものが表1及び表2である。な
お濾過水には残留塩素05〜1.0ψ〕存在するように
した。
Tables 1 and 2 compare the treatment of this rL2 electrolytic manganese dioxide catalyst agent and the conventional manganese sand P agent. Note that residual chlorine of 05 to 1.0 ψ was present in the filtered water.

(5) なお上記実施例では酸化剤として次曲塩素酸ソーダを用
いているが、酸化剤としてオゾンケ用いることにエリ、
トリハロメタン生成の懸念はなくなって有利となり、あ
るいは水中の溶存酸素増加全はかるために、加圧空気注
入を行う場合もある。
(5) In the above example, sodium chlorate was used as the oxidizing agent, but there are some problems with using ozone as the oxidizing agent.
In some cases, pressurized air injection is used to remove the concern about trihalomethane formation, which is advantageous, or to increase the amount of dissolved oxygen in the water.

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?従来の凝集剤と比較すると、薬注量にしてほぼ1/
100、したがって汚泥量も1/100以下、その他溶
存鉄、マンガンの除去効果も消熱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。
This invention is carried out as described above, but is this? Compared to conventional flocculants, the amount of chemical injection is approximately 1/1
100, therefore the amount of sludge is less than 1/100, and the removal effect of dissolved iron and manganese is also excellent despite being a result of heat quenching, making it an extremely effective method for treating naturally colored water.

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

添付図面はこの発明の方法全実施すべき装置の系統図で
ある。 (6) なお図において、 1   濾過筒 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    NaCノ0添加部 7   凝集剤添加部 8   接触触媒炉剤 である。 特許出願人 水道機工株式会社 (7) 551
The accompanying drawing is a system diagram of the apparatus in which the entire method of the invention is carried out. (6) In the figure, 1 filter cylinder 2 ozone reaction tower 3 raw water tank 4 system line 5 pressurized air introduction section 6 NaC-0 addition section 7 flocculant addition section 8 contact catalyst reactor. Patent applicant Suido Kiko Co., Ltd. (7) 551

Claims (1)

【特許請求の範囲】[Claims] 活性度の高いマンガン酸化物全触媒として水”′中の溶
存物等ケ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。
In a method for removing dissolved substances in water as a highly active manganese oxide total catalyst, electrolytic manganese dioxide particles are used as the manganese oxide, and humic acid and fulvic acid are used to remove the chromaticity of naturally colored water. A method for removing chromaticity of water, characterized by performing the following steps.
JP1883882A 1982-02-10 1982-02-10 Method for removing color of water Granted JPS58137492A (en)

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 true JPS58137492A (en) 1983-08-15
JPH0135714B2 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)

Cited By (6)

* Cited by examiner, † Cited by third party
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
KR20030042428A (en) * 2001-11-22 2003-05-28 오르가노 가부시키가이샤 Method for treating power plant heater drain water
CN105174565A (en) * 2015-10-13 2015-12-23 辽宁石油化工大学 Method for deeply treating acrylon wastewater
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

Cited By (7)

* Cited by examiner, † Cited by third party
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
KR20030042428A (en) * 2001-11-22 2003-05-28 오르가노 가부시키가이샤 Method for treating power plant heater drain water
CN105174565A (en) * 2015-10-13 2015-12-23 辽宁石油化工大学 Method for deeply treating acrylon wastewater
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

Also Published As

Publication number Publication date
JPH0135714B2 (en) 1989-07-26

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