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JP3517697B2 - Method and remover for removing heavy metal ions - Google Patents
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JP3517697B2 - Method and remover for removing heavy metal ions - Google Patents

Method and remover for removing heavy metal ions

Info

Publication number
JP3517697B2
JP3517697B2 JP12771599A JP12771599A JP3517697B2 JP 3517697 B2 JP3517697 B2 JP 3517697B2 JP 12771599 A JP12771599 A JP 12771599A JP 12771599 A JP12771599 A JP 12771599A JP 3517697 B2 JP3517697 B2 JP 3517697B2
Authority
JP
Japan
Prior art keywords
heavy metal
water
removing agent
metal ions
dissolved
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 - Lifetime
Application number
JP12771599A
Other languages
Japanese (ja)
Other versions
JP2000317469A (en
Inventor
憲司 辰巳
慎二 和田
恭啓 湯川
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.)
Mitsubishi Corp
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Mitsubishi Corp
National Institute of Advanced Industrial Science and Technology AIST
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 Mitsubishi Corp, National Institute of Advanced Industrial Science and Technology AIST filed Critical Mitsubishi Corp
Priority to JP12771599A priority Critical patent/JP3517697B2/en
Publication of JP2000317469A publication Critical patent/JP2000317469A/en
Application granted granted Critical
Publication of JP3517697B2 publication Critical patent/JP3517697B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Removal Of Specific Substances (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、水中に溶存重金属
イオンを除去するための方法及び除去剤に関するもので
ある。
TECHNICAL FIELD The present invention relates to a method and a removing agent for removing dissolved heavy metal ions in water.

【0002】[0002]

【従来の技術】従来から、水中に含まれる溶存重金属イ
オンの除去方法としては、水中に水酸化ナトリウムや水
酸化カルシウム等のアルカリ性物質を添加して、水酸化
物として沈殿させる方法が知られている。このような方
法において、アルカリ性物質として水酸化ナトリウムを
使用するときには、生成するスラッジ(重金属水酸化
物)の発生量は少ないものの、そのスラッジ粒子が小さ
く分離しにくいという欠点がある。従って、これまで
は、水酸化カルシウムがもっぱら使用されてきたが、こ
の場合には、スラッジ発生量が多いという欠点がある。
2. Description of the Related Art Conventionally, as a method for removing dissolved heavy metal ions contained in water, a method of adding an alkaline substance such as sodium hydroxide or calcium hydroxide to water and precipitating it as a hydroxide is known. There is. In such a method, when sodium hydroxide is used as the alkaline substance, the amount of sludge (heavy metal hydroxide) generated is small, but the sludge particles are small and difficult to separate. Therefore, until now, calcium hydroxide has been exclusively used, but in this case, there is a drawback that a large amount of sludge is generated.

【0003】[0003]

【発明が解決しようとする課題】本発明は、水中に含ま
れる溶存重金属イオンを効率よくかつ低められたスラッ
ジ発生量で除去するための方法及びそれに用いる重金属
イオン除去剤を提供することをその課題とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for efficiently removing dissolved heavy metal ions contained in water with a reduced sludge generation amount, and a heavy metal ion removing agent used therefor. And

【0004】[0004]

【課題を解決するための手段】本発明者らは、前記課題
を解決すべく鋭意研究を重ねた結果、本発明を完成する
に至った。即ち、本発明によれば、水中に含まれる重金
属イオンを除去する方法において、該水中に、アニオン
基含有親水性高分子物質と水酸化ナトリウムとの混合物
からなる粉末状又は該高分子物質を非溶解状で含む水性
液状の重金属イオン除去剤を投入し、該除去剤中の該高
分子物質を水中に溶解させることなく分散させることに
より、該水中に含まれる溶存重金属イオンを不溶化させ
ることを特徴とする重金属イオンの除去方法が提供され
る。また、本発明によれば、水中に含まれる溶存重金属
イオンを除去するための除去剤であって、アニオン基含
有親水性高分子物質と水酸化ナトリウムとの混合物から
り、粉末状又は該高分子物質を非溶解状で含む水性液
状であり、かつ該除去剤を水中に投入した場合に該高分
子物質は不溶性の状態で存在するものであることを特徴
とする重金属イオンの除去剤が提供される。
The present inventors have completed the present invention as a result of intensive studies to solve the above problems. That is, according to the present invention, in a method for removing heavy metal ions contained in water, in the aqueous, powder powder-like or polymeric material ing of a mixture of anionic group-containing hydrophilic polymeric substance with sodium hydroxide A non-dissolved aqueous liquid heavy metal ion removing agent is added, and
Provided is a method for removing heavy metal ions, which comprises insolubilizing a dissolved heavy metal ion contained in water by dispersing a molecular substance in water without dissolving it. Further, according to the present invention, there is provided a removing agent for removing dissolved heavy metal ions contained in the water, Ri Na <br/> a mixture of anionic group-containing hydrophilic polymeric substance with sodium hydroxide, powder Liquid containing a polymer or the polymer substance in a non-dissolved form
If the removing agent is put in water,
Child material removing agent of heavy metal ions, characterized in der Rukoto those existing in the state of insoluble is provided.

【0005】[0005]

【発明の実施の形態】本発明の重金属イオン除去剤(以
下、単に除去剤とも言う)は、アニオン基含有親水性高
分子物質と水酸化ナトリウムと必要に応じての無害性多
価金属化合物との混合物からなるものである。アニオン
基含有親水性高分子物質には、カルボキシル基、スルホ
ン酸基、リン酸基等のアニオン基を含有する各種の高分
子物質が包含され、天産品及び合成品のいずれも使用で
きるが、環境保全の点からは生分解性を有するものの使
用が好ましい。このような高分子物質としては、アルギ
ン酸、ジエランガム、キサンタンガム、トラガカントガ
ム、ペクチン、ペクチン酸、ペクチニン酸、カラギーナ
ン、ゼラチン、寒天、アニオン化でんぷん、アルギン酸
プロピレングリコールエステル、カルボキシメチルセル
ロース、デンプングリコール酸、繊維素グリコール酸、
デンプンリン酸、ガラクトマンナン等の多糖類及びそれ
らのアルカリ金属塩;ポリアクリル酸、アクリルアミド
とアクリル酸との共重合体及びその金属塩;高吸水性高
分子(例えば、住友化学社製、「スミカゲル」、三洋化
成社製、「サンウェット」、昭和電工社製、「プレアプ
ル」、日澱化学社製、「WAS」等)等が挙げられる。
前記アニオン基含有親水性高分子物質として、(i)ア
ルギン酸もしくはその塩又は(ii)アルギン酸もしくは
その塩と他のアニオン基含有親水性高分子物質との混合
物や、(i)ペクチン、ペクチン酸もしくはそれらの塩
又は(ii)ペクチン、ペクチン酸もしくはそれらの塩と
他のアニオン基含有親水性高分子物質との混合物、及び
(i)ポリアクリル酸、アクリルアミドとアクリル酸と
の共重合体もしくはその塩又は(ii)ポリアクリル酸、
アクリルアミドとアクリル酸との共重合体もしくはその
塩と他のアニオン基含有親水性高分子物質との混合物が
挙げられる。
BEST MODE FOR CARRYING OUT THE INVENTION The heavy metal ion removing agent of the present invention (hereinafter, also simply referred to as a removing agent) is an anionic group-containing hydrophilic polymer substance, sodium hydroxide and, if necessary, a harmless polyvalent metal compound. It is composed of a mixture of The anion group-containing hydrophilic polymer substance includes various polymer substances containing anion groups such as a carboxyl group, a sulfonic acid group and a phosphoric acid group, and both natural products and synthetic products can be used. From the viewpoint of conservation, it is preferable to use those having biodegradability. Such high molecular substances include alginic acid, dielan gum, xanthan gum, tragacanth gum, pectin, pectic acid, pectinic acid, carrageenan, gelatin, agar, anionized starch, propylene glycol alginate, carboxymethyl cellulose, starch glycolic acid, fibrin glycol. acid,
Polysaccharides such as starch phosphate and galactomannan and alkali metal salts thereof; polyacrylic acid, copolymers of acrylamide and acrylic acid and metal salts thereof; super absorbent polymers (for example, Sumika Gel manufactured by Sumitomo Chemical Co., Ltd. , Sanyo Kasei Co., Ltd., “Sunwet”, Showa Denko KK, “Pre-Apple”, Nisseki Kagaku KK, “WAS”, etc.) and the like.
Examples of the anionic group-containing hydrophilic polymer substance include (i)
Ruginic acid or its salt or (ii) alginic acid or
Mixing the salt with other hydrophilic polymer containing anion groups
Thing, (i) pectin, pectic acid or their salts
Or (ii) with pectin, pectic acid or salts thereof
Mixture with other anionic group-containing hydrophilic polymer, and
(I) Polyacrylic acid, acrylamide and acrylic acid
Or a salt thereof or (ii) polyacrylic acid,
Copolymer of acrylamide and acrylic acid or its
A mixture of salt and other hydrophilic polymer containing anionic groups
Can be mentioned.

【0006】本発明では、特に、アルギン酸ナトリウム
やアルギン酸カルシウムの使用が好ましいが、このもの
を用いる場合には、アルギン酸を構成しているマンヌマ
ロン酸(M)とグルロン酸(G)の含有比率(モル比)
[M]/[G]が、0.1〜4.0、好ましくは0.1
〜3の範囲にあるものの使用が好ましい。グルロン酸の
含有比率が多いもの程、フロック形成性にすぐれてい
る。これらのアニオン基含有親水性高分子物質は、通
常、粉末状(短繊維状を含む)で用いられ、その平均粒
径は、10〜500μm、好ましくは20〜200μ
m、より好ましくは50〜150μmである。
In the present invention, it is particularly preferable to use sodium alginate or calcium alginate. When this is used, the content ratio of mannumamaronic acid (M) and guluronic acid (G) constituting alginic acid (mol ratio)
[M] / [G] is 0.1 to 4.0, preferably 0.1.
It is preferable to use those in the range of 3 to 3. The higher the content ratio of guluronic acid, the better the floc forming property. These anionic group-containing hydrophilic polymer substances are usually used in powder form (including short fiber form), and the average particle size thereof is 10 to 500 μm, preferably 20 to 200 μm.
m, more preferably 50 to 150 μm.

【0007】本発明において除去剤成分として用いる前
記アニオン基含有親水性高分子物質は、単独又は混合物
の形態で用いることができる。
The anionic group-containing hydrophilic polymer substance used as the remover component in the present invention can be used alone or in the form of a mixture.

【0008】本発明の除去剤は、水酸化ナトリウムを含
有する。この水酸化ナトリウムは、アニオン基含有親水
性高分子物質に対して、その高分子物質の溶解性をコン
トロールする等の作用を示す。水酸化ナトリウムの使用
割合は特に制約されず、水中に溶解する重金属イオンの
種類や量及び被処理水のpH等により適宜選ばれるが、
一般的には、アニオン基含有親水性高分子物質1重量部
に対して、1〜2000重量部、好ましくは10〜10
00重量部、より好ましくは50〜1000重量部の割
合である。
The removing agent of the present invention contains sodium hydroxide.
Have. This sodium hydroxide has an action of controlling the solubility of the anionic group-containing hydrophilic high molecular weight substance, and the like. The proportion of sodium hydroxide used is not particularly limited and is appropriately selected depending on the type and amount of heavy metal ions dissolved in water, the pH of the water to be treated, etc.
Generally, 1 to 2000 parts by weight, preferably 10 to 10 parts by weight, relative to 1 part by weight of the anionic group-containing hydrophilic polymer substance.
The amount is 00 parts by weight, more preferably 50 to 1000 parts by weight.

【0009】本発明の除去剤は、必要に応じ、無害性の
多価金属化合物を含有する。このようなものには、硫酸
第1鉄、硫酸第2鉄、塩化第1鉄、塩化第2鉄等の鉄塩
の他、硫酸アルミニウム、塩化アルミニウム、水酸化カ
ルシウム、塩化カルシウム、硫酸マグネシウム、塩化マ
グネシウム、水酸化マグネシウム等が包含される。本発
明では、保存安定性及び価格の点で、硫酸第1鉄・7水
和物が好ましく使用される。これらの多価金属化合物は
アニオン基含有親水性高分子物質に対してイオン結合や
キレート結合を生成して、その高分子物質の溶解性をコ
ントロールする作用を示す。この多価金属化合物の使用
割合は特に制約されず、水中に溶解する金属イオンの種
類や量及び被処理水のpH等により適宜選ばれるが、一
般的には、アニオン基含有親水性高分子物質100重量
部に対して、1〜10000重量部、好ましくは20〜
5000重量部、より好ましくは100〜2000重量
部の割合である。
The removing agent of the present invention optionally contains a harmless polyvalent metal compound. In addition to iron salts such as ferrous sulfate, ferric sulfate, ferrous chloride and ferric chloride, aluminum sulfate, aluminum chloride, calcium hydroxide, calcium chloride, magnesium sulfate, chloride Magnesium, magnesium hydroxide and the like are included. In the present invention, ferrous sulfate heptahydrate is preferably used in terms of storage stability and price. These polyvalent metal compounds form an ionic bond or a chelate bond with respect to the anionic group-containing hydrophilic polymer substance, and exhibit the action of controlling the solubility of the polymer substance. The proportion of the polyvalent metal compound used is not particularly limited and is appropriately selected depending on the type and amount of metal ions dissolved in water, the pH of the water to be treated, and the like. Generally, anionic group-containing hydrophilic polymer substances are used. 1 to 10,000 parts by weight, preferably 20 to 100 parts by weight
The amount is 5000 parts by weight, and more preferably 100 to 2000 parts by weight.

【0010】本発明の除去剤は、粉末状又は該アニオン
基含有親水性高分子物質を非溶解状で含む水性液状で
って、水中に投入分散させるが、このようにして除去剤
を水中に投入分散させる場合には、それに含まれるアニ
オン基含有親水性物質は溶解せずに不溶性(非水溶性)
の状態で存在する。本発明による好ましい除去剤の1つ
の態様は、アニオン基含有親水性高分子物質と水酸化ナ
トリウムを含有し、その水酸化ナトリウムの濃度が高濃
度である水性液である。この水性液において、その水酸
化ナトリウムの濃度は10〜52重量%、好ましくは2
0〜50重量%である。そのアニオン基含有親水性高分
子物質の濃度は0.005〜10重量%、好ましくは
0.01〜3重量%である。
[0010] removing agent of the present invention, Oh aqueous liquid containing powder or the anion group-containing hydrophilic polymeric substance in undissolved form
Then, it is put into water and dispersed, but when the remover is put and dispersed in water in this way, the anionic group-containing hydrophilic substance contained therein is not dissolved and is insoluble (water-insoluble).
Exists in the state of. One embodiment of the preferred remover according to the present invention is an aqueous liquid containing an anionic group-containing hydrophilic polymer and sodium hydroxide, and the concentration of the sodium hydroxide is high. In this aqueous liquid, the sodium hydroxide concentration is 10 to 52% by weight, preferably 2
It is 0 to 50% by weight. The concentration of the anionic group-containing hydrophilic polymer substance is 0.005 to 10% by weight, preferably 0.01 to 3% by weight.

【0011】本発明による好ましい他の態様は、アニオ
ン基含有親水性高分子物質と水酸化ナトリウムと無害性
多価金属化合物を含有し、その水酸化ナトリウムの濃度
が高濃度である水性液である。この水性液において、そ
水酸化ナトリウムの濃度は5〜52重量%、好ましく
は10〜50重量%である。そのアニオン基含有親水性
高分子物質の濃度は0.005〜10重量%、好ましく
は0.01〜3重量%である。その無害性多価金属化合
物の濃度は0.03〜20重量%、好ましくは0.3〜
10重量%である。この水性液においては、アニオン基
含有親水性高分子物質は非溶解状態で存在する。前記無
害性多価金属化合物としては、特に、硫酸第一鉄の使用
が好ましい。
Another preferred embodiment according to the present invention is an aqueous liquid containing an anionic group-containing hydrophilic polymer, sodium hydroxide and a harmless polyvalent metal compound, and the concentration of sodium hydroxide is high. . In this aqueous liquid, the concentration of sodium hydroxide is 5 to 52% by weight, preferably 10 to 50% by weight. The concentration of the anionic group-containing hydrophilic polymer substance is 0.005 to 10% by weight, preferably 0.01 to 3% by weight. The concentration of the harmless polyvalent metal compound is 0.03 to 20% by weight, preferably 0.3 to
It is 10% by weight. In this aqueous liquid, the anionic group-containing hydrophilic polymer substance exists in a non-dissolved state. It is particularly preferable to use ferrous sulfate as the harmless polyvalent metal compound.

【0012】本発明の除去剤においては、凝集剤を併用
するのが好ましい。この場合の凝集剤は、フロックの凝
集に用いられているものであり、このようなものには、
キトサン、塩化カルシウム、ビス(リン酸2水素)カル
シウム、塩化第1鉄、塩化第2鉄、硫酸第1鉄、硫酸第
2鉄、硫酸アルミニウム、ポリ塩化アルミニウム等の無
機系凝集剤の他、ポリアクリルアミドのカチオン化変性
物、ポリアクリル酸ジメチルアミノエチルエステル、ポ
リメタクリル酸ジメチルアミノエチルエステル、ポリエ
チレンイミン、キトサン等のカチオン性有機系凝集剤、
ポリアクリルアミド等のノニオン性有機系凝集剤、ポリ
アクリル酸、アクリルアミドとアクリル酸との共重合体
及びその塩等のアニオン性有機系凝集剤が包含される。
In the removing agent of the present invention, it is preferable to use a coagulant together. The aggregating agent in this case is used for floc aggregating, and in such a thing,
In addition to inorganic flocculants such as chitosan, calcium chloride, calcium bis (dihydrogen phosphate), ferrous chloride, ferric chloride, ferrous sulfate, ferric sulfate, aluminum sulfate, polyaluminum chloride, poly Cationic organic flocculants such as cation-modified acrylamide, polyacrylic acid dimethylaminoethyl ester, polymethacrylic acid dimethylaminoethyl ester, polyethyleneimine, chitosan, etc.,
Nonionic organic flocculants such as polyacrylamide, anionic organic flocculants such as polyacrylic acid, copolymers of acrylamide and acrylic acid, and salts thereof are included.

【0013】本発明が適用される排水としては、銅イオ
ン、亜鉛イオン、ニッケルイオン、鉛イオン、クロムイ
オン、鉄イオンなどの溶存多価重金属イオンを1種又は
2種以上含有する排水が挙げられる。この排水中の重金
属イオンの濃度については特に制限はないし、共存する
他のイオンの制限もない。
Examples of wastewater to which the present invention is applied include wastewater containing one or more dissolved polyvalent heavy metal ions such as copper ions, zinc ions, nickel ions, lead ions, chromium ions and iron ions. . There is no particular limitation on the concentration of heavy metal ions in this wastewater, and there is no limitation on other coexisting ions.

【0014】本発明の除去剤を用いて水中に含まれる溶
存重金属イオンを除去するには、その水中に、その除去
剤を投入し、分散させて、重金属イオンを不溶化させ
る。この場合、水中に投入する除去剤中に含まれる水酸
化ナトリウムの量を、水中に含まれる溶存重金属イオン
を不溶性金属水酸化物として沈殿させるのに必要な理論
的量以上、通常、その理論的量の1〜1.5倍量、好ま
しくは1〜1.2倍量の割合で添加する。水中に投入す
る除去剤中の水酸化ナトリウムの量が不十分な場合に
は、その除去剤添加後に水酸化ナトリウムを添加し、溶
解状態の重金属イオンを不溶性水酸化物として沈殿させ
ればよい。また、重金属イオンの除去をより完全なもの
にするには、その除去剤の添加後、被処理水のpHを、
6〜12、好ましくは7〜11の範囲に調節するのが好
ましい。
In order to remove the dissolved heavy metal ions contained in water using the removing agent of the present invention, the removing agent is put into the water and dispersed to insolubilize the heavy metal ions. In this case, the hydroxide contained in the remover added to the water
The amount of sodium iodide is equal to or more than the theoretical amount required to precipitate dissolved heavy metal ions contained in water as an insoluble metal hydroxide, usually 1 to 1.5 times the theoretical amount, preferably 1 to It is added in the ratio of 1.2 times. When the amount of sodium hydroxide in the remover added to water is insufficient, sodium hydroxide may be added after the remover is added, and the heavy metal ions in the dissolved state may be precipitated as insoluble hydroxide. In addition, in order to make the removal of heavy metal ions more complete, after adding the removing agent, the pH of the water to be treated is
It is preferable to adjust the range of 6 to 12, preferably 7 to 11.

【0015】本発明の除去剤を用いて排水中に溶存する
重金属イオンを除去する場合、その排水は酸性排水であ
ることが好ましいが、その排水が中性やアルカリ性の場
合には、あらかじめその排水のpHを酸性領域、通常、
pH1〜7、好ましくは2〜4の範囲に調節するのが好
ましい。しかし、このような前以ってのpH調節は必ず
しも必要とはされず、本発明の場合、中性ないしアルカ
リ性排水には、本発明の除去剤を添加後、必要に応じて
そのpHを、6〜12の範囲、好ましくは6〜10の範
囲に調節することもできる。
When the heavy metal ions dissolved in the wastewater are removed by using the removing agent of the present invention, the wastewater is preferably acidic wastewater, but when the wastewater is neutral or alkaline, the wastewater is previously discharged. The pH of the acidic range, usually
It is preferable to adjust the pH to a range of 1 to 7, preferably 2 to 4. However, such pre-adjustment of pH is not always necessary, and in the case of the present invention, the neutral or alkaline waste water is added with the removing agent of the present invention, and then its pH is adjusted as necessary. It can be adjusted within the range of 6 to 12, preferably within the range of 6 to 10.

【0016】被処理水のpHをアルカリ性領域や酸性領
域に調節する場合、pH調節剤が用いられるが、このよ
うなpH調節剤としては、水酸化ナトリウム、水酸化カ
リウム、炭酸ナトリウム、炭酸カリウム、水酸化カルシ
ウム等のアルカリ性物質、もしくは塩酸、硫酸、硝酸等
の酸性物質が用いられる。
When the pH of the water to be treated is adjusted to an alkaline range or an acidic range, a pH adjusting agent is used. Examples of such a pH adjusting agent include sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, An alkaline substance such as calcium hydroxide or an acidic substance such as hydrochloric acid, sulfuric acid or nitric acid is used.

【0017】前記のようにして生成された不溶化重金属
イオンを吸着もしくは取り込んだゲルは、通常固液分離
可能なフロックであるが、そのフロックが十分でないと
きは凝集剤を添加しさらに巨大で強固なフロックにする
ことができる。本発明においては、前記のようにして生
成したフロックは、固液分離法により水中から分離す
る。この場合の固液分離法としては、濾過法や遠心分離
法、沈降法等の慣用の方法を採用することができる。本
発明による水中から溶存重金属イオンを除去するための
処理時間は、非常に短く、通常、1時間以内、特に30
分以内、好ましくは3〜10分である。
The gel in which the insolubilized heavy metal ions generated as described above are adsorbed or taken in is usually a floc capable of solid-liquid separation, but when the floc is not sufficient, a flocculant is added to make the gel larger and stronger. Can be flock. In the present invention, the flocs produced as described above are separated from water by the solid-liquid separation method. As the solid-liquid separation method in this case, a conventional method such as a filtration method, a centrifugation method, or a precipitation method can be adopted. The treatment time for removing dissolved heavy metal ions from the water according to the invention is very short, usually within 1 hour, in particular 30.
Within minutes, preferably 3 to 10 minutes.

【0018】本発明を実施する場合、アニオン基含有親
水性高分子物質としては、アルギン酸やそのアルカリ金
属塩のような水溶性のものが使用されるが、本発明の場
合、このような水溶性高分子物質でも円滑に使用するこ
とが可能である。即ち、アニオン基含有親水性高分子物
質は、水溶性を示すものであっても、アルカリ性物質及
び無害性多価金属化合物との混合物として水中に投入分
散することにより、その高分子物質の溶解を防止するこ
とができる。また、溶解性の低いアルギン酸カルシウム
を使用することによってその溶解をより効果的に防止す
ることができる。従って、本発明の場合には、その高分
子物質の粉体が完全溶解しない条件下においてその重金
属イオンの不溶化と固液分離を行えばよい。本発明を実
施する場合、必要に応じて、凝集剤を添加することがで
きる。この凝集剤の添加は、水中に分散するアニオン基
含有親水性高分子物質の他、有害性重金属イオンの不溶
化物を凝集させ、巨大フロックを生成させる作用を示
す。
In carrying out the present invention, as the anionic group-containing hydrophilic polymer substance, a water-soluble substance such as alginic acid or an alkali metal salt thereof is used. In the present invention, such a water-soluble substance is used. It is possible to smoothly use even polymer materials. That is, even if the anionic group-containing hydrophilic polymer is water-soluble, it can be dissolved by pouring and dispersing it in water as a mixture with an alkaline substance and a harmless polyvalent metal compound. Can be prevented. Further, the use of calcium alginate, which has low solubility, can prevent the dissolution more effectively. Therefore, in the case of the present invention, the heavy metal ions may be insolubilized and solid-liquid separated under the condition that the powder of the polymer substance is not completely dissolved. When practicing the present invention, an aggregating agent can be added if necessary. The addition of this aggregating agent has the effect of aggregating the insoluble matter of harmful heavy metal ions in addition to the anionic group-containing hydrophilic polymer substance dispersed in water to form a giant floc.

【0019】本発明において、酸性水中に含まれる重金
属イオンを除去する場合、先ず、その酸性水中に除去剤
を加え、必要に応じて、アルカリを加えて全体を撹拌す
る。これにより水中に含まれる重金属イオンは不溶化さ
れる。この際、水中に含まれる重金属イオンの一部は、
アニオン基含有親水性高分子物質と反応して、高分子の
不溶性塩を形成して沈殿を生じる。そして、この際、ア
ニオン基含有親水性高分子物質が存在することにより、
生成した重金属水酸化物のフロックをより大きく成長さ
せることができる。さらに、凝集剤を添加することによ
り、より巨大で、強固なフロックを沈殿させることがで
きる。
In the present invention, when removing heavy metal ions contained in acidic water, first, a removing agent is added to the acidic water, and if necessary, alkali is added and the whole is stirred. As a result, heavy metal ions contained in water are insolubilized. At this time, some of the heavy metal ions contained in the water are
Reacts with anionic group-containing hydrophilic polymeric material to form an insoluble salt of the polymeric material resulting in precipitation. And at this time, due to the presence of the anionic group-containing hydrophilic polymer,
Ru can be more greatly grow flocs generated heavy metal hydroxides. Furthermore, by adding a coagulant, larger and stronger flocs can be precipitated.

【0020】本発明において、被処理原水として用いら
れる重金属含有排水には、半導体製造業、鉄鋼・非鉄金
属業、電気機器製造業、機械器具製造業等の各種工場か
らの排水、メッキ工場からの排水、各種研究所からの排
水等が包含される。これらの排水の大部分は有害性の重
金属を含有する。本発明は、一般的には、Cu、Zn、
Cd、Pd、Ag、Al、Cr、Pb、Mn、Fe、N
i等の各種の重金属を含む排水の処理法として適用する
ことができる。
In the present invention, the heavy metal-containing wastewater used as raw water to be treated includes wastewater from various factories such as semiconductor manufacturing industry, iron and steel / nonferrous metal industry, electrical equipment manufacturing industry, machinery / equipment manufacturing industry, and plating factory. Drainage, drainage from various laboratories, etc. are included. Most of these effluents contain harmful heavy metals. The present invention generally relates to Cu, Zn,
Cd, Pd, Ag, Al, Cr, Pb, Mn, Fe, N
It can be applied as a method for treating wastewater containing various heavy metals such as i.

【0021】[0021]

【実施例】次に本発明を実施例によりさらに詳細に説明
する。以下の例はさらに本発明を説明しているものの、
いかなる形であり、請求されている本発明の範囲を制限
することを意図したものではない。
EXAMPLES Next, the present invention will be described in more detail by way of examples. Although the following examples further illustrate the invention,
It is in no way intended to limit the scope of the claimed invention.

【0022】処理例1 水酸化ナトリウム48wt%水溶液にアルギン酸ナトリ
ウム0.12重量%添加し、50℃で40分間撹拌した
後、硫酸第一鉄・七水和物を0.88重量%添加し、5
0℃で40分間撹拌したところ、灰色の懸濁液となっ
た。これを除去剤[I]とした。この除去剤[I]を、
銅、ニッケル、鉛、亜鉛各100ppmを含有するpH
2の被処理水に、アルギン酸ナトリウムと硫酸第一鉄の
合計濃度が12ppmとなるように添加したところ、p
H10となった。10分間撹拌した後、固液分離し、残
存金属イオン濃度を測定した。その結果、銅0.036
ppm、ニッケル0.074ppm、鉛0.153pp
m、亜鉛0.066ppmであり、良好な結果が得られ
た。
Treatment Example 1 0.12% by weight of sodium alginate was added to a 48% by weight aqueous solution of sodium hydroxide, the mixture was stirred at 50 ° C. for 40 minutes, and then 0.88% by weight of ferrous sulfate heptahydrate was added, 5
After stirring for 40 minutes at 0 ° C., a gray suspension resulted. This was designated as a remover [I]. This removing agent [I]
PH containing 100ppm each of copper, nickel, lead and zinc
When sodium alginate and ferrous sulfate were added to the treated water of No. 2 so that the total concentration was 12 ppm, p
It became H10. After stirring for 10 minutes, solid-liquid separation was performed, and the residual metal ion concentration was measured. As a result, copper 0.036
ppm, nickel 0.074 ppm, lead 0.153 pp
m, zinc was 0.066 ppm, and good results were obtained.

【0023】処理例2(比較例) 処理例1において、除去剤[I]の代わりに水酸化カル
シウム660ppmを被処理水に添加した以外は同様に
して実験を行った。その結果、処理水の残存金属イオン
濃度は、銅0.175ppm、ニッケル0.225pp
m、鉛0.270pm、亜鉛0.211ppmであっ
た。
Treatment Example 2 (Comparative Example) An experiment was conducted in the same manner as in Treatment Example 1 except that 660 ppm of calcium hydroxide was added to the water to be treated instead of the removing agent [I]. As a result, the residual metal ion concentration of the treated water was 0.175 ppm for copper and 0.225 pp for nickel.
m, lead 0.270 pm and zinc 0.211 ppm.

【0024】処理例3(比較例) 処理例1において、除去剤[I]の代わりに水酸化ナト
リウムをpH10になるまで添加した以外は同様にして
実験を行った。その結果、処理水の残存金属イオン濃度
は、銅0.294ppm、ニッケル0.583ppm,
鉛0.271ppm、亜鉛0.567ppmであった。
Treatment Example 3 (Comparative Example) An experiment was conducted in the same manner as in Treatment Example 1 except that sodium hydroxide was added in place of the removing agent [I] until the pH became 10. As a result, the residual metal ion concentration of the treated water was 0.294 ppm for copper, 0.583 ppm for nickel,
Lead was 0.271 ppm and zinc was 0.567 ppm.

【0025】処理例4 水酸化ナトリウム48wt%水溶液にアルギン酸ナトリ
ウム0.12重量%添加し、50℃で40分間撹拌して
懸濁液を作り、これを除去剤[II]とした。処理例1に
おいて、この除去剤[II]を用いた以外は同様にして実
験を行った。その結果、処理水の残存金属イオン濃度
は、銅0.035ppm、ニッケル0.083ppm、
鉛0.173ppm、亜鉛0.073ppmであり、良
好な結果が得られた。
Treatment Example 4 0.12% by weight of sodium alginate was added to a 48% by weight aqueous solution of sodium hydroxide and stirred at 50 ° C. for 40 minutes to prepare a suspension, which was used as a remover [II]. An experiment was conducted in the same manner as in Treatment Example 1 except that this removing agent [II] was used. As a result, the residual metal ion concentration of the treated water was 0.035 ppm for copper, 0.083 ppm for nickel,
Lead was 0.173 ppm and zinc was 0.073 ppm, and good results were obtained.

【0026】処理例5(比較例) 処理例1において、除去剤[I]の代わりに硫酸第一鉄
・七水和物を12ppm添加し、水酸化ナトリウムをp
H10になるまで添加した以外は同様にして実験を行っ
た。その結果、処理水の残存金属イオン濃度は、銅0.
146ppm、ニッケル0.329ppm、鉛0.20
5ppm、亜鉛0.286ppmであった。
Treatment Example 5 (Comparative Example) In Treatment Example 1, 12 ppm of ferrous sulfate heptahydrate was added in place of the removing agent [I], and sodium hydroxide was added to p.
The experiment was performed in the same manner except that the addition was performed until H10 was reached. As a result, the residual metal ion concentration of the treated water was 0.2%.
146ppm, nickel 0.329ppm, lead 0.20
It was 5 ppm and zinc 0.286 ppm.

【0027】処理例6 水酸化ナトリウム48wt%水溶液にアルギン酸ナトリ
ウム0.12重量%と硫酸第一鉄・七水和物0.88重
量%の混合物を添加し、60℃で2時間撹拌したとこ
ろ、黒色の懸濁液となった。これを除去剤[III]とし
た。処理剤1において、この除去剤[III]を用いた以
外は同様にして実験を行った。その結果、処理水の残存
金属イオン濃度は、銅0.031ppm、ニッケル0.
079ppm、鉛0.162ppm、亜鉛0.060p
pmであったが、処理水がわずかに黒色を呈した。
Treatment Example 6 A mixture of 0.12% by weight of sodium alginate and 0.88% by weight of ferrous sulfate heptahydrate was added to a 48% by weight aqueous solution of sodium hydroxide, and the mixture was stirred at 60 ° C. for 2 hours. It became a black suspension. This was designated as a remover [III]. An experiment was performed in the same manner as in Treatment Agent 1 except that this removing agent [III] was used. As a result, the residual metal ion concentration of the treated water was 0.031 ppm for copper and 0.
079ppm, lead 0.162ppm, zinc 0.060p
Although it was pm, the treated water was slightly black.

【0028】処理例7 銅444ppm、ニッケル448ppmを含有する実排
水に処理例1の除去剤[I](アルギン酸ナトリウム
0.12重量%、硫酸第一鉄・七水和物0.88重量%
含む)を添加してpH10とし、10分間撹拌した後、
固液分離した。処理水の残存金属濃度を表1に示す。
Treatment Example 7 The removing agent [I] of Treatment Example 1 (0.12% by weight of sodium alginate, 0.88% by weight of ferrous sulfate heptahydrate) was added to actual wastewater containing 444 ppm of copper and 448 ppm of nickel.
(Including) to a pH of 10 and stirred for 10 minutes,
Solid-liquid separation was performed. Table 1 shows the residual metal concentration of the treated water.

【0029】[0029]

【表1】 [Table 1]

【0030】処理例8(比較例) 処理例7において、除去剤[I]の代わりに水酸化カル
シウムを2800ppm添加した以外は同様にして実験
を行った。その結果、残存金属濃度は、銅0.25pp
m,、ニッケル0.31ppmであった。
Treatment Example 8 (Comparative Example) An experiment was conducted in the same manner as in Treatment Example 7 except that 2800 ppm of calcium hydroxide was added instead of the removing agent [I]. As a result, the residual metal concentration was 0.25 pp of copper.
m, and nickel was 0.31 ppm.

【0031】処理例9 銅50ppmを含有する実排水に処理例1の除去剤
[I]を添加してpH10とし、10分間撹拌した後、
固液分離した。処理水の残存金属濃度を表2に示す。
Treatment Example 9 To the actual wastewater containing 50 ppm of copper, the removing agent [I] of Treatment Example 1 was added to adjust the pH to 10, and after stirring for 10 minutes,
Solid-liquid separation was performed. Table 2 shows the residual metal concentration of the treated water.

【0032】[0032]

【表2】 [Table 2]

【0033】処理例10(比較例) 処理例9において、除去剤[I]の代わりに水酸化カル
シウムを2000ppm添加した以外は同様にして実験
を行った。その結果、残存銅濃度は、0.11ppmで
あった。
Treatment Example 10 (Comparative Example) An experiment was conducted in the same manner as in Treatment Example 9 except that 2000 ppm of calcium hydroxide was added instead of the removing agent [I]. As a result, the residual copper concentration was 0.11 ppm.

【0034】[0034]

【発明の効果】本発明によれば、各種の溶存重金属を含
む被処理水から、それに含まれる重金属を高い除去率で
かつ低められたスラッジ発生量で効率よく除去すること
ができる。
According to the present invention, it is possible to efficiently remove heavy metals contained in water to be treated containing various dissolved heavy metals with a high removal rate and a reduced sludge generation amount.

───────────────────────────────────────────────────── フロントページの続き (73)特許権者 597126848 和田 愼二 茨城県取手市戸頭4−18−9−101 (73)特許権者 000005979 三菱商事株式会社 東京都千代田区丸の内2丁目6番3号 (74)上記3名の代理人 100074505 弁理士 池浦 敏明 (72)発明者 辰巳 憲司 茨城県つくば市松代5−518−304 (72)発明者 和田 慎二 茨城県取手市戸頭4−15−18−302 (72)発明者 湯川 恭啓 兵庫県宝塚市逆瀬台5−16−14 (56)参考文献 特開 昭53−34624(JP,A) 特開 平10−34163(JP,A) 特開 昭61−274792(JP,A) 特開 昭54−22953(JP,A) 特表 昭58−500358(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 1/56,1/62 ─────────────────────────────────────────────────── ─── Continuation of front page (73) Patent holder 597126848 Shinji Wada 4-18-9-101 Togashira, Toride-shi, Ibaraki (73) Patent holder 000005979 Mitsubishi Corporation 2-3-6 Marunouchi, Chiyoda-ku, Tokyo (74) The above three agents 100074505 Patent Attorney Toshiaki Ikeura (72) Inventor Kenji Tatsumi 5-518-304 Matsushiro Tsukuba City, Ibaraki Prefecture (72) Shinji Wada 4-15-18-302 Togashira, Toride City, Ibaraki Prefecture (72) Inventor Yasuhiro Yukawa 5-16-14 Sakasedai, Takarazuka City, Hyogo Prefecture (56) References JP-A-53-34624 (JP, A) JP-A-10-34163 (JP, A) JP-A-61- 274792 (JP, A) JP 54-22953 (JP, A) Special Table 58-500358 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C02F 1 / 56,1 / 62

Claims (11)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水中に含まれる溶存重金属イオンを除去
する方法において、該水中に、アニオン基含有親水性高
分子物質と水酸化ナトリウムとの混合物からなる粉末状
又は該高分子物質を非溶解状で含む水性液状の重金属イ
オン除去剤を投入し、該除去剤中の該高分子物質を水中
に溶解させることなく分散させることにより、該水中に
含まれる溶存重金属イオンを不溶化させることを特徴と
する重金属イオンの除去方法。
1. A process for removing dissolved heavy metal ions contained in water, in the aqueous, anion-containing hydrophilic polymeric substance flour powder-like or polymeric material ing of a mixture of sodium hydroxide non Aqueous liquid heavy metal a contained in dissolved form
A method for removing heavy metal ions, which comprises injecting an on-removing agent and dispersing the polymer substance in the removing agent without dissolving it in water to insolubilize dissolved heavy metal ions contained in the water.
【請求項2】 該混合物が無害性多価金属化合物を含有
する請求項1の方法。
2. The method of claim 1 wherein said mixture contains a harmless polyvalent metal compound.
【請求項3】 該無害性多価金属化合物が、硫酸第一鉄
である請求項2の方法。
3. The method according to claim 2, wherein the harmless polyvalent metal compound is ferrous sulfate.
【請求項4】 該除去剤の添加後に、該水のpHを7〜
12の範囲に調節する請求項1〜3のいずれかの方法。
4. The pH of the water is adjusted to 7 to 7 after the removal agent is added.
The method according to claim 1, wherein the range is adjusted to 12.
【請求項5】 該水中に凝集剤を添加する請求項1〜4
のいずれかの方法。
5. A coagulant is added to the water.
Either way.
【請求項6】 該アニオン基含有親水性高分子物質が、
(i)アルギン酸もしくはその塩又は(ii)アルギン酸
もしくはその塩と他のアニオン基含有親水性高分子物質
との混合物からなる請求項1〜5のいずれかの方法。
6. The hydrophilic polymer substance containing an anion group,
The method according to claim 1, which comprises (i) alginic acid or a salt thereof, or (ii) a mixture of alginic acid or a salt thereof and another anionic group-containing hydrophilic polymer substance.
【請求項7】 水中に含まれる溶存重金属イオンを除去
するための除去剤であって、アニオン基含有親水性高分
子物質と水酸化ナトリウムとの混合物からなり、粉末状
又は該高分子物質を非溶解状で含む水性液状であり、か
つ該除去剤を水中に投入した場合に該高分子物質は不溶
性の状態で存在するものであることを特徴とする重金属
イオン除去剤。
7. A removing agent for removing dissolved heavy metal ions contained in the water, Ri Do from a mixture of an anionic group-containing hydrophilic polymeric substance with sodium hydroxide, powdered
Or an aqueous liquid containing the polymer substance in a non-dissolved state, or
The polymeric substance is insoluble when the remover is put into water.
Heavy metal ion removal agent characterized der Rukoto those present in sexual state.
【請求項8】 該混合物が無害性多価金属化合物を含有
する請求項7の重金属イオン除去剤。
8. The heavy metal ion removing agent according to claim 7, wherein the mixture contains a harmless polyvalent metal compound.
【請求項9】 該無害性多価金属化合物が硫酸第一鉄で
ある請求項8の重金属イオン除去剤。
9. The heavy metal ion removing agent according to claim 8, wherein the harmless polyvalent metal compound is ferrous sulfate.
【請求項10】 凝集剤を併用する請求項7〜9のいず
れかの重金属イオン除去剤。
10. The heavy metal ion removing agent according to claim 7, which further comprises an aggregating agent.
【請求項11】 該アニオン基含有親水性高分子物質
が、(i)アルギン酸もしくはその塩又は(ii)アルギ
ン酸もしくはその塩と他のアニオン基含有親水性高分子
物質との混合物からなる請求項7〜10のいずれかの重
金属イオン除去剤。
11. The hydrophilic polymer substance containing an anion group comprises (i) alginic acid or a salt thereof or (ii) a mixture of alginic acid or a salt thereof and another hydrophilic polymer substance containing an anion group. The heavy metal ion removal agent in any one of 10-10.
JP12771599A 1999-05-07 1999-05-07 Method and remover for removing heavy metal ions Expired - Lifetime JP3517697B2 (en)

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