JPH0464757B2 - - Google Patents

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Publication number
JPH0464757B2
JPH0464757B2 JP8999885A JP8999885A JPH0464757B2 JP H0464757 B2 JPH0464757 B2 JP H0464757B2 JP 8999885 A JP8999885 A JP 8999885A JP 8999885 A JP8999885 A JP 8999885A JP H0464757 B2 JPH0464757 B2 JP H0464757B2
Authority
JP
Japan
Prior art keywords
aqueous solution
hours
metal scavenger
polyamine
added
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
Application number
JP8999885A
Other languages
Japanese (ja)
Other versions
JPS61249590A (en
Inventor
Masafumi Morya
Kazuo Hosoda
Akira Nishimura
Tomio Imachi
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.)
Myoshi Oil and Fat Co Ltd
Original Assignee
Myoshi Oil and Fat Co 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 Myoshi Oil and Fat Co Ltd filed Critical Myoshi Oil and Fat Co Ltd
Priority to JP8999885A priority Critical patent/JPS61249590A/en
Priority to US06/853,692 priority patent/US4670180A/en
Priority to EP86105545A priority patent/EP0200143B1/en
Priority to DE8686105545T priority patent/DE3673222D1/en
Priority to AT86105545T priority patent/ATE55362T1/en
Priority to US06/905,977 priority patent/US4670160A/en
Publication of JPS61249590A publication Critical patent/JPS61249590A/en
Publication of JPH0464757B2 publication Critical patent/JPH0464757B2/ja
Granted legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Removal Of Specific Substances (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は金属捕集剤に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a metal scavenger.

〔従来の技術〕[Conventional technology]

近年、工場等の廃水による河川、海等の汚染が
問題となるにつれて、廃水による汚染防止のため
の規制が強化され、廃水中に含有される金属類を
所定濃度以下とすることが義務づけられており、
特に水銀、カドミウム、亜鉛、鉛、銅、クロム等
の人体に有害な重金属類に対しては特に厳しい規
制が設けられている。このため廃水中の金属類を
除去するための種々の方法が提案されており、こ
の種の方法として、イオン浮選法、イオン交換
法、電解浮上法、電気透析法、逆浸透圧法あるい
は消石灰、苛性ソーダ等のアルカリ中和剤を投入
して金属類を水酸化物とした後、高分子凝集剤に
より凝集沈澱して除去する中和凝集沈澱法等が知
られている。また金属捕集剤により金属を捕集し
て除去する方法も知られており、この種の金属捕
集剤として脂肪族ポリジチオカルバミン酸又はそ
の塩類を含有する金属捕集剤が知られている(特
開昭49−99978号)。
In recent years, as the pollution of rivers, oceans, etc. by wastewater from factories has become a problem, regulations to prevent pollution by wastewater have been strengthened, and it is now mandatory to keep metals contained in wastewater below a specified concentration. Ori,
Particularly strict regulations are in place for heavy metals that are harmful to the human body, such as mercury, cadmium, zinc, lead, copper, and chromium. For this reason, various methods have been proposed to remove metals from wastewater, including ion flotation, ion exchange, electrolytic flotation, electrodialysis, reverse osmosis, slaked lime, A known method is a neutralization coagulation-sedimentation method, in which metals are turned into hydroxides by adding an alkaline neutralizing agent such as caustic soda, and then removed by coagulation and precipitation using a polymer flocculant. A method of collecting and removing metals using a metal scavenger is also known, and a metal scavenger containing aliphatic polydithiocarbamic acid or its salts is known as this type of metal scavenger. (Japanese Patent Publication No. 49-99978).

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、イオン浮選法、イオン交換法、
電解浮上法、電気透析法、逆浸透圧法は重金属類
の除去率、操作性、ランニングコスト等に問題が
あり、一部の特殊な廃水処理のみにしか利用され
ていないのが現状である。また中和凝集沈澱法で
は大量の金属水酸化物のスラツジが生成し、これ
ら水酸化物のスラツジは脱水性が悪く、スラツジ
容積も大きいため運搬が困難であるという問題を
有するとともに重金属類を排水基準値以下に除去
することも非常に困難である。しかもこれらスラ
ツジは廃棄の仕方によつては再溶解して二次公害
を生じるという問題も含んでいる。
However, ion flotation method, ion exchange method,
The electrolytic flotation method, electrodialysis method, and reverse osmosis method have problems with the removal rate of heavy metals, operability, running costs, etc., and are currently only used for some special wastewater treatments. In addition, the neutralization coagulation precipitation method generates a large amount of metal hydroxide sludge, and these hydroxide sludges have problems such as poor dewatering properties and large sludge volumes, making it difficult to transport. It is also very difficult to remove it below the standard value. Moreover, depending on how these sludge is disposed of, there is also the problem that it may re-melt and cause secondary pollution.

一方、脂肪族ポリジチオカルバミン酸又はその
塩類を含有する金属捕集剤により金属を捕集して
除去する方法によれば上記の問題点は一応解消さ
れるものの、この金属捕集剤は分子量が小さいた
め添加量が多く必要となるとともに、生成フロツ
クも小さく、沈降性が悪い等の問題を有してい
た。
On the other hand, although the above problems can be solved by a method of collecting and removing metals using a metal scavenger containing aliphatic polydithiocarbamic acid or its salts, the molecular weight of this metal scavenger is small. Therefore, it is necessary to add a large amount, and the floc produced is small, resulting in problems such as poor sedimentation properties.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは上記の点に鑑み鋭意研究した結
果、ポリアミン類とエピハロヒドリンとが重縮合
した重縮合ポリアミンの活性水素原子と置換した
少なくとも1個のカルボジチオ酸基及び/又その
塩類を置換基として有する化合物が金属捕集剤と
して優れた性能を有することを見出し本発明を完
成するに至つた。
As a result of intensive research in view of the above points, the present inventors have found that at least one carbodithioic acid group and/or its salts are substituted with the active hydrogen atom of a polycondensed polyamine obtained by polycondensation of polyamines and epihalohydrin. The present inventors have discovered that the compound has excellent performance as a metal scavenger, and have completed the present invention.

即ち本発明はポリアミン類とエピハロヒドリン
とが重縮合した重縮合ポリアミンの活性水素原子
と置換した少なくとも1個のカルボジチオ酸基及
び/又はその塩類を置換基として有することを特
徴とする金属捕集剤を要旨とする。
That is, the present invention provides a metal scavenger characterized by having as a substituent at least one carbodithio acid group and/or a salt thereof substituted with an active hydrogen atom of a polycondensed polyamine obtained by polycondensation of a polyamine and an epihalohydrin. This is the summary.

本発明の金属捕集剤は重縮合ポリアミンの活性
水素原子と置換した少なくとも1個のカルボジチ
オ酸基:−CSSH及び/又はその塩類を置換基と
して有する構造の化合物であり、後述するように
ポリアミン類とエピハロヒドリンとを重縮合せし
めて重縮合ポリアミンとした後、この重縮合ポリ
アミンにカルボジチオ酸基あるいはその塩類を置
換基として導入する方法によるか、ポリアミン類
にカルボジチオ酸基あるいはその塩類を置換基と
して導入した後、エピハロヒドリンと重縮合せし
める方法により得られる。
The metal scavenger of the present invention is a compound having a structure having at least one carbodithioic acid group (-CSSH) and/or its salts as a substituent substituted with the active hydrogen atom of a polycondensed polyamine, and as described below and epihalohydrin are polycondensed to form a polycondensed polyamine, and then a carbodithio acid group or its salts are introduced as a substituent into the polycondensed polyamine, or a carbodithio acid group or its salts are introduced into polyamines as a substituent. After that, it is obtained by a method of polycondensation with epihalohydrin.

また本発明の金属捕集剤は重縮合ポリアミンの
窒素原子にN−置換基としてアルキル基、ヒドロ
キシアルキル基、アシル基の1種または2種以上
が結合していても良い。上記N−置換基はエピハ
ロヒドリンと重縮合せしめる前にポリアミン類を
メチルハライド、エチルハライド、ブチルハライ
ド、ラウリルハライド、ステアリルハライド等の
アルキルハライド;エチレンオキシド、プロピレ
ンオキシド、ブチレンオキシド、スチレンオキシ
ド、1,2−ドデシルエポキシアルカン、1,2
−オクタコシルエポキシアルカン等のエポキシア
ルカンあるいは酢酸、プロピオン酸、酪酸、カプ
ロン酸、カプリル酸、ラウリン酸、ミリスチン
酸、パルミチン酸、ステアリン酸、ベヘン酸等の
脂肪酸あるいはこれら脂肪酸のエステル類、また
はこれら脂肪酸の酸ハライド類と反応させるか、
ポリアミン類とエピハロヒドリンとを重縮合させ
て重縮合ポリアミンとした後、上記の如きアルキ
ルハライド、エポキシアルカンあるいは脂肪酸類
と反応させることにより導入することができる。
またN−置換基としては同種のものが分子中に2
個以上存在しても良く、異種のものが2個以上存
在しても良い。
Further, in the metal scavenger of the present invention, one or more types of an alkyl group, a hydroxyalkyl group, and an acyl group may be bonded to the nitrogen atom of the polycondensed polyamine as an N-substituent. The above-mentioned N-substituents are used to convert polyamines into alkyl halides such as methyl halide, ethyl halide, butyl halide, lauryl halide, stearyl halide, etc. before polycondensation with epihalohydrin; ethylene oxide, propylene oxide, butylene oxide, styrene oxide, 1,2- Dodecyl epoxy alkane, 1,2
- Epoxy alkanes such as octacosyl epoxy alkanes, fatty acids such as acetic acid, propionic acid, butyric acid, caproic acid, caprylic acid, lauric acid, myristic acid, palmitic acid, stearic acid, behenic acid, or esters of these fatty acids; React with acid halides of fatty acids, or
It can be introduced by polycondensing polyamines and epihalohydrin to obtain a polycondensed polyamine, and then reacting it with the above-mentioned alkyl halides, epoxyalkanes, or fatty acids.
Also, the same type of N-substituent is present in the molecule.
There may be more than one, and two or more of different types may exist.

本発明の金属捕集剤は重縮合ポリアミンの窒素
原子にカルボジチオ酸基及び/又その塩類が結合
した構造を有するものでも、アミン類とエピハロ
ヒドリンとが重縮合した際にエピハロヒドリン骨
格部分に生じる水酸基の水素原子と置換してカル
ボジチオ酸基及び/又その塩類が酸素原子に結合
した構造を有するものでも良く、また窒素原子と
酸素原子の両方に結合した構造を有するものでも
良い。上記カルボジチオ酸基の塩類としてはナト
リウム塩、カリウム塩等のアルカリ金属塩、カル
シウム塩、マグネシウム塩等のアルカリ土類金属
塩、アンモニウム塩等が挙げられる。
The metal scavenger of the present invention may have a structure in which a carbodithioic acid group and/or its salts are bonded to the nitrogen atom of a polycondensed polyamine. It may have a structure in which a carbodithioic acid group and/or its salt is bonded to an oxygen atom in substitution for a hydrogen atom, or it may have a structure in which it is bonded to both a nitrogen atom and an oxygen atom. Examples of the salts of the carbodithioic acid group include alkali metal salts such as sodium salts and potassium salts, alkaline earth metal salts such as calcium salts and magnesium salts, and ammonium salts.

上記ポリアミン類とは窒素原子に1個または2
個の活性水素原子が結合してなるイミノ基または
アミノ基を2個以上有する化合物であり、例えば
エチレンジアミン、プロピレンジアミン、ブチレ
ンジアミン、ヘキサメチレンジアミン、ジエチレ
ントリアミン、ジプロピレントリアミン、ジブチ
レントリアミン、トリエチレンテトラミン、トリ
プロピレンテトラミン、トリブチレンテトラミ
ン、テトラエチレンペンタミン、テトラプロピレ
ンペンタミン、テトラブチレンペンタミン、ペン
タエチレンヘキサミン等のポリアルキレンポリア
ミン;フエニレンジアミン、キシレンジアミン、
メタキシレンジアミン、イミノビスプロピルアミ
ン、モノメチルアミノプロピルアミン、メチルイ
ミノビスプロピルアミン、1,3−ビス(アミノ
メチル)シクロヘキサン、1,3−ジアミノプロ
パン、1,4−ジアミノブタン、3,5−ジアミ
ノクロロベンゼン、メラミン、1−アミノエチル
ピペラジン、ピペラジン、ジアミノフエニルエー
テル、3,3′−ジクロロベンジジン、トリジンベ
ース、m−トルイレンジアミン等やポリエチレン
ポリイミン(平均分子量300以上)等が挙げられ
る。また上記のポリアミン類の他に、これらのポ
リアミン類にアルキルハライド、エポキシアルカ
ンあるいは脂肪酸類を反応せしめる等により得ら
れるN−アルキルポリアミン、N−ヒドロキシア
ルキルポリアミンあるいはN−アシルポリアミン
等を用いることもできる。N−アルキルポリアミ
ンとしてはN−アルキルエチレンジアミン、N−
アルキルプロピレンジアミン、N−アルキルヘキ
サメチレンジアミン、N−アルキルフエニレンジ
アミン、N−アルキルキシレンジアミン、N−ア
ルキルジエチレントリアミン、N−アルキルトリ
エチレンテトラミン、N−アルキルテトラエチレ
ンペンタミン、N−アルキルペンタエチレンヘキ
サミン等を用いることができる。上記N−置換ア
ルキル基の炭素数は2〜18が好ましい。N−ヒド
ロキシアルキルポリアミンとしてはN−ヒドロキ
シエチルポリアミン、N−ヒドロキシプロピルポ
リアミン、N−ヒドロキシブチルポリアミン、N
−β−ヒドロキシドデシルポリアミン、N−β−
ヒドロキシテトラデシルポリアミン、N−β−ヒ
ドロキシヘキサデシルポリアミン、N−β−ヒド
ロキシオクタデシルポリアミン、N−β−ヒドロ
キシオクタコシルポリアミン等が挙げられる。ま
たN−アシルポリアミンとしては、N−アセチル
ポリアミン、N−プロピオニルポリアミン、N−
ブチルポリアミン、N−カプロイルポリアミン、
N−ラウロイルポリアミン、N−オレオイルポリ
アミン、N−ミリスチロイルポリアミン、N−ス
テアロイルポリアミン、N−ベヘロイルポリアミ
ン等が挙げられる。これらポリアミン類は単独ま
たは二種以上混合して用いることができる。また
エピハロヒドリンとしてはエピクロルヒドリン、
エピブロムヒドリン、エピヨードヒドリン、等が
挙げられる。
The above polyamines have 1 or 2 atoms per nitrogen atom.
A compound having two or more imino or amino groups formed by bonding active hydrogen atoms, such as ethylenediamine, propylenediamine, butylenediamine, hexamethylenediamine, diethylenetriamine, dipropylenetriamine, dibutylenetriamine, triethylenetetramine. , polyalkylene polyamines such as tripropylenetetramine, tributylenetetramine, tetraethylenepentamine, tetrapropylenepentamine, tetrabutylenepentamine, pentaethylenehexamine; phenylenediamine, xylenediamine,
meta-xylene diamine, iminobispropylamine, monomethylaminopropylamine, methyliminobispropylamine, 1,3-bis(aminomethyl)cyclohexane, 1,3-diaminopropane, 1,4-diaminobutane, 3,5-diamino Examples include chlorobenzene, melamine, 1-aminoethylpiperazine, piperazine, diaminophenyl ether, 3,3'-dichlorobenzidine, tolidine base, m-tolylenediamine, and polyethylene polyimine (average molecular weight 300 or more). In addition to the above polyamines, it is also possible to use N-alkyl polyamines, N-hydroxyalkyl polyamines, N-acyl polyamines, etc. obtained by reacting these polyamines with alkyl halides, epoxy alkanes, or fatty acids. . As the N-alkyl polyamine, N-alkylethylenediamine, N-
Alkylpropylene diamine, N-alkylhexamethylene diamine, N-alkylphenylene diamine, N-alkylxylene diamine, N-alkyldiethylenetriamine, N-alkyltriethylenetetramine, N-alkyltetraethylenepentamine, N-alkylpentaethylenehexamine etc. can be used. The N-substituted alkyl group preferably has 2 to 18 carbon atoms. Examples of N-hydroxyalkylpolyamines include N-hydroxyethylpolyamine, N-hydroxypropylpolyamine, N-hydroxybutylpolyamine, and N-hydroxybutylpolyamine.
-β-hydroxydodecylpolyamine, N-β-
Examples include hydroxytetradecylpolyamine, N-β-hydroxyhexadecylpolyamine, N-β-hydroxyoctadecylpolyamine, N-β-hydroxyoctacosylpolyamine, and the like. In addition, N-acylpolyamines include N-acetylpolyamine, N-propionylpolyamine, N-
Butyl polyamine, N-caproyl polyamine,
Examples include N-lauroylpolyamine, N-oleoylpolyamine, N-myristyroylpolyamine, N-stearoylpolyamine, and N-beheroylpolyamine. These polyamines can be used alone or in combination of two or more. Also, epihalohydrin is epichlorohydrin,
Examples include epibromohydrin, epiiodohydrin, and the like.

本発明の金属捕集剤はエピハロヒドリンと重縮
合せしめるポリアミン類(エピハロヒドリンと重
縮合せしめる前にポリアミンに置換基を導入する
場合は、置換基導入前のポリアミン類)がアミノ
基を2個有するジアミンの場合には直鎖状構造を
有し、一般に水溶性となる。また架橋構造を有す
る場合には水に対して分散性あるいは懸濁性とな
る。
The metal scavenger of the present invention is a polyamine that is polycondensed with epihalohydrin (in the case where a substituent is introduced into the polyamine before polycondensation with epihalohydrin, the polyamine before the introduction of the substituent) is a diamine having two amino groups. In some cases, it has a linear structure and is generally water-soluble. Further, when it has a crosslinked structure, it becomes dispersible or suspendable in water.

次に本発明の金属捕集剤の製造方法を具体的に
説明する。
Next, the method for producing the metal scavenger of the present invention will be specifically explained.

本発明の金属捕集剤を製造する第1の方法はポ
リアミン類とエピハロヒドリンとを重縮合させて
重縮合ポリアミンとした後、この重縮合ポリアミ
ンに二硫化炭素を作用させてカルボジチオ酸基を
導入する方法である。この方法ではまずアミン類
とエピハロヒドリンとを重縮合せしめて重縮合ポ
リアミンを得るが、この重縮合ポリアミンはアミ
ン類を加熱撹拌しつつエピハロヒドリンを滴下し
た後、1〜20時間、好ましくは1〜6時間加熱す
ることによつて得られる。エピハロヒドリンを滴
下する際のアミン類の加熱温度は10〜100℃、好
ましくは30〜90℃であり、エピハロヒドリン滴下
終了後の加熱温度は10〜150℃、好ましくは30〜
100℃である。次いでアルカリの存在下で重縮合
ポリアミンと二硫化炭素とを溶媒中で10〜100℃
で1〜20時間、好ましくは30〜60℃で1〜8時間
加熱することにより重縮合ポリアミンにカルボジ
チオ酸基及び/又はその塩基が導入されて本発明
の金属捕集剤が得られる。上記アルカリとしては
水酸化リチウム、水酸化カリウム、水酸化ナトリ
ウム、水酸化カルシウム、水酸化マグネシウム、
水酸化アンモニウム等が用いられる。また溶媒と
しては水、メタノール、アセトン、ジオキサン、
トルエン、ジメチルフオルムアミド等が用いられ
るが、特に水、アセトン、ジオキサンが好まし
い。
The first method for producing the metal scavenger of the present invention is to polycondensate polyamines and epihalohydrin to obtain a polycondensed polyamine, and then introduce a carbodithioic acid group by acting carbon disulfide on the polycondensed polyamine. It's a method. In this method, amines and epihalohydrin are first polycondensed to obtain a polycondensed polyamine. After the epihalohydrin is added dropwise to the amine while heating and stirring, the polycondensed polyamine is prepared for 1 to 20 hours, preferably 1 to 6 hours. Obtained by heating. The heating temperature of the amine when dropping epihalohydrin is 10 to 100°C, preferably 30 to 90°C, and the heating temperature after epihalohydrin is dropped is 10 to 150°C, preferably 30 to 90°C.
It is 100℃. Next, the polycondensed polyamine and carbon disulfide are heated in a solvent at 10 to 100°C in the presence of an alkali.
By heating for 1 to 20 hours, preferably at 30 to 60°C for 1 to 8 hours, carbodithioic acid groups and/or their bases are introduced into the polycondensed polyamine, thereby obtaining the metal scavenger of the present invention. The above alkalis include lithium hydroxide, potassium hydroxide, sodium hydroxide, calcium hydroxide, magnesium hydroxide,
Ammonium hydroxide etc. are used. Also, as a solvent, water, methanol, acetone, dioxane,
Toluene, dimethylformamide, etc. are used, and water, acetone, and dioxane are particularly preferred.

本発明の金属捕集剤を製造する第2の方法は、
ポリアミン類に二硫化炭素を作用せしめてカルボ
ジチオ酸基及び/又はその塩基を有するポリアミ
ン誘導体を製造し、次いでこのポリアミン誘導体
をエピハロヒドリンと重縮合せしめる方法であ
る。ポリアミン類と二硫化炭素との反応は、ポリ
アミン類と二硫化炭素とをアルカリの存在下で10
〜100℃で1〜20時間、好ましくは30〜60℃で1
〜5時間加熱することにより行われる。ポリアミ
ン類に二硫化炭素を反応せしめる際のアルカリと
しては上記第1の方法に用いられると同様のアル
カリが用いられる。上記反応は必要に応じて溶媒
中で行つてもよく、溶媒としては上記第1の方法
に用いられると同様の溶媒が用いられるが、特に
水、アセトン、ジオキサンが好ましい。次にカル
ボジチオ酸基及び/又はその塩類を導入したポリ
アミン誘導体をエピハロヒドリンと重縮合せしめ
るが、この反応は上記カルボジチオ酸基を導入し
たポリアミン誘導体を10〜100℃、好ましくは30
〜90℃に加熱し、撹拌下にエピハロヒドリンを滴
下した後、10〜150℃で1〜20時間、好ましくは
30〜100℃で1〜6時間保持することによつて行
われる。
The second method for producing the metal scavenger of the present invention is
This method involves reacting polyamines with carbon disulfide to produce a polyamine derivative having a carbodithioic acid group and/or its base, and then polycondensing this polyamine derivative with epihalohydrin. The reaction between polyamines and carbon disulfide is carried out by reacting polyamines and carbon disulfide in the presence of an alkali.
~100℃ for 1 to 20 hours, preferably 30 to 60℃ for 1 hour
This is done by heating for ~5 hours. As the alkali for reacting polyamines with carbon disulfide, the same alkali as used in the first method is used. The above reaction may be carried out in a solvent if necessary, and the same solvents used in the first method may be used, but water, acetone, and dioxane are particularly preferred. Next, the polyamine derivative into which the carbodithioic acid group and/or its salts have been introduced is polycondensed with epihalohydrin, and this reaction is carried out at a temperature of 10 to 100°C, preferably at 30°C.
After heating to ~90°C and adding epihalohydrin dropwise under stirring, at 10-150°C for 1-20 hours, preferably
This is carried out by holding at 30-100°C for 1-6 hours.

以上のようにしてカルボジチオ酸基及び/又は
その塩類を置換基として有する本発明の金属捕集
剤が得られるが、カルボジチオ酸のアルカリ金属
塩基、アンモニウム塩基を置換基として有する金
属捕集剤を、カルシウム、マグネシウムの水酸化
物や、カルシウム、マグネシウムの塩化物、硝酸
塩、硫酸塩等の水溶性のアルカリ土類金属塩を用
いて処理してアルカリ土類金属と置換する方法に
よりカルボジチオ酸のアルカリ土類金属塩を置換
基とする金属捕集剤とすることもできる。
The metal scavenger of the present invention having a carbodithioic acid group and/or its salt as a substituent can be obtained as described above. The alkaline earth of carbodithioic acid is treated with a water-soluble alkaline earth metal salt such as calcium or magnesium hydroxide or calcium or magnesium chloride, nitrate, or sulfate to replace the alkaline earth metal. A metal scavenger having a similar metal salt as a substituent can also be used.

本発明の金属捕集剤によれば水銀、カドミウ
ム、亜鉛、鉛、銅、クロム、砒素、金、銀、白
金、バナジウム、タリウム等の金属を効率良く捕
集して除去することができる。
According to the metal collector of the present invention, metals such as mercury, cadmium, zinc, lead, copper, chromium, arsenic, gold, silver, platinum, vanadium, and thallium can be efficiently collected and removed.

〔実施例〕〔Example〕

以下、実施例を挙げて本発明を更に詳細に説明
する。
Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例 1 撹拌機、温度計、滴下ロート、及び還流冷却器
を付けた1の4つ口フラスコにメタキシレンジ
アミン261.1gと水−アセトン(1:1)混合物
300gを入れ、撹拌下に60℃に加熱し、これにエ
ピクロルヒドリン174gを4時間かけて90℃を超
えないように温度調整を行いながら滴下し、滴下
終了後80〜90℃で1時間保持し、メタキシレンジ
アミンとエピクロルヒドリンとが重縮合した重縮
合ポリアミンの水−アセトン溶液727gを得た。
Example 1 261.1 g of metaxylene diamine and a water-acetone (1:1) mixture were placed in a four-necked flask equipped with a stirrer, thermometer, dropping funnel, and reflux condenser.
300g was added and heated to 60°C with stirring, and 174g of epichlorohydrin was added dropwise over 4 hours while controlling the temperature so as not to exceed 90°C. After the dropwise addition was completed, it was held at 80 to 90°C for 1 hour. 727 g of a water-acetone solution of a polycondensed polyamine obtained by polycondensing meta-xylene diamine and epichlorohydrin was obtained.

次いで上記重縮合ポリアミン溶液234.1g、純
水517.4gおよび水酸化ナトリウム59.9gを上記
と同様の装置に入れ、40℃にて撹拌下に86.9gの
二硫化炭素を3時間かけて滴下した。更に同温度
で1時間保持した後、60〜90℃にて水−アセトン
を留去した後、水305gを加えて反応生成物(金
属捕集剤)の水溶液を得た。この反応生成物の水
溶液の粘度84mPa・s(25℃)であり、また金属
捕集剤の濃度は27.2%であつた。
Next, 234.1 g of the polycondensed polyamine solution, 517.4 g of pure water, and 59.9 g of sodium hydroxide were placed in the same apparatus as above, and 86.9 g of carbon disulfide was added dropwise over 3 hours while stirring at 40°C. After further holding at the same temperature for 1 hour, water-acetone was distilled off at 60 to 90°C, and 305 g of water was added to obtain an aqueous solution of the reaction product (metal scavenger). The viscosity of the aqueous solution of this reaction product was 84 mPa·s (25°C), and the concentration of the metal scavenger was 27.2%.

次にCu2+として100mg/含有する水溶液1
に対し、上記金属捕集剤の水溶液を金属捕集剤と
しての添加量が40mg、85mg、125mg、165mgとなる
ように添加し、10分間撹拌し、金属捕集剤に銅が
捕集されて生成した沈澱物を分離し、溶液中に残
存しているCu2+濃度を測定したところ、各々60
mg/、28mg/、13mg/、0.05mg/であつ
た。この結果よりこの金属捕集剤へのCu2+の捕
集量を求めたところ、300mg−Cu/g(金属捕集
剤1g当たり)であつた。またHg2+として100
mg/含有する水溶液を用い、上記銅含有水溶液
と同様の実験を行い、この結果より金属捕集剤へ
のHg2+の捕集量を求めたところ、1172mg−Hg/
gであつた。
Next, aqueous solution 1 containing 100mg/Cu 2+
To this, an aqueous solution of the above metal collector was added so that the amount of the metal collector was 40 mg, 85 mg, 125 mg, and 165 mg, and the mixture was stirred for 10 minutes until the copper was collected by the metal collector. When the precipitates formed were separated and the concentration of Cu 2+ remaining in the solution was measured, each was found to be 60
mg/, 28 mg/, 13 mg/, and 0.05 mg/. From this result, the amount of Cu 2+ captured by this metal scavenger was determined to be 300 mg-Cu/g (per 1 g of metal scavenger). Also 100 as Hg 2+
An experiment similar to the above copper-containing aqueous solution was conducted using an aqueous solution containing 1,172 mg-Hg/
It was hot at g.

実施例 2 実施例1と同様の装置の中にエチレンジアミン
30.6g、純水450g、水酸化カリウム57.2gを入
れ、50℃にて二硫化炭素77.5gを4時間かけて滴
下した後、60℃にて3時間加熱しカルボジチオ酸
カリウム塩基を置換基として有するエチレンジア
ミン誘導体を得た。次いで30℃に冷却し、この中
にエピクロルヒドリン47.2gを5時間かけて滴下
した後、70〜90℃にて3時間反応を続けた。得ら
れた反応生成物に308gの純水を加え、金属捕集
剤の20%水溶液を得た。この水溶液の粘度は32m
Pa・s(25℃)であつた。
Example 2 Ethylenediamine was placed in an apparatus similar to Example 1.
30.6 g, pure water 450 g, and potassium hydroxide 57.2 g were added, and 77.5 g of carbon disulfide was added dropwise at 50°C over 4 hours, and then heated at 60°C for 3 hours to form a solution containing potassium carbodithioate base as a substituent. An ethylenediamine derivative was obtained. Next, the mixture was cooled to 30°C, and 47.2 g of epichlorohydrin was added dropwise thereto over 5 hours, and the reaction was continued at 70 to 90°C for 3 hours. 308 g of pure water was added to the obtained reaction product to obtain a 20% aqueous solution of metal scavenger. The viscosity of this aqueous solution is 32m
The temperature was Pa·s (25°C).

この金属捕集剤の水溶液を用い、実施例1と同
様の銅含有水溶液及び水銀含有水溶液を同様の方
法で処理し、この結果より金属捕集剤へのCu2+
Hg2+の捕集量を求めたところ、それぞれ168mg−
Cu/g、637mg−Hg/gであつた。
Using this aqueous solution of metal scavenger, the same copper-containing aqueous solution and mercury-containing aqueous solution as in Example 1 were treated in the same manner, and the results showed that Cu 2+ and
When the amount of Hg 2+ collected was determined, it was 168 mg−
Cu/g and 637 mg-Hg/g.

実施例 3 温度計、還流冷却器、撹拌機及び滴下ロートを
付けた500mlの4つ口フラスコにメタキシレンジ
アミン71.2g、7.5%水酸化ナトリウム水溶液279
gを入れ、激しく撹拌しながら45℃にて二硫化炭
素79.6gを6時間かけて滴下し、滴下終了後、同
温度にて1.5時間反応を行い、更に70℃で2時間
反応を行い、カルボジチオ酸基及びカルボジチオ
酸ナトリウム塩基を置換基として有する反応生成
物の水溶液を得た。
Example 3 In a 500 ml four-necked flask equipped with a thermometer, reflux condenser, stirrer, and dropping funnel, 71.2 g of metaxylene diamine and 279 g of a 7.5% aqueous sodium hydroxide solution were added.
79.6 g of carbon disulfide was added dropwise over 6 hours at 45°C with vigorous stirring. After the dropwise addition, the reaction was carried out at the same temperature for 1.5 hours, and then at 70°C for 2 hours. An aqueous solution of a reaction product having an acid group and a sodium carbodithioate base as a substituent was obtained.

上記水溶液400gと純水267.3gを上記と同様の
装置に入れ、60℃にてエピクロルヒドリン50.3g
を4時間かけて添加し、さらに70〜80℃にて1時
間反応を行い、金属捕集剤の水溶液を得た。
Put 400g of the above aqueous solution and 267.3g of pure water into the same device as above, and heat 50.3g of epichlorohydrin at 60℃.
was added over a period of 4 hours, and the reaction was further carried out at 70 to 80°C for 1 hour to obtain an aqueous solution of a metal scavenger.

得られた金属捕集剤の水溶液中には金属捕集剤
が28.1%含有されていた。また、この金属捕集剤
水溶液の粘度は73mPa・s(25℃)であつた。
The resulting aqueous solution of metal scavenger contained 28.1% metal scavenger. Further, the viscosity of this metal scavenger aqueous solution was 73 mPa·s (25°C).

上記金属捕集剤の水溶液を用いて実施例1と同
様の方法で銅含有水溶液および水銀含有水溶液を
処理し、この金属捕集剤へのCu2+、Hg2+の捕集
量を求めたところ、それぞれ300mg−Cu/g、
1143mg−Hg/gであつた。
A copper-containing aqueous solution and a mercury-containing aqueous solution were treated using the aqueous solution of the above metal scavenger in the same manner as in Example 1, and the amounts of Cu 2+ and Hg 2+ captured by this metal scavenger were determined. However, 300mg-Cu/g, respectively.
It was 1143 mg-Hg/g.

実施例 4 実施例3と同様の装置にジエチレントリアミン
21.0g、純水326.4gおよび水酸化ナトリウム24.5
gを入れ、40℃にて二硫化炭素46.5gを3時間か
けて滴下した。滴下終了後70℃で更に反応を行つ
た後、約30℃まで冷却しエピブロモヒドリン34.4
gを2時間かけて添加した後、80〜90℃に昇温し
て2時間反応を続け、27.1%の金属捕集剤を含有
する水溶液を得た。この水溶液の粘度は58m
Pa・s(25℃)であつた。
Example 4 Diethylenetriamine was added to the same apparatus as in Example 3.
21.0g, pure water 326.4g and sodium hydroxide 24.5g
g, and 46.5 g of carbon disulfide was added dropwise at 40° C. over 3 hours. After the dropwise addition was completed, the reaction was further carried out at 70°C, and then cooled to approximately 30°C and epibromohydrin 34.4
g was added over 2 hours, the temperature was raised to 80 to 90°C, and the reaction was continued for 2 hours to obtain an aqueous solution containing 27.1% of the metal scavenger. The viscosity of this aqueous solution is 58m
The temperature was Pa·s (25°C).

上記金属捕集剤の水溶液を用いて実施例1と同
様の方法により銅含有水溶液及び水銀含有水溶液
を処理し、この結果より金属捕集剤へのCu2+
Hg2+の捕集量を求めたところ、それぞれ169mg−
Cu/g、651mg−Hg/gであつた。
A copper-containing aqueous solution and a mercury-containing aqueous solution were treated using the aqueous solution of the metal scavenger in the same manner as in Example 1, and the results showed that Cu 2+ in the metal scavenger,
When the amount of Hg 2+ collected was determined, it was 169 mg−
Cu/g and 651 mg-Hg/g.

実施例 5 実施例1と同様の装置にジエチレントリアミン
29.9gおよびトルエン120gを入れ、40〜50℃で
エピクロルヒドリン26.8gを3時間かけて滴下
し、滴下終了後60℃で2時間反応を続けた。次い
で、これに水酸化ナトリウム46.4gおよび純水
641.8gを加えて40℃にて二硫化炭素66.1gを2
時間かけて滴下し、滴下終了後更に70℃にて4時
間反応を行つた。反応終了後30℃に冷却し、撹拌
を停止すると2層に分離した。上層のトルエンを
除去した後、撹拌下に40℃に加熱してブロモメチ
ルオキシラン48.9gを3時間かけて滴下し、滴下
終了後70〜80℃で1時間反応を続け、金属捕集剤
の水溶液を得た。得られた水溶液中には金属捕集
剤が22.6%含有されていた。この水溶液の粘度は
32mPa・s(25℃)であつた。
Example 5 Diethylenetriamine was added to the same apparatus as in Example 1.
29.9 g and 120 g of toluene were added thereto, and 26.8 g of epichlorohydrin was added dropwise over 3 hours at 40 to 50°C. After the dropwise addition was completed, the reaction was continued at 60°C for 2 hours. Next, add 46.4g of sodium hydroxide and pure water to this.
Add 641.8g of carbon disulfide to 66.1g of carbon disulfide at 40℃.
The mixture was added dropwise over a period of time, and after the completion of the addition, the reaction was further carried out at 70°C for 4 hours. After the reaction was completed, the mixture was cooled to 30° C., stirring was stopped, and the mixture was separated into two layers. After removing the toluene in the upper layer, it was heated to 40°C with stirring, and 48.9 g of bromomethyloxirane was added dropwise over 3 hours. After the dropwise addition, the reaction was continued at 70 to 80°C for 1 hour to form an aqueous solution of the metal scavenger. I got it. The resulting aqueous solution contained 22.6% metal scavenger. The viscosity of this aqueous solution is
It was 32mPa・s (25℃).

上記金属捕集剤の水溶液を用いて実施例1と同
様の水溶液の処理を行い、金属捕集剤へのCu2+
Hg2+の捕集量を求めたところ、それぞれ145mg−
Cu/g、546mg−Hg/gあつた。
Using the aqueous solution of the metal scavenger, the aqueous solution was treated in the same manner as in Example 1 to remove Cu 2+ and
When the amount of Hg 2+ collected was determined, it was 145 mg−
Cu/g, 546 mg-Hg/g hot.

実施例 6 実施例1と同様の装置にジエチレントリアミン
31.1gを入れ、90℃にてエポキシアルカン(アル
キル基の炭素数28)123.2gを30分かけて滴下し、
滴下終了後同温度にて更に2時間反応を行い、N
−ヒドロキシアルキルジエチレントリアミンを得
た。次いで40℃に冷却し、この中に純水667.7g
及び水酸化ナトリウム24.2gを加えた後、二硫化
炭素45.9gを2時間かけて滴下し、滴下終了後70
℃にて3時間反応を続けた。反応終了後、80〜90
℃にて27.9gのエピクロルヒドリンを3時間かけ
て滴下し、滴下終了後90〜100℃にて更に3時間
反応を続けた。
Example 6 Diethylenetriamine was added to the same apparatus as in Example 1.
31.1g was added, and 123.2g of epoxyalkane (alkyl group has 28 carbon atoms) was added dropwise at 90℃ over 30 minutes.
After the dropwise addition, the reaction was further carried out at the same temperature for 2 hours, and N
-Hydroxyalkyldiethylenetriamine was obtained. Next, it was cooled to 40℃, and 667.7g of pure water was added to it.
After adding 24.2 g of sodium hydroxide, 45.9 g of carbon disulfide was added dropwise over 2 hours.
The reaction was continued for 3 hours at ℃. After the reaction is completed, 80-90
27.9 g of epichlorohydrin was added dropwise over 3 hours at a temperature of 0.degree. C., and after the addition was completed, the reaction was continued at 90 to 100.degree. C. for an additional 3 hours.

上記のようにして得られた反応生成物に純水を
260.9g加え、20.0%の金属捕集剤を含有する水
溶液を得た。この水溶液の粘度は45mPa・s(25
℃)であつた。
Add pure water to the reaction product obtained as above.
260.9g was added to obtain an aqueous solution containing 20.0% metal scavenger. The viscosity of this aqueous solution is 45 mPa・s (25
℃).

上記水溶液を用いて実施例1と同様にして銅含
有水溶液及び水銀含有水溶液を処理し、この金属
捕集剤へのCu2+、Hg2+の捕集量を求めたところ、
それぞれ80mg−Cu/g、302mg−Hg/gであつ
た。
A copper-containing aqueous solution and a mercury-containing aqueous solution were treated using the above aqueous solution in the same manner as in Example 1, and the amounts of Cu 2+ and Hg 2+ captured by the metal collector were determined.
They were 80 mg-Cu/g and 302 mg-Hg/g, respectively.

実施例 7 N,N′′′′−ビス(ヒドロキシエチル)トリエ
チレンテトラミン62.7gを実施例3と同様の装置
に入れ、50℃にてエピクロルヒドリン24.8gを4
時間かけて滴下し、滴下終了後80〜90℃にて更に
2時間反応を続けた。次いでこれに8%水酸化ナ
トリウム水溶液672.7gを加え、50℃にて二硫化
炭素81.5gを2時間かけて滴下し、滴下終了後70
℃に昇温して3時間反応を続け、金属捕集剤を
22.3%含有する水溶液を得た。この水溶液の粘度
は48mPa・s(25℃)であつた。
Example 7 62.7 g of N,N′′′′-bis(hydroxyethyl)triethylenetetramine was placed in the same apparatus as in Example 3, and 24.8 g of epichlorohydrin was added at 50°C.
The mixture was added dropwise over a period of time, and after the completion of the addition, the reaction was continued for an additional 2 hours at 80-90°C. Next, 672.7 g of 8% sodium hydroxide aqueous solution was added to this, and 81.5 g of carbon disulfide was added dropwise at 50°C over 2 hours.
The temperature was raised to ℃, the reaction was continued for 3 hours, and the metal scavenger was removed.
An aqueous solution containing 22.3% was obtained. The viscosity of this aqueous solution was 48 mPa·s (25°C).

上記金属捕集剤を含有する水溶液を用いて実施
例1と同様の水溶液の処理を行い、金属捕集剤へ
のCu2+、Hg2+の捕集量を求めたところ、それぞ
れ177mg−Cu/g、666mg−Hg/gであつた。
The aqueous solution containing the above metal scavenger was treated in the same manner as in Example 1, and the amounts of Cu 2+ and Hg 2+ captured by the metal scavenger were determined to be 177 mg-Cu, respectively. /g, 666 mg-Hg/g.

実施例 8 実施例1と同様の装置にポリエチレンイミン
(平均分子量70000)22.4g及び1.1%水酸化ナト
リウム水溶液933.2gを入れ、50℃にて二硫化炭
素19.7gを1時間かけて滴下し、滴下終了後同温
度にて更に2時間反応させた。次いでエピクロル
ヒドリン0.5gを3時間かけて滴下し、その後80
℃にて2時間反応を続けた。得られた反応生成物
の粘度は28mPa・s(25℃)であり、5%の金属
捕集剤を含有していた。
Example 8 22.4 g of polyethyleneimine (average molecular weight 70,000) and 933.2 g of a 1.1% aqueous sodium hydroxide solution were placed in the same apparatus as in Example 1, and 19.7 g of carbon disulfide was added dropwise at 50°C over 1 hour. After completion of the reaction, the reaction was continued for an additional 2 hours at the same temperature. Next, 0.5 g of epichlorohydrin was added dropwise over 3 hours, and then 80 g of
The reaction continued at ℃ for 2 hours. The resulting reaction product had a viscosity of 28 mPa·s (25°C) and contained 5% metal scavenger.

上記金属捕集剤を含有する水溶液を用いて実施
例1と同様の水溶液の処理を行い、金属捕集剤へ
のCu2+、Hg2+の捕集量を求めたところ、それぞ
れ214mg−Cu/g、821mg−Hg/gであつた。
The aqueous solution containing the above metal scavenger was treated in the same manner as in Example 1, and the amount of Cu 2+ and Hg 2+ captured by the metal scavenger was determined to be 214 mg-Cu. /g, and 821 mg-Hg/g.

実施例 9 実施例3と同様の装置にN−メチルジエチレン
トリアミン42.5gと水−ジオキサン(2:1)混
合物50gを入れ、エピクロルヒドリン33.6gを70
℃で滴下を開始し、95℃を超えないように温度調
整を行いながら4時間かけて滴下した後、更に90
〜95℃にて2時間反応を続けた。次いで40℃に冷
却して純水230g、水酸化ナトリウム43.6gを加
え、二硫化炭素55.3gを3時間かけて滴下し、滴
下終了後70℃にて減圧下、ジオキサンが検出され
なくなるまでトツピングを行つた後、純水120g
を加えて金属捕集剤の水溶液を得た。得られた水
溶液中の金属捕集剤濃度は22.5%であり、この水
溶液の粘度は31mPa・s(25℃)であつた。
Example 9 42.5 g of N-methyldiethylenetriamine and 50 g of a water-dioxane (2:1) mixture were placed in the same apparatus as in Example 3, and 33.6 g of epichlorohydrin was added to 70 g of a mixture of water and dioxane (2:1).
Start dropping at a temperature of 95°C, continue dropping for 4 hours while adjusting the temperature so as not to exceed 95°C.
The reaction continued for 2 hours at ~95°C. Next, the mixture was cooled to 40°C, 230g of pure water and 43.6g of sodium hydroxide were added, and 55.3g of carbon disulfide was added dropwise over 3 hours. After the dropwise addition, topping was continued at 70°C under reduced pressure until dioxane was no longer detected. After going, 120g of pure water
was added to obtain an aqueous solution of a metal scavenger. The metal scavenger concentration in the obtained aqueous solution was 22.5%, and the viscosity of this aqueous solution was 31 mPa·s (25°C).

上記金属捕集剤を含有する水溶液を用いて実施
例1と同様の水溶液の処理を行い、金属捕集剤へ
のCu2+、Hg2+の捕集量を求めたところ、それぞ
れ157mg−Cu/g、594mg−Hg/gであつた。
The aqueous solution containing the above metal scavenger was treated in the same manner as in Example 1, and the amount of Cu 2+ and Hg 2+ captured by the metal scavenger was determined to be 157 mg-Cu. /g, and 594 mg-Hg/g.

実施例 10 実施例1と同様の装置にN−メチルエチレンジ
アミン64g、純水619.9g及び水酸化ナトリウム
34.6gを入れ、これに二硫化炭素65.7gを50℃に
て3時間かけて滴下し、滴下終了後更に70℃にて
2時間反応を続けた。反応終了後、30℃に冷却
し、エピクロルヒドリン79.9gを70℃にて3時間
かけて滴下し、さらに同温度にて3時間反応を続
け、金属捕集剤の水溶液を得た。
Example 10 In a device similar to Example 1, 64 g of N-methylethylenediamine, 619.9 g of pure water, and sodium hydroxide were added.
34.6 g of carbon disulfide was added thereto, and 65.7 g of carbon disulfide was added dropwise thereto at 50°C over 3 hours, and after the dropwise addition was completed, the reaction was continued at 70°C for an additional 2 hours. After the reaction was completed, the mixture was cooled to 30° C., 79.9 g of epichlorohydrin was added dropwise at 70° C. over 3 hours, and the reaction was further continued at the same temperature for 3 hours to obtain an aqueous solution of a metal scavenger.

得られた水溶液中の金属捕集剤濃度は26.5%で
あり、水溶液中の粘度は88mPa・s(25℃)であ
つた。
The metal scavenger concentration in the resulting aqueous solution was 26.5%, and the viscosity of the aqueous solution was 88 mPa·s (25°C).

上記金属捕集剤を含有する水溶液を用いて実施
例1と同様の水溶液の処理を行い、金属捕集剤へ
のCu2+、Hg2+の捕集量を求めたところ、それぞ
れ130mg−Cu/g、430mg−Hg/gであつた。
The aqueous solution containing the above metal scavenger was treated in the same manner as in Example 1, and the amount of Cu 2+ and Hg 2+ captured by the metal scavenger was determined to be 130 mg-Cu. /g, and 430 mg-Hg/g.

比較例 1 実施例1と同様の装置に30.6gのエチレンジア
ミン、450gの純水及び57.2gの水酸化カリウム
を入れ、実施例2と同様の条件で二硫化炭素77.5
gを添加して反応させ反応生成物を得た。これに
水を加えて20%濃度とした水溶液の粘度は4m
Pa・s(25℃)であつた。
Comparative Example 1 30.6 g of ethylenediamine, 450 g of pure water and 57.2 g of potassium hydroxide were placed in the same apparatus as in Example 1, and 77.5 g of carbon disulfide was added under the same conditions as in Example 2.
g was added and reacted to obtain a reaction product. The viscosity of the aqueous solution made by adding water to make it 20% is 4m.
The temperature was Pa·s (25°C).

上記水溶液を用い、実施例1と同様の水溶液を
処理し、Cu2+、Hg2+の捕集量を求めたところ、
それぞれ108mg−Cu/g、403mg−Hg/gであつ
た。
Using the above aqueous solution, the same aqueous solution as in Example 1 was treated and the amount of collected Cu 2+ and Hg 2+ was determined.
They were 108 mg-Cu/g and 403 mg-Hg/g, respectively.

比較例 2 実施例1と同様の装置にペンタエチレンヘキサ
ミン50.9g、純水300g及び水酸化ナトリウム
52.7gを入れ、実施例2と同様の条件で二硫化炭
素100.1gを添加して反応させ反応生成物を得た。
これに水を加えて20%濃度とした水溶液の粘度は
6mPa・s(25℃)であつた。
Comparative Example 2 50.9 g of pentaethylenehexamine, 300 g of pure water, and sodium hydroxide were placed in the same apparatus as in Example 1.
52.7 g of carbon disulfide was added and reacted under the same conditions as in Example 2 to obtain a reaction product.
The viscosity of an aqueous solution made by adding water to a 20% concentration was 6 mPa·s (25°C).

上記水溶液を用い、実施例1と同様の水溶液を
処理し、Cu2+、Hg2+の捕集量を求めたところ、
それぞれ298mg−Cu/g、1068mg−Hg/gであ
つた。
Using the above aqueous solution, the same aqueous solution as in Example 1 was treated and the amount of collected Cu 2+ and Hg 2+ was determined.
They were 298 mg-Cu/g and 1068 mg-Hg/g, respectively.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明の金属捕集剤は、ポ
リアミン類とエピハロヒドリンとが重縮合した重
縮合ポリアミンの活性水素と置換した少なくとも
1個のカルボジチオ酸基及び/又その塩類を置換
基として結合した構造を有することによつて、従
来の脂肪族ポリジチオカルバミン酸またはその塩
類を含有する金属捕集剤に比べ、少ない添加量で
充分に金属吸着処理を行うことができる。しかも
本発明の金属捕集剤は、金属を捕集して生じたフ
ロツクが大きいため、該フロツクの沈降速度が速
く、このため廃水中の金属を迅速に捕集して除去
することができる効果を有する。
As explained above, the metal scavenger of the present invention has at least one carbodithioic acid group substituted with the active hydrogen of a polycondensed polyamine obtained by polycondensation of a polyamine and an epihalohydrin and/or a salt thereof bonded as a substituent. Due to this structure, metal adsorption treatment can be sufficiently performed with a smaller amount added than conventional metal scavengers containing aliphatic polydithiocarbamic acids or salts thereof. Furthermore, since the metal collecting agent of the present invention has large flocs produced by collecting metals, the sedimentation speed of the flocs is fast, and therefore metals in wastewater can be quickly collected and removed. has.

Claims (1)

【特許請求の範囲】 1 ポリアミン類とエピハロヒドリンとが重縮合
した重縮合ポリアミンの活性水素原子と置換した
少なくとも1個のカルボジチオ酸基及び/又はそ
の塩類を置換基として有することを特徴とする金
属捕集剤。 2 重縮合ポリアミンの窒素原子に結合したN−
置換基としてアルキル基、ヒドロキシアルキル
基、アシル基からなる群より選ばれた少なくとも
1種を有する特許請求の範囲第1項に記載の金属
捕集剤。
[Scope of Claims] 1. A metal trap characterized by having as a substituent at least one carbodithioic acid group and/or a salt thereof substituted with an active hydrogen atom of a polycondensed polyamine obtained by polycondensation of a polyamine and an epihalohydrin. Collection drug. 2 N- bonded to the nitrogen atom of the polycondensed polyamine
The metal scavenger according to claim 1, which has at least one kind selected from the group consisting of an alkyl group, a hydroxyalkyl group, and an acyl group as a substituent.
JP8999885A 1985-04-26 1985-04-26 Metal capturing agent Granted JPS61249590A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP8999885A JPS61249590A (en) 1985-04-26 1985-04-26 Metal capturing agent
US06/853,692 US4670180A (en) 1985-04-26 1986-04-18 Metal scavenger and metal scavenging process
EP86105545A EP0200143B1 (en) 1985-04-26 1986-04-22 Metal scavenger and metal scavenging process
DE8686105545T DE3673222D1 (en) 1985-04-26 1986-04-22 RELEASE AGENTS AND METHOD OF SEPARATION.
AT86105545T ATE55362T1 (en) 1985-04-26 1986-04-22 SEPARATION MEANS AND SEPARATION PROCESSES FOR METALS.
US06/905,977 US4670160A (en) 1985-04-26 1986-09-11 Metal scavenger and metal scavenging process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8999885A JPS61249590A (en) 1985-04-26 1985-04-26 Metal capturing agent

Publications (2)

Publication Number Publication Date
JPS61249590A JPS61249590A (en) 1986-11-06
JPH0464757B2 true JPH0464757B2 (en) 1992-10-15

Family

ID=13986266

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8999885A Granted JPS61249590A (en) 1985-04-26 1985-04-26 Metal capturing agent

Country Status (1)

Country Link
JP (1) JPS61249590A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6490083A (en) * 1987-10-01 1989-04-05 Miyoshi Yushi Kk Fixing of heavy metal contained in soil or in solid waste
JP2001115136A (en) * 1999-10-20 2001-04-24 Miyoshi Oil & Fat Co Ltd Production method of metal collector

Also Published As

Publication number Publication date
JPS61249590A (en) 1986-11-06

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