JP2002188078A - Metal scavenger and method for producing the same - Google Patents

Metal scavenger and method for producing the same

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Publication number
JP2002188078A
JP2002188078A JP2000385719A JP2000385719A JP2002188078A JP 2002188078 A JP2002188078 A JP 2002188078A JP 2000385719 A JP2000385719 A JP 2000385719A JP 2000385719 A JP2000385719 A JP 2000385719A JP 2002188078 A JP2002188078 A JP 2002188078A
Authority
JP
Japan
Prior art keywords
metal
amino group
group
secondary amino
waste
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.)
Pending
Application number
JP2000385719A
Other languages
Japanese (ja)
Inventor
Hisashi Takeuchi
寿 竹内
Katsuyuki Sugiyama
克之 杉山
Kazuo Hosoda
和夫 細田
Masafumi Moriya
雅文 守屋
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.)
Miyoshi Yushi KK
Miyoshi Oil and Fat Co Ltd
Original Assignee
Miyoshi Yushi KK
Miyoshi 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 Miyoshi Yushi KK, Miyoshi Oil and Fat Co Ltd filed Critical Miyoshi Yushi KK
Priority to JP2000385719A priority Critical patent/JP2002188078A/en
Publication of JP2002188078A publication Critical patent/JP2002188078A/en
Pending legal-status Critical Current

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  • Removal Of Specific Substances (AREA)
  • Treatment Of Sludge (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Treating Waste Gases (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a metal scavenger having excellent activities for scavenging lead, zinc or the like, and excellent scavenging activities in an acidic condition and capable of reducing the metal concentration remaining in a waste water or a waste gas, and the metal concentration eluted from a solid waste, and further to provide a method for producing the scavenger. SOLUTION: This metal scavenger contains at least one of a dithio acid group and a salt of the dithio acid group as a metal-scavenging functional group bonded to the nitrogen atom of a secondary amino group of the amino compound formed by condensing amines having at least one primary amino group, with aldehydes, and having no primary amino group and at least one secondary amino group. The method for producing the metal scavenger comprises reacting the amino compound having the secondary amino group with carbon disulfide to introduce the metal-scavenging functional group by substituting the active hydrogen bonded to the nitrogen atom of the secondary amino group.

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、廃水及び焼却灰、
煤塵、鉱滓、汚泥、土壌、シュレッダーダスト等の固体
状廃棄物中に存在する金属を固定化したり、廃ガス中の
金属を捕集除去して、廃水や固体状廃棄物、廃ガスを無
害化することのできる金属捕集剤及びその製造方法に関
する。
The present invention relates to wastewater and incinerated ash,
Immobilize metals present in solid waste such as dust, slag, sludge, soil, shredder dust, and collect and remove metals in waste gas to detoxify wastewater, solid waste, and waste gas. And a method for producing the same.

【0002】[0002]

【従来の技術】工場や研究施設等から排出される廃水及
びゴミ焼却場等で生じる焼却灰や煤塵、鉱山から排出さ
れる鉱滓、廃水処理の際に用いられる活性汚泥、汚染さ
れた土壌等の固体状廃棄物、或いはゴミ焼却場から排出
される排煙の如き廃ガス中には種々の金属が含有されて
おり、水銀、カドミウム、鉛、亜鉛、銅、クロム等の人
体に有害な重金属が多量に含有されている場合がある。
金属を含む固体状廃棄物から溶出した金属による地下
水、河川、海水の汚染や、金属を含む廃ガスによる大気
汚染も大きな社会問題となっている。
2. Description of the Related Art Wastewater discharged from factories and research facilities, incinerated ash and dust generated in garbage incineration plants, slag discharged from mines, activated sludge used in wastewater treatment, contaminated soil, etc. Various metals are contained in solid waste or waste gas such as smoke emitted from a garbage incineration plant, and heavy metals harmful to the human body such as mercury, cadmium, lead, zinc, copper, and chromium are contained. May be present in large amounts.
Pollution of groundwater, rivers and seawater by metals eluted from solid wastes containing metals, and air pollution by waste gases containing metals have also become major social problems.

【0003】このため従来より、廃水、固体状廃棄物、
廃ガス等を放出したり投棄する前に金属捕集剤で処理す
ることが提案されており、金属捕集剤としては水銀やカ
ドミウム等の捕集力に優れたジチオカルバミン酸型の金
属捕集剤が広く利用されている。このようなジチオカル
バミン酸型の金属捕集剤としては、アミン類に二硫化炭
素を反応させ、アミン類のアミノ基の窒素原子にジチオ
酸基やその塩を導入した化合物が広く知られている。
[0003] For this reason, conventionally, wastewater, solid waste,
It has been proposed to treat with a metal scavenger before releasing or discarding waste gas. As the metal scavenger, a dithiocarbamic acid-type metal scavenger with excellent ability to collect mercury, cadmium, etc. Is widely used. As such a dithiocarbamic acid-type metal collector, compounds obtained by reacting carbon disulfide with amines and introducing a dithioic acid group or a salt thereof into a nitrogen atom of an amino group of the amines are widely known.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来の
ジチオカルバミン酸型の金属捕集剤は、水銀やカドミウ
ム等の金属に対する捕集力は優れるものの、鉛や亜鉛等
の金属に対する捕集力が低く、これらを含む場合には充
分な処理が行い難かった。また固体状廃棄物中の金属
は、金属捕集剤によって固定化され、固体状廃棄物中か
ら溶出しないように処理するものであり、金属捕集剤で
処理した固体状廃棄物は、そのまま或いは更にコンクリ
ート等で固めた後に最終処分される。しかしながら従来
より広く用いられているジチオカルバミン酸型の金属捕
集剤は酸性条件下での金属に対する結合力が弱く、この
ため処理後の固体状廃棄物が酸性雨等に晒された場合、
金属捕集剤と金属との結合が外れて固体状廃棄物中から
金属が溶出して環境汚染を生じる虞れがあった。また金
属捕集剤で処理後の廃水や廃ガス中の残存金属濃度や、
金属捕集剤で処理後の固体状廃棄物から溶出する金属濃
度は、現在の基準値よりも更に低減化できればより好ま
しいが、アミン類に二硫化炭素を反応させて得られる従
来のジチオカルバミン酸型の金属捕集剤は、添加量を更
に多くしたとしても、廃水や廃ガス中の残存金属濃度が
金属捕集剤の添加量に比例して低減化できなかったり、
固体状廃棄物中から溶出する金属濃度が金属捕集剤の添
加量に比例して低減化できず、廃棄物を従来よりも更に
安全に処理することは困難であった。
However, conventional dithiocarbamic acid-type metal scavengers have a good ability to collect metals such as mercury and cadmium, but have a low ability to collect metals such as lead and zinc. When these were included, it was difficult to perform sufficient treatment. Further, the metal in the solid waste is fixed by the metal trapping agent and is treated so as not to be eluted from the solid waste, and the solid waste treated with the metal trapping agent is used as it is. After being hardened with concrete, it is finally disposed. However, dithiocarbamic acid-type metal scavengers that have been widely used in the past have a weak binding force to metals under acidic conditions, and therefore, when the solid waste after treatment is exposed to acid rain or the like,
There is a risk that the bond between the metal collecting agent and the metal may be released, and the metal may be eluted from the solid waste to cause environmental pollution. In addition, the concentration of residual metals in wastewater and waste gas after treatment with a metal scavenger,
The metal concentration eluted from the solid waste after treatment with the metal scavenger is more preferable if it can be further reduced from the current standard value, but the conventional dithiocarbamic acid type obtained by reacting amines with carbon disulfide Even if the addition amount is further increased, the concentration of the residual metal in the wastewater or the waste gas cannot be reduced in proportion to the addition amount of the metal collection agent,
The concentration of the metal eluted from the solid waste could not be reduced in proportion to the amount of the metal scavenger added, and it was difficult to treat the waste more safely than before.

【0005】本発明は上記課題を解決するためになされ
たもので、水銀やカドミウム等の金属に対する捕集力は
もとより、鉛や亜鉛等の金属に対する結合力にも優れ、
しかも酸性条件下でも金属に対して強い結合力を有する
とともに、従来のジチオカルバミン酸型金属捕集剤や金
属ジチオカルバミン酸型金属捕集剤に比べ、更に金属捕
集力が高く、廃水や廃ガス中の残存金属濃度や固体状廃
棄物中から溶出する金属濃度を更に低減化することが可
能な、優れた金属捕集剤を提供することを目的とする。
また本発明は上記金属捕集力に優れたジチオカルバミン
酸型金属捕集剤を製造する方法を提供することを目的と
する。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and has an excellent binding force to metals such as lead and zinc as well as a trapping force for metals such as mercury and cadmium.
In addition, it has a strong binding force to metals even under acidic conditions, and has a higher metal-collecting power than conventional dithiocarbamic acid-type metal collectors and metal dithiocarbamic acid-type metal collectors. It is an object of the present invention to provide an excellent metal collecting agent which can further reduce the concentration of residual metal and the concentration of metal eluted from solid waste.
Another object of the present invention is to provide a method for producing a dithiocarbamic acid-type metal trapping agent having excellent metal trapping power.

【0006】[0006]

【課題を解決するための手段】即ち本発明の金属捕集剤
は、少なくとも1個の1級アミノ基を有するアミン類と
アルデヒド類との縮合により形成される、1級アミノ基
を有さず且つ少なくとも1個の2級アミノ基を有するア
ミノ化合物の2級アミノ基の窒素原子に結合した活性水
素と置換して導入された金属捕集性の官能基として、ジ
チオ酸基、ジチオ酸基の塩の少なくとも一方を有するこ
とを特徴とする。また本発明の金属捕集剤の製造方法
は、少なくとも1個の1級アミノ基を有するアミン類と
アルデヒド類とを重縮合させて、1級アミノ基を有さず
且つ少なくとも1個の2級アミノ基を有するアミノ化合
物を得、次いでこのアミノ化合物と二硫化炭素を反応さ
せてアミノ化合物の2級アミノ基の窒素原子に結合した
金属捕集性の官能基として、ジチオ酸基、ジチオ酸基の
塩の少なくとも一方を導入することを特徴とする。
That is, the metal collecting agent of the present invention has no primary amino group formed by condensation of an amine having at least one primary amino group with an aldehyde. And a dithioic acid group or a dithioic acid group as a metal-trapping functional group introduced by substituting an active hydrogen bonded to a nitrogen atom of a secondary amino group of an amino compound having at least one secondary amino group. It has at least one of a salt. Further, the method for producing a metal collecting agent of the present invention comprises the step of polycondensing an amine having at least one primary amino group and an aldehyde to form at least one secondary amino group having no primary amino group. An amino compound having an amino group is obtained, and then the amino compound is reacted with carbon disulfide to form a dithioacid group or a dithioacid group as a metal-trapping functional group bonded to the nitrogen atom of the secondary amino group of the amino compound. Characterized by introducing at least one of the following salts:

【0007】[0007]

【発明の実施の形態】本発明の金属捕集剤は、少なくと
も1個の1級アミノ基を有するアミン類とアルデヒド類
とを縮合させた後、この重縮合物とアルカリの存在下又
は不在下で二硫化炭素を反応させることにより得られ
る。
BEST MODE FOR CARRYING OUT THE INVENTION The metal scavenger of the present invention is obtained by condensing an amine having at least one primary amino group with an aldehyde and then reacting the polycondensate with an alkali in the presence or absence of an alkali. And by reacting carbon disulfide.

【0008】上記少なくとも1個の1級アミノ基を有す
るアミン類としては、例えばモノメチルアミン、モノエ
チルアミン、モノプロピルアミン、モノイソプロピルア
ミン、モノブチルアミン、モノイソブチルアミン等のモ
ノアルキルアミン;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、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等の脂肪族アミ
ン;フェニレンジアミン、o−,m−,p−キシリレン
ジアミン、3,5−ジアミノクロロベンゼン等の芳香族
アミン;1,3−ビス(アミノメチル)シクロヘキサン
等のシクロアルカン系ポリアミン;ポリビニルアミン、
ポリアリルアミン等の不飽和アミンの重合体が挙げられ
る。また、ビニルアミン、アリルアミン等の不飽和アミ
ンと、ジメチルアクリルアミド、スチレン、アクリル酸
メチル、メタクリル酸メチル、アクリル酸、メタクリル
酸、スチレンスルホン酸等及びその塩類等の、不飽和ア
ミンと共重合可能な不飽和結合を有する他のモノマーと
の共重合体も挙げられる。
Examples of the amines having at least one primary amino group include monoalkylamines such as monomethylamine, monoethylamine, monopropylamine, monoisopropylamine, monobutylamine and monoisobutylamine; ethylenediamine, propylenediamine , Butylenediamine, hexamethylenediamine, diethylenetriamine, dipropylenetriamine, dibutylenetriamine, triethylenetetramine, tripropylenetetramine, tributylenetetramine, tetraethylenepentamine, tetrapropylenepentamine, tetrabutylenepentamine, pentaethylenehexamine, imino Aliphatic amines such as bispropylamine, monomethylaminopropylamine and methyliminobispropylamine; phenylenediamine Down, o-, m-, p-xylylenediamine, 3,5-diamino aromatic amines such as chlorobenzene; 1,3-bis cycloalkane polyamines such as (aminomethyl) cyclohexane; polyvinylamine,
Examples include polymers of unsaturated amines such as polyallylamine. In addition, unsaturated amines such as vinylamine and allylamine, and unsaturated amines that can be copolymerized with unsaturated amines such as dimethylacrylamide, styrene, methyl acrylate, methyl methacrylate, acrylic acid, methacrylic acid, styrene sulfonic acid, and salts thereof. Copolymers with other monomers having a saturated bond are also included.

【0009】また上記アミン類と縮合させるアルデヒド
類としては、例えばホルムアルデヒド、グルタルアルデ
ヒド、フタルアルデヒド、イソフタルアルデヒド、テレ
フタルアルデヒド等が挙げられる。
The aldehydes condensed with the above amines include, for example, formaldehyde, glutaraldehyde, phthalaldehyde, isophthalaldehyde, terephthalaldehyde and the like.

【0010】上記アミン類とアルデヒド類とは、アミン
類の1級アミノ基が残らず、且つ2級アミノ基が少なく
とも1個残存するように縮合せしめる必要がある。少な
くとも1個の1級アミノ基を有するアミン類とアルデヒ
ドとを縮合させて、1級アミノ基を有さず且つ少なくと
も1個の2級アミノ基を有するアミノ化合物は、アミン
類とアルデヒド類を20〜150℃で0.5〜10時間
反応を行う。また、必要に応じて脱水等を行うことによ
り得ることができる。1級アミノ基1個当たりに対し、
アルデヒド類0.5分子当量が好ましい。1級アミノ基
を有するアミン類とアルデヒド類とを縮合せしめて得た
アミノ化合物に1級アミノ基が残存していると、このア
ミノ化合物に二硫化炭素を反応せしめて得た反応金属捕
集剤中の不純物含有量が多くなる。また1級アミノ基を
有するアミン類とアルデヒド類とを縮合せしめて得たア
ミノ化合物に2級アミノ基が存在しないと、二硫化炭素
と反応させてジチオ酸基やジチオ酸基の塩を官能基とし
て導入することができなくなる。
The amines and aldehydes need to be condensed so that no primary amino group of the amine remains and at least one secondary amino group remains. An amine having at least one primary amino group and an aldehyde are condensed to form an amino compound having no primary amino group and having at least one secondary amino group. The reaction is carried out at 150150 ° C. for 0.5 to 10 hours. Further, it can be obtained by performing dehydration or the like as necessary. For each primary amino group,
0.5 molecular equivalents of aldehydes are preferred. When a primary amino group remains in an amino compound obtained by condensing an amine having a primary amino group with an aldehyde, a reactive metal trapping agent obtained by reacting carbon disulfide with the amino compound The content of impurities in the inside increases. In addition, if a secondary amino group is not present in an amino compound obtained by condensing an amine having a primary amino group with an aldehyde, the compound is reacted with carbon disulfide to form a dithioacid group or a salt of a dithioacid group. Can not be introduced.

【0011】1級アミノ基を有さず、少なくとも1個の
2級アミノ基を有するアミノ化合物と、二硫化炭素とを
反応させることにより、2級アミノ基の窒素原子に結合
した金属捕集性の官能基としてジチオ酸基を導入するこ
とができ、この反応をアルカリの存在下で行うことによ
り、ジチオ酸基の塩を導入することができる。アルカリ
としては、水酸化ナトリウム、水酸化カリウム、水酸化
カルシウム、水酸化マグネシウム、アンモニア等が挙げ
られる。1級アミノ基を有さず、少なくとも1個の2級
アミノ基を有するアミノ化合物と二硫化炭素は、アルカ
リの存在又は不在下において2級アミノ基1個当たりに
対し、二硫化炭素0.2〜1.0分子当量反応させる。
反応温度は10〜60℃、反応時間は0.5〜20時間
であり、好ましくは10〜40℃、1〜10時間であ
る。
By reacting an amino compound having no primary amino group and having at least one secondary amino group with carbon disulfide, the metal compound bound to the nitrogen atom of the secondary amino group can be collected. A dithioacid group can be introduced as a functional group of the above, and by carrying out this reaction in the presence of an alkali, a salt of the dithioacid group can be introduced. Examples of the alkali include sodium hydroxide, potassium hydroxide, calcium hydroxide, magnesium hydroxide, ammonia and the like. An amino compound having no primary amino group and having at least one secondary amino group and carbon disulfide are present in an amount of 0.2 carbon disulfide per secondary amino group in the presence or absence of an alkali.反 応 1.0 molecular equivalent reaction.
The reaction temperature is 10 to 60 ° C, and the reaction time is 0.5 to 20 hours, preferably 10 to 40 ° C and 1 to 10 hours.

【0012】本発明の金属捕集剤が処理対象とする廃棄
物としては、廃水や、例えばゴミ焼却場において生成す
る焼却灰や煤塵、鉱滓、汚泥、土壌、シュレッダーダス
ト等の固体状廃棄物、ゴミ焼却場においてゴミを焼却し
た際に生じる廃ガス等が挙げられる。
Examples of the waste to be treated by the metal collecting agent of the present invention include wastewater and solid waste such as incinerated ash, dust, slag, sludge, soil, and shredder dust generated in a garbage incineration plant. Waste gas generated when garbage is incinerated in a garbage incineration plant is exemplified.

【0013】廃水を処理する場合、処理しようとする廃
水に本発明の金属捕集剤をそのまま、又は水に溶解ない
し分散させた状態で添加し、金属捕集剤が金属を捕集し
て生成したフロックを沈殿除去する方法が採用される。
また集塵された焼却灰や煤塵、鉱滓、汚泥、土壌、シュ
レッダーダスト等の固体状廃棄物を処理する場合、これ
らの廃棄物に本発明の金属捕集剤を液状又は粉末状のま
ま添加したり、水溶液ないし分散液として添加したり噴
霧し、混練する等の方法が採用され、これにより固体状
廃棄物中の金属は本発明の金属捕集剤と反応して固定化
される。また煤塵や廃ガスの場合、焼却炉における焼却
工程中、例えば煙路に本発明の金属捕集剤の溶液等を噴
霧する等によって、本発明の捕集剤と煤塵とを接触さ
せ、処理後の煤塵をバグフィルターで集塵する等の方法
を採用することができる。廃ガスと煤塵とが存在する煙
路内に本発明の金属捕集剤を噴霧する等の方法で供給す
ると、廃ガス中に含まれる金属(主として水銀等のガス
化し易い金属)を捕集して廃ガス中から分離できるとと
もに、煤塵中に含まれる金属の固定化も行うことができ
る。
When treating wastewater, the metal-collecting agent of the present invention is added to the wastewater to be treated as it is or in a state of being dissolved or dispersed in water. A method of removing precipitated floc by precipitation is employed.
When treating solid waste such as collected incineration ash, dust, slag, sludge, soil, shredder dust, etc., the metal collecting agent of the present invention is added to these wastes in liquid or powder form. For example, a method of adding, spraying and kneading as an aqueous solution or dispersion, or kneading is adopted, whereby the metal in the solid waste reacts with the metal collecting agent of the present invention and is fixed. In the case of dust and waste gas, during the incineration process in an incinerator, for example, by spraying a solution of the metal-collecting agent of the present invention on the flue, etc. For example, a method of collecting soot and dust with a bag filter can be adopted. When the metal collecting agent of the present invention is supplied to the flue where waste gas and dust are present by spraying or the like, the metal contained in the waste gas (mainly a metal which is easily gasified such as mercury) is collected. And separate from the waste gas, and fix the metal contained in the dust.

【0014】本発明の金属捕集剤により廃水、固体状廃
棄物、廃ガス等を処理する際に、本発明の所期の目的を
阻害しない範囲において、従来の金属捕集剤を併用して
も良い。尚、金属捕集剤の添加量は、固体状廃棄物等に
含まれる金属等の量によっても異なるが、一般に、本発
明の金属捕集剤の添加量は、廃水の場合0.5〜100
mg/l、固体状廃棄物の場合には0.1〜50重量
%、廃ガスの場合には0.5〜2000mg/Nm3
度が好ましい。
When treating the waste water, solid waste, waste gas and the like with the metal collecting agent of the present invention, a conventional metal collecting agent may be used in combination within a range not to impair the intended purpose of the present invention. Is also good. The amount of the metal collecting agent varies depending on the amount of the metal contained in the solid waste or the like, but generally, the amount of the metal collecting agent of the present invention is 0.5 to 100 in the case of wastewater.
mg / l, preferably 0.1 to 50% by weight for solid waste, and about 0.5 to 2000 mg / Nm 3 for waste gas.

【0015】本発明の金属捕集剤によって処理した廃水
は、フロックを分離除去後、河川に放流することができ
る。また焼却灰や煤塵、鉱滓、土壌、シュレッダーダス
ト、汚泥等の固体状廃棄物や、廃ガス処理後の煤塵等の
廃棄物は、必要に応じて処理後の廃棄物をセメントで固
めて投棄する等の最終処分を行うことができる。本発明
の金属捕集剤で処理後の廃棄物をセメント等で固めて最
終処分する場合、従来の金属捕集剤によって処理した場
合に比べ、セメントの使用量が少ない場合でも、廃棄物
中の金属が再溶出して二次汚染を生じる等の虞れが少な
い。
The wastewater treated with the metal trapping agent of the present invention can be discharged to a river after separating and removing flocs. Solid waste such as incineration ash, dust, slag, soil, shredder dust, and sludge, and waste such as dust after waste gas treatment are solidified and discarded as necessary. Final disposal such as can be performed. When the waste treated with the metal trapping agent of the present invention is solidified with cement or the like and finally disposed of, even if the amount of cement used is small compared to the case where the waste is treated with the conventional metal trapping agent, the waste There is little fear that the metal is re-eluted to cause secondary contamination.

【0016】[0016]

【実施例】以下、実施例を挙げて本発明を更に詳細に説
明する。尚、以下の実施例、比較例で用いた金属捕集剤
は以下の通りである。
EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples. The metal scavengers used in the following examples and comparative examples are as follows.

【0017】金属捕集剤1(本発明品):モノエチルア
ミン1.0モルおよびテトラエチレンペンタミン0.5
モルの混合物に対して、フタルアルデヒド1.0モルを
50℃で7時間滴下した後、減圧下で脱水することによ
り反応させて得られたアミノ化合物(2級アミノ基の割
合は1分子当たり7.0個)1分子に対し、二硫化炭素
5.0モルを水酸化ナトリウムの存在下で反応させて得
た化合物(1分子当たりのジチオ酸基の数は5.0個、
2級アミノ基の残存量は2個)。
Metal collecting agent 1 (product of the present invention): 1.0 mol of monoethylamine and 0.5 of tetraethylenepentamine
An amino compound obtained by dropping 1.0 mol of phthalaldehyde at 50 ° C. for 7 hours to the mixture of the above and then dehydrating under reduced pressure to obtain an amino compound (the ratio of secondary amino groups is 7 per molecule) A compound obtained by reacting 5.0 moles of carbon disulfide with one molecule in the presence of sodium hydroxide (the number of dithioic acid groups per molecule is 5.0,
The remaining amount of secondary amino groups is 2).

【0018】金属捕集剤2(本発明品):ジプロピレン
トリアミン1モル当たり、グルタルアルデヒド1モルを
30℃で3時間滴下した後、減圧下で脱水することによ
り反応させて得られたアミノ化合物(2級アミノ基の割
合は1ユニット当たり3.0個)1ユニットに対し、二
硫化炭素2.0モルを水酸化カリウムの存在下で反応さ
せて得た化合物(1ユニット当たりのジチオ酸基の数は
2.0個、2級アミノ基の残存量は1.0個)。上記1
ユニットはアミン類とアルデヒド類から得られた繰り返
し構造を持つアミノ化合物の1繰り返し構造である。
Metal collecting agent 2 (product of the present invention): 1 mol of glutaraldehyde per 1 mol of dipropylenetriamine
After dropping at 30 ° C. for 3 hours, the mixture was dehydrated under reduced pressure, and reacted by dehydration under reduced pressure. A compound obtained by reacting 0 mol in the presence of potassium hydroxide (the number of dithioic acid groups per unit is 2.0, and the remaining amount of secondary amino groups is 1.0). 1 above
The unit is a single repeating structure of an amino compound having a repeating structure obtained from amines and aldehydes.

【0019】金属捕集剤3(本発明品):p-キシリレン
ジアミン0.5モルおよびトリエチレンテトラミン0.
5モルの混合物に対して、ホルムアルデヒド1.0モル
を70℃で6時間滴下した後、減圧下で脱水することに
より反応させて得られたアミノ化合物(2級アミノ基の
割合は1ユニット当たり6.0個)1ユニットに対し、
二硫化炭素5.0モルを水酸化ナトリウムの存在下で反
応させて得た化合物(1ユニット当たりのジチオ酸基の
数は5.0個、2級アミノ基の残存量は1.0個)。
Metal collecting agent 3 (product of the present invention): 0.5 mol of p-xylylenediamine and 0.5 mol of triethylenetetramine
To a 5 mol mixture, 1.0 mol of formaldehyde was added dropwise at 70 ° C. for 6 hours, followed by dehydration under reduced pressure to obtain an amino compound (the ratio of secondary amino groups was 6 mol / unit). .0) per unit
Compound obtained by reacting 5.0 moles of carbon disulfide in the presence of sodium hydroxide (the number of dithioic acid groups per unit is 5.0, the remaining amount of secondary amino groups is 1.0) .

【0020】金属捕集剤4(本発明品):テトラエチレ
ンペンタミン1モル当たり、グルタルアルデヒド1.0
モルを50℃で4時間滴下した後、減圧下で脱水するこ
とにより反応させて得られたアミノ化合物(2級アミノ
基の割合は1ユニット当たり5.0個)1ユニットに対
し、二硫化炭素3.0モルを水酸化ナトリウムの存在下
で反応させて得た化合物(1ユニット当たりのジチオ酸
基の数は3.0個、2級アミノ基の残存量は2.0個)。
Metal collecting agent 4 (product of the present invention): glutaraldehyde 1.0 per mole of tetraethylenepentamine
Mol was added dropwise at 50 ° C. for 4 hours, and then dehydrated under reduced pressure to react. One unit of an amino compound (the ratio of secondary amino groups was 5.0 per unit) was added to carbon disulfide. A compound obtained by reacting 3.0 moles in the presence of sodium hydroxide (the number of dithioic acid groups per unit is 3.0, and the remaining amount of secondary amino groups is 2.0).

【0021】金属捕集剤5(本発明品):ジエチレント
リアミン1モル当たり、イソフタルアルデヒド1.0モ
ルを90℃で3時間滴下した後、減圧下で脱水すること
により反応させて得られたアミノ化合物(2級アミノ基
の割合は1ユニット当たり3.0個)1ユニットに対
し、二硫化炭素2.5モルを水酸化カリウムの存在下で
反応させて得た化合物(1ユニット当たりのジチオ酸基
の数は2.5個、2級アミノ基の残存量は0.5個)。
Metal collecting agent 5 (product of the present invention): An amino compound obtained by dropping 1.0 mol of isophthalaldehyde per 90 mol of diethylenetriamine at 90 ° C. for 3 hours and then dehydrating under reduced pressure to react. A compound obtained by reacting 2.5 mol of carbon disulfide with 1 unit in the presence of potassium hydroxide (the ratio of dithioic acid groups per unit is 3.0). Is 2.5, and the remaining amount of secondary amino groups is 0.5).

【0022】金属捕集剤6(従来品):エチレンジアミ
ン1モル当たり、二硫化炭素2モルを水酸化ナトリウム
の存在下で反応させエチレンジアミンの窒素原子に、ジ
チオ酸基のナトリウム塩2個を導入した化合物。
Metal collecting agent 6 (conventional product): 2 moles of carbon disulfide per mole of ethylenediamine were reacted in the presence of sodium hydroxide to introduce two sodium salts of dithioic acid groups into the nitrogen atom of ethylenediamine. Compound.

【0023】実施例1〜3、比較例1 亜鉛830mg/kg、鉛1460mg/kg、水銀4
70mg/kgを含む煤塵100g当たりに対し、表1
に示す金属捕集剤の水溶液(又は分散液)を、金属捕集
剤の添加量が4g(固形分換算)となるように添加し、
50〜80℃で20分間混練した。各捕集剤で処理済の
煤塵と未処理の煤塵各50gを、pH=6.0とpH=
3.5の水500ml中で常温にて6時間振とうし、水
中に溶出した金属濃度を測定した。水中に溶出した金属
の濃度は原子吸光分析法により測定した。結果を表1に
示す。
Examples 1-3, Comparative Example 1 830 mg / kg of zinc, 1460 mg / kg of lead, 4 mercury
Table 1 for 100 g of dust containing 70 mg / kg
An aqueous solution (or dispersion) of the metal collecting agent shown in (1) is added so that the addition amount of the metal collecting agent becomes 4 g (in terms of solid content),
The mixture was kneaded at 50 to 80 ° C for 20 minutes. 50 g of each of the dust treated and the untreated dust treated with each trapping agent were subjected to pH = 6.0 and pH =
The mixture was shaken in 500 ml of 3.5 water at room temperature for 6 hours, and the concentration of the metal eluted in the water was measured. The concentration of the metal eluted in the water was measured by atomic absorption spectrometry. Table 1 shows the results.

【0024】[0024]

【表1】 [Table 1]

【0025】実施例4〜6、比較例2 鉛520mg/kg、亜鉛1730mg/kg、カドミ
ウム180mg/kgを含有する鉱滓100g当たりに
対し、表2に示す金属捕集剤の水溶液(又は分散液)を
添加量が3.5g(固形分換算)となるように添加し、
80〜120℃で10分間混練した。各捕集剤で処理済
の鉱滓と未処理の鉱滓各50gを用い、実施例1〜3と
同様にして水中に溶出した金属濃度を測定した。結果を
表2に示す。
Examples 4 to 6, Comparative Example 2 An aqueous solution (or dispersion) of a metal collector shown in Table 2 per 100 g of slag containing 520 mg / kg of lead, 1,730 mg / kg of zinc, and 180 mg / kg of cadmium. Is added so that the added amount becomes 3.5 g (in terms of solid content),
The mixture was kneaded at 80 to 120 ° C for 10 minutes. Using 50 g of each of the slag treated and the untreated slag with each collector, the metal concentration eluted in water was measured in the same manner as in Examples 1 to 3. Table 2 shows the results.

【0026】[0026]

【表2】 [Table 2]

【0027】実施例7〜9、比較例3 鉛28mg/kg、水銀11mg/kg、カドミウム5
22mg/kgを含有する土壌100g当たりに対し、
表3に示す金属捕集剤の水溶液(又は分散液)を添加量
が2g(固形分換算)となるように添加し、100〜1
50℃で30分間混練した。各捕集剤で処理済の土壌と
未処理の土壌各50gを用い、実施例1〜3と同様にし
て水中に溶出した金属濃度を測定した。結果を表3に示
す。
Examples 7 to 9, Comparative Example 3 28 mg / kg of lead, 11 mg / kg of mercury, 5 cadmium
For 100 g of soil containing 22 mg / kg,
An aqueous solution (or dispersion) of the metal collecting agent shown in Table 3 was added so that the addition amount became 2 g (in terms of solid content), and 100 to 1
Kneaded at 50 ° C. for 30 minutes. Using 50 g of each of soil treated with each collector and untreated soil, the metal concentration eluted in water was measured in the same manner as in Examples 1 to 3. Table 3 shows the results.

【0028】[0028]

【表3】 [Table 3]

【0029】実施例10〜12、比較例4 水銀2mg/Nm3 、鉛5mg/Nm3、ダスト3g/
Nm3 を含むゴミ焼却場の廃ガス(16000Nm3
時間、250℃)に、表4に示す金属捕集剤の水溶液
を、金属捕集剤が固型分として300mg/Nm3 の割
合で供給されるように煙道中に噴霧し、廃ガス中の水銀
と金属捕集剤とを反応させた後、バグフィルターにて集
塵した。バグフィルター通過後の廃ガス中に残存する水
銀の濃度を測定した結果を表4に示す。また、バグフィ
ルターにて集塵された煤塵50gを用い、実施例1〜3
と同様にして水中に溶出した金属濃度を測定した。結果
を表4に示す。
[0029] Examples 10 to 12, Comparative Example 4 mercury 2mg / Nm 3, lead 5mg / Nm 3, dust 3g /
Waste gas from garbage incineration plants containing Nm 3 (16000 Nm 3 /
Time, 250 ° C.), an aqueous solution of the metal trapping agent shown in Table 4 was sprayed into the flue so that the metal trapping agent was supplied as a solid component at a rate of 300 mg / Nm 3 , and the waste gas was discharged. After reacting mercury with the metal collector, dust was collected with a bag filter. Table 4 shows the results of measuring the concentration of mercury remaining in the waste gas after passing through the bag filter. Further, using 50 g of dust collected by a bag filter, Examples 1 to 3 were used.
The concentration of the metal eluted in water was measured in the same manner as described above. Table 4 shows the results.

【0030】[0030]

【表4】 [Table 4]

【0031】実施例13〜16、比較例5 鉛32mg/kg、水銀7mg/kg、亜鉛8mg/k
gを含有する廃水1リットル当たりに対し、表5に示す
金属捕集剤の水溶液(又は分散液)を添加量が7mg
(固形分換算)となるように添加して20℃で20分間
撹拌し、次いで静置した後、生成したフロックを分離し
て除去した。フロック除去後の廃水中の残存金属濃度を
測定した結果を表5に示す。
Examples 13 to 16, Comparative Example 5 32 mg / kg of lead, 7 mg / kg of mercury, 8 mg / k of zinc
g of wastewater containing 7 g of an aqueous solution (or dispersion) of the metal collecting agent shown in Table 5 in an amount of 7 mg per liter of the wastewater.
(In terms of solid content), the mixture was stirred at 20 ° C. for 20 minutes, and then allowed to stand. Then, generated flocs were separated and removed. Table 5 shows the results of measuring the residual metal concentration in the wastewater after removing the flocs.

【0032】[0032]

【表5】 [Table 5]

【0033】実施例17、比較例6 実施例1〜3で用いた煤塵100g当たり、表6に示す
金属捕集剤を異なる量添加し(固形物換算量で1g、2
g、3g、4g、5g)、処理後の煤塵からの水銀の溶
出量を実施例1〜3と同様にして測定し(但し、pH=
6の水中への溶出量のみ)、金属捕集剤の添加量と、水
銀の固定化能との関係を調べた。結果を表6にあわせて
示す。
Example 17, Comparative Example 6 Per 100 g of the dust used in Examples 1 to 3, different amounts of the metal collector shown in Table 6 were added (1 g in terms of solid matter, 2 g).
g, 3 g, 4 g, 5 g), and the amount of mercury eluted from the treated dust was measured in the same manner as in Examples 1 to 3 (provided that pH =
No. 6 only eluted into water), the relationship between the amount of metal scavenger added and the ability to immobilize mercury was examined. The results are shown in Table 6.

【0034】[0034]

【表6】 [Table 6]

【0035】[0035]

【発明の効果】以上説明したように本発明の金属捕集剤
は、従来のジチオカルバミン酸型金属捕集剤と同様に水
銀やカドミウムに対して優れた捕集力を発揮するととも
に、鉛や亜鉛に対しても優れた捕集力を有するため、本
発明の金属捕集剤によれば、鉛や亜鉛を含む廃水、固体
状廃棄物、廃ガスを効果的に処理することができる。ま
た本発明の金属捕集剤は、酸性条件下においても金属に
対して優れた結合力を有するため、本発明の金属捕集剤
で処理した固体状廃棄物は、酸性雨等に晒された場合で
も、固体状廃棄物中から金属が再溶出する虞れがない。
また本発明の金属捕集剤は、通常の方法で得たジチオカ
ルバミン酸型の金属捕集剤に比べ、廃水や廃ガス中の残
存金属濃度や、固体状廃棄物中からの溶出金属濃度を更
に低減化することができ、廃水や固体状廃棄物等の廃棄
物を更に安全に処理することができる。また本発明の方
法によれば、上記優れた金属捕集効果を有する金属捕集
剤を効果的に得ることができる。
As described above, the metal trapping agent of the present invention exhibits excellent trapping power for mercury and cadmium as well as the conventional dithiocarbamic acid type metal trapping agent, Therefore, according to the metal collecting agent of the present invention, wastewater containing lead and zinc, solid waste, and waste gas can be effectively treated. Further, since the metal trapping agent of the present invention has an excellent binding force to metals even under acidic conditions, solid waste treated with the metal trapping agent of the present invention was exposed to acid rain and the like. Even in such a case, there is no fear that the metal is eluted again from the solid waste.
Further, the metal-collecting agent of the present invention further reduces the concentration of residual metal in wastewater or waste gas and the concentration of metal eluted from solid waste compared to a dithiocarbamic acid-type metal-collecting agent obtained by an ordinary method. The waste can be reduced, and waste such as wastewater and solid waste can be more safely treated. Further, according to the method of the present invention, a metal collecting agent having the above-mentioned excellent metal collecting effect can be effectively obtained.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B09C 1/08 B09B 3/00 304K B09B 3/00 304G C02F 1/62 ZAB 304J (72)発明者 細田 和夫 東京都葛飾区堀切4丁目66番1号 ミヨシ 油脂株式会社内 (72)発明者 守屋 雅文 東京都葛飾区堀切4丁目66番1号 ミヨシ 油脂株式会社内 Fターム(参考) 4D002 AA29 AA31 AA40 AC04 AC10 BA03 BA14 CA01 DA61 EA05 HA01 4D004 AA28 AA36 AA37 AA41 AA43 AB03 AC07 CA34 CB21 CB42 CC06 4D038 AA08 AB63 AB69 AB73 AB74 BB18 4D059 BF20 DB08 DB21 4H006 AA01 AA03 AB99 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B09C 1/08 B09B 3/00 304K B09B 3/00 304G C02F 1/62 ZAB 304J (72) Inventor Kazuo Hosoda 4-66, Horikiri, Katsushika-ku, Tokyo Miyoshi Oil & Fat Co., Ltd. (72) Inventor Masafumi Moriya 4-66-1, Horikiri, Katsushika-ku, Tokyo Miyoshi Oil & Fat Co., Ltd. F-term (reference) 4D002 AA29 AA31 AA40 AC04 AC10 BA03 BA14 CA01 DA61 EA05 HA01 4D004 AA28 AA36 AA37 AA41 AA43 AB03 AC07 CA34 CB21 CB42 CC06 4D038 AA08 AB63 AB69 AB73 AB74 BB18 4D059 BF20 DB08 DB21 4H006 AA01 AA03 AB99

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 少なくとも1個の1級アミノ基を有する
アミン類とアルデヒド類との縮合により形成される、1
級アミノ基を有さず且つ少なくとも1個の2級アミノ基
を有するアミノ化合物の2級アミノ基の窒素原子に結合
した活性水素と置換して導入された金属捕集性の官能基
として、ジチオ酸基、ジチオ酸基の塩の少なくとも一方
を有することを特徴とする金属捕集剤。
1. A compound formed by condensation of an amine having at least one primary amino group with an aldehyde.
The amino compound having no secondary amino group and having at least one secondary amino group has a metal-capturing functional group introduced by substituting with active hydrogen bonded to the nitrogen atom of the secondary amino group. A metal collector having at least one of an acid group and a salt of a dithioacid group.
【請求項2】 少なくとも1個の1級アミノ基を有する
アミン類とアルデヒド類とを重縮合させて、1級アミノ
基を有さず且つ少なくとも1個の2級アミノ基を有する
アミノ化合物を得、次いでこのアミノ化合物と二硫化炭
素を反応させて、アミノ化合物の2級アミノ基の窒素原
子に結合した金属捕集性の官能基として、ジチオ酸基、
ジチオ酸基の塩の少なくとも一方を導入することを特徴
とする金属捕集剤の製造方法。
2. An amino compound having at least one primary amino group and an aldehyde is polycondensed to obtain an amino compound having no primary amino group and having at least one secondary amino group. Then, the amino compound is reacted with carbon disulfide to form a dithioic acid group as a metal-trapping functional group bonded to the nitrogen atom of the secondary amino group of the amino compound.
A method for producing a metal collecting agent, comprising introducing at least one of salts of a dithioacid group.
JP2000385719A 2000-12-19 2000-12-19 Metal scavenger and method for producing the same Pending JP2002188078A (en)

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Country Link
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4951187A (en) * 1972-09-18 1974-05-17
JPS6048139A (en) * 1983-08-26 1985-03-15 Unitika Ltd Heavy metal adsorbent, manufacture thereof and adsorption treatment

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4951187A (en) * 1972-09-18 1974-05-17
JPS6048139A (en) * 1983-08-26 1985-03-15 Unitika Ltd Heavy metal adsorbent, manufacture thereof and adsorption treatment

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