JPH0871597A - Separation of harmful metal in sludge - Google Patents
Separation of harmful metal in sludgeInfo
- Publication number
- JPH0871597A JPH0871597A JP6239573A JP23957394A JPH0871597A JP H0871597 A JPH0871597 A JP H0871597A JP 6239573 A JP6239573 A JP 6239573A JP 23957394 A JP23957394 A JP 23957394A JP H0871597 A JPH0871597 A JP H0871597A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- harmful
- iron
- ferrite
- separated
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、下水汚泥等に含まれ
る人体等に有害な金属の分離方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for separating metals contained in sewage sludge and the like, which are harmful to the human body and the like.
【0002】[0002]
【従来の技術】従来、下水汚泥等に含まれている水銀や
カドニウム等が人体に有害なことはよく知られており、
大量に発生する下水汚泥は肥料分を含み農作物に有効で
あることが知られていながら使用できないのが現状であ
る。そして、この有害な金属を汚泥から分離する手段と
しては、その金属を含む汚泥を固結して有害金属が溶出
しないようにして投棄している。2. Description of the Related Art It is well known that mercury and cadmium contained in sewage sludge are harmful to humans.
The large amount of sewage sludge, which contains fertilizer and is known to be effective for agricultural crops, cannot be used at present. Then, as a means for separating the harmful metal from the sludge, the sludge containing the metal is solidified and discarded so that the harmful metal is not eluted.
【0003】[0003]
【発明が解決しようとする課題】上述のような有害金属
を含む汚泥は、その発生量が年々増加して、固結するに
も大量の固結材を要し、また、投棄場所にも限界があ
る。さらに、コンポストして利用できるようにする点に
おいても、上述のように有害金属の処理上に問題を残し
ている。The amount of sludge containing harmful metals as described above increases year by year, requires a large amount of solidifying material to solidify, and has a limit to the dumping site. There is. Further, as described above, there is a problem in processing harmful metals in that it can be used by composting.
【0004】[0004]
【課題を解決するための手段】この発明は、上述のよう
な課題を解決し得るものであって、その要旨とするとこ
ろは、カドニウム等の有害金属を含む汚泥に硫酸等を加
えてPHを低下させて有害金属をイオン化して溶出さ
せ、次いで、この汚泥を正負の極共に鉄の電極で電解し
たのち、この電解液を同じ電解槽で極性変換して電解
し、その電解液を磁気分離器で処理するようにしたもの
である。The present invention can solve the above-mentioned problems, and the gist of the present invention is to add sulfuric acid or the like to sludge containing harmful metals such as cadmium to remove PH. After reducing and ionizing the harmful metal to elute it, and then electrolyzing this sludge with iron electrodes with both positive and negative poles, this electrolytic solution is polarity-converted in the same electrolytic cell and electrolyzed, and the electrolytic solution is magnetically separated. It is designed to be processed by a vessel.
【0005】[0005]
【作用】すなわち、この発明は、有害金属を含む汚泥を
酸処理して、有害金属を液中に溶出させ、その汚泥を鉄
電極で電解することによって、電極面に有害金属と鉄の
化合物(フエライト)を析出させ、このフエライトを極
性変換をすることによって電極から剥離し、この剥離し
た鉄の化合物を磁力を用いて他の夾雑物から分離するも
のである。以下図面に基づいてこの発明を具体的に説明
する。That is, according to the present invention, sludge containing harmful metals is treated with an acid to dissolve the harmful metals in the liquid, and the sludge is electrolyzed by an iron electrode, whereby a compound of the harmful metal and iron ( Ferrite) is deposited, and the ferrite is peeled from the electrode by changing the polarity, and the peeled iron compound is separated from other contaminants by using magnetic force. The present invention will be specifically described below with reference to the drawings.
【0006】[0006]
【実施例】図1は、この発明に係る有害金属の処離方法
のブロック図であり、符号1は汚泥槽、2は有害金属の
溶出槽、3は電解槽、4は磁気分離槽、5は分離フエラ
イト槽、6は処理済の汚泥槽、7は添加する硫酸槽を示
すものであり、図例では PHを低下させるのに硫酸を用
いている。1 is a block diagram of a method for removing harmful metals according to the present invention. Reference numeral 1 is a sludge tank, 2 is a harmful metal elution tank, 3 is an electrolytic tank, 4 is a magnetic separation tank, 5 Indicates a separation ferrite tank, 6 indicates a treated sludge tank, and 7 indicates a sulfuric acid tank to be added. In the illustrated example, sulfuric acid is used to reduce PH.
【0007】図2は、上記電解槽3の模式斜面図であっ
て、電極板3aは、陽極、陰極共に鉄で構成してある。
符号8は極性の切換装置、9は電源、10は電解用汚泥
の供給口、11は電解処理済汚泥の取出口を示すもので
ある。FIG. 2 is a schematic perspective view of the electrolytic cell 3 in which the electrode plate 3a is made of iron for both the anode and the cathode.
Reference numeral 8 is a polarity switching device, 9 is a power source, 10 is an electrolysis sludge supply port, and 11 is an electrolysis-treated sludge removal port.
【0008】次に、上述装置を用いて汚泥から有害金属
を除去する方法について説明する。まず、溶出槽2に導
入した汚泥に、硫酸槽7の硫酸を添加して汚泥のPHを
低下させ、含まれる有害金属類をイオン化して溶出させ
る。Next, a method for removing harmful metals from sludge using the above-mentioned apparatus will be described. First, the sulfuric acid in the sulfuric acid tank 7 is added to the sludge introduced into the elution tank 2 to reduce the pH of the sludge, and the harmful metals contained therein are ionized and eluted.
【0009】そして、この処理汚泥を電解槽3に導入し
て、通電し、電解する。斯くすることによって、陽極よ
り鉄イオンが溶出し、その一部が水和反応で水酸化鉄を
生成し、汚泥のPHを上昇させる。一方、鉄イオンの他
の一部は、有害金属イオンと共に陰極へ移動し、電解で
発生した酸素で酸化され、有害金属イオンを吸着しなが
ら、酸化成長するフエライト化反応を行ないフエライト
(鉄化合物)を形成する。Then, the treated sludge is introduced into the electrolytic cell 3 and is energized for electrolysis. By doing so, iron ions are eluted from the anode, part of which produces iron hydroxide by the hydration reaction, and raises the pH of sludge. On the other hand, other part of iron ions moves to the cathode together with harmful metal ions, is oxidized by oxygen generated by electrolysis, and adsorbs the harmful metal ions, and performs ferrite (iron compound) which undergoes oxidative growth ferrite reaction. To form.
【0010】そして、形成されたフエライトは、陰極に
付着し、汚泥から分離される。陰極に付着したフエライ
トは再溶解しないので、電極の極変換をすることによっ
て、極板(陽極に変換されている)から剥離する。The formed ferrite adheres to the cathode and is separated from the sludge. Since the ferrite attached to the cathode does not redissolve, it is peeled from the electrode plate (which has been converted to the anode) by changing the electrode pole.
【0011】このようにして、剥離されたフエライトは
磁性体であるので、次段の磁気分離手段によって汚泥中
から分離することができる。すなわち、この発明に係る
方法は、汚泥中に散在する有害金属を鉄電極で以て電解
することによって不溶性のフエライトに変え、電極の極
変換することによって電極から剥離し、磁石で回収する
ようにしたものであり、その回収操作は簡単で、且つ、
確実に有害金属のみを汚泥から分離できる。In this way, since the peeled ferrite is a magnetic substance, it can be separated from the sludge by the magnetic separation means in the next stage. That is, the method according to the present invention converts harmful metal scattered in sludge into insoluble ferrite by electrolyzing with an iron electrode, peels from the electrode by converting the electrode pole, and collects with a magnet. The collection operation is simple, and
Only harmful metals can be reliably separated from sludge.
【0012】このようにして、有害金属が分離除去され
た汚泥は、有機物質を含んでいて農業等に使用して安全
なるは勿論のこと、電解によって生じた水酸化鉄が作用
して改質されているので、脱水性が向上しており、処理
後段における脱水作業を容易にすることができるもので
ある。[0012] In this way, the sludge from which harmful metals have been separated and removed is not only safe as it contains organic substances and is used in agriculture, but it is also modified by the action of iron hydroxide produced by electrolysis. Therefore, the dehydration property is improved and the dehydration work in the latter stage of the treatment can be facilitated.
【0013】以上のような処理操作をZnを含む汚泥に
ついて試験操作した結果は、次の通りであった。1L当
り8.7mgのZnを含む汚泥を上述手段によって処理
したところ、処理汚泥中に含まれるZn量は、2.22
mgであった。すなわち、除去できたZn量は6.48
mgであり、原汚泥に含まれていたZn量の74.5%
を分離して除去することができた。The results of a test operation on the sludge containing Zn by the above treatment operation were as follows. When sludge containing 8.7 mg of Zn per liter was treated by the above means, the amount of Zn contained in the treated sludge was 2.22.
It was mg. That is, the amount of removed Zn was 6.48.
mg, 74.5% of the amount of Zn contained in the original sludge
Could be separated and removed.
【0014】[0014]
【発明の効果】このように、この発明は、従来分離除去
することが困難であった下水汚泥等に含まれる有害金属
を簡単且つ、確実に除去することができ、農業用のコン
ポスト等として再利用できるようにするとともに、この
発明によって処理した汚泥は、事後の脱水処理性も向上
するものであり、従来のこの種汚泥の処理、処分上の課
題を完全に解決し得たものである。As described above, the present invention can easily and reliably remove harmful metals contained in sewage sludge and the like, which were conventionally difficult to separate and remove, and can be reused as agricultural compost or the like. In addition to being made available, the sludge treated according to the present invention has an improved post-process dehydration treatment property, and can completely solve the conventional problems in treating and disposing of this type of sludge.
【図1】この発明に係る汚泥の処理方法の工程を示すブ
ロック図である。FIG. 1 is a block diagram showing steps of a sludge treatment method according to the present invention.
【図2】この発明に係る汚泥の処理に用いる電解装置の
斜面図である。FIG. 2 is a perspective view of an electrolysis device used for treating sludge according to the present invention.
3 電解槽 3a 電極 3 Electrolyzer 3a Electrode
Claims (1)
Hを低下させて有害金属をイオン化して溶出させ、次い
で、この汚泥を正負の電極3aが共に鉄の電極3aで電
解したのち、この電解液を同じ電解槽3で極性変換して
電解し、その電解液を磁気分離器で処理することを特長
とする汚泥中の有害金属の分離方法。1. Sulfuric acid is added to sludge containing harmful metals to obtain P.
H is lowered to ionize and elute the harmful metal, and then the sludge is electrolyzed with the positive and negative electrodes 3a together with the iron electrode 3a, and then the electrolytic solution is subjected to polarity conversion in the same electrolytic cell 3 to be electrolyzed, A method for separating harmful metals in sludge, which is characterized by treating the electrolytic solution with a magnetic separator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06239573A JP3118793B2 (en) | 1994-09-06 | 1994-09-06 | Separation method of toxic metals in sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP06239573A JP3118793B2 (en) | 1994-09-06 | 1994-09-06 | Separation method of toxic metals in sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0871597A true JPH0871597A (en) | 1996-03-19 |
JP3118793B2 JP3118793B2 (en) | 2000-12-18 |
Family
ID=17046812
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP06239573A Expired - Fee Related JP3118793B2 (en) | 1994-09-06 | 1994-09-06 | Separation method of toxic metals in sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3118793B2 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100369711B1 (en) * | 2000-09-15 | 2003-01-30 | 광주과학기술원 | Electrochemical process for removal of toxic heavy metals in sludges |
WO2013063644A2 (en) * | 2011-10-31 | 2013-05-10 | Steelmore Holdings Pty Ltd | Method of removing metal from a cathode |
JP2013217801A (en) * | 2012-04-10 | 2013-10-24 | Kurita Engineering Co Ltd | Decontamination method for radioactive waste resin |
KR101333319B1 (en) * | 2013-03-25 | 2013-11-27 | 신라대학교 산학협력단 | Heavy metal elimination device for using a electromagnetic field |
JP5916936B1 (en) * | 2015-12-03 | 2016-05-11 | 智治 竹内 | Heavy metal separation system |
JP6116733B1 (en) * | 2016-04-25 | 2017-04-19 | 智治 竹内 | Heavy metal separation system |
WO2017094448A1 (en) * | 2015-12-03 | 2017-06-08 | 智治 竹内 | Heavy metal separation system |
CN112047588A (en) * | 2020-09-02 | 2020-12-08 | 辽宁大学 | Method for removing heavy metals in municipal sludge by magnetization electric method |
CN114349228A (en) * | 2020-06-10 | 2022-04-15 | 长沙维禹环保科技有限公司 | Electrochemical desulfurization method for sewage |
-
1994
- 1994-09-06 JP JP06239573A patent/JP3118793B2/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100369711B1 (en) * | 2000-09-15 | 2003-01-30 | 광주과학기술원 | Electrochemical process for removal of toxic heavy metals in sludges |
WO2013063644A2 (en) * | 2011-10-31 | 2013-05-10 | Steelmore Holdings Pty Ltd | Method of removing metal from a cathode |
WO2013063644A3 (en) * | 2011-10-31 | 2014-09-25 | Steelmore Holdings Pty Ltd | Method of removing metal from a cathode |
JP2013217801A (en) * | 2012-04-10 | 2013-10-24 | Kurita Engineering Co Ltd | Decontamination method for radioactive waste resin |
KR101333319B1 (en) * | 2013-03-25 | 2013-11-27 | 신라대학교 산학협력단 | Heavy metal elimination device for using a electromagnetic field |
JP5916936B1 (en) * | 2015-12-03 | 2016-05-11 | 智治 竹内 | Heavy metal separation system |
WO2017094448A1 (en) * | 2015-12-03 | 2017-06-08 | 智治 竹内 | Heavy metal separation system |
JP6116733B1 (en) * | 2016-04-25 | 2017-04-19 | 智治 竹内 | Heavy metal separation system |
JP2017196543A (en) * | 2016-04-25 | 2017-11-02 | 智治 竹内 | Heavy metal separation system |
CN114349228A (en) * | 2020-06-10 | 2022-04-15 | 长沙维禹环保科技有限公司 | Electrochemical desulfurization method for sewage |
CN112047588A (en) * | 2020-09-02 | 2020-12-08 | 辽宁大学 | Method for removing heavy metals in municipal sludge by magnetization electric method |
Also Published As
Publication number | Publication date |
---|---|
JP3118793B2 (en) | 2000-12-18 |
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