JPH02203905A - Method for adsorbing and removing heavy metals - Google Patents
Method for adsorbing and removing heavy metalsInfo
- Publication number
- JPH02203905A JPH02203905A JP2265289A JP2265289A JPH02203905A JP H02203905 A JPH02203905 A JP H02203905A JP 2265289 A JP2265289 A JP 2265289A JP 2265289 A JP2265289 A JP 2265289A JP H02203905 A JPH02203905 A JP H02203905A
- Authority
- JP
- Japan
- Prior art keywords
- heavy metals
- contact
- exudate
- pref
- carbonate mineral
- 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
Links
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910001868 water Inorganic materials 0.000 claims abstract description 25
- 210000000416 exudates and transudate Anatomy 0.000 claims abstract description 23
- 229910001748 carbonate mineral Inorganic materials 0.000 claims abstract description 20
- 238000001179 sorption measurement Methods 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 abstract description 8
- 229910052793 cadmium Inorganic materials 0.000 abstract description 5
- 239000002440 industrial waste Substances 0.000 abstract description 4
- 229910052742 iron Inorganic materials 0.000 abstract description 4
- 229910052753 mercury Inorganic materials 0.000 abstract description 4
- 229910021532 Calcite Inorganic materials 0.000 abstract description 3
- 238000005273 aeration Methods 0.000 abstract description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 abstract description 2
- 239000010459 dolomite Substances 0.000 abstract description 2
- 229910000514 dolomite Inorganic materials 0.000 abstract description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract 1
- 238000009792 diffusion process Methods 0.000 abstract 1
- 229910052745 lead Inorganic materials 0.000 abstract 1
- 235000014653 Carica parviflora Nutrition 0.000 description 9
- 241000243321 Cnidaria Species 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 229910052748 manganese Inorganic materials 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- 239000013522 chelant Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000329589 Gersemia rubiformis Species 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- -1 for example Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、滲出水中に含まれる重金属の吸着除去方法に
関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a method for adsorbing and removing heavy metals contained in exudate water.
〈従来の技術〉
従来、工業用等の廃水を含む産業又は一般廃棄物最終処
理場の滲出水から、例えばカドミウム、水銀等の重金属
を除去する方法としては、例えば重金属用キレート樹脂
又はイオン交換樹脂等に吸着させて行う方法が知られて
いる。<Prior art> Conventionally, as a method for removing heavy metals such as cadmium and mercury from leachate of industrial or general waste final treatment plants, including industrial wastewater, for example, chelate resins for heavy metals or ion exchange resins have been used. A known method is to adsorb it onto a material such as
しかしながら前記重金属用キレート樹脂及びイオン交換
樹脂は、非常に高価であり、経済的に問題がある。However, the chelate resins and ion exchange resins for heavy metals are very expensive and pose an economical problem.
〈発明が解決しようとする課題〉
本発明の目的は、容易にしかも効率良く滲出水から重金
属を吸着除去する方法を提供することにある。<Problems to be Solved by the Invention> An object of the present invention is to provide a method for easily and efficiently adsorbing and removing heavy metals from exudate water.
〈課題を解決するための手段〉
本発明によれば、好気的条件下、重金属を含む滲出水に
、炭酸塩鉱物を接触させることを特徴とする重金属の吸
着除去方法が提供される。<Means for Solving the Problems> According to the present invention, there is provided a method for adsorption and removal of heavy metals, which comprises bringing carbonate minerals into contact with exudate water containing heavy metals under aerobic conditions.
以下本発明を更に詳細に説明する。The present invention will be explained in more detail below.
本発明の吸着除去方法では、工業用、生ゴミ等の滲出水
等に好気的条件下、炭酸塩鉱物を接触させることを特徴
とする。The adsorption removal method of the present invention is characterized by bringing carbonate minerals into contact with exudate water from industrial waste, garbage, etc. under aerobic conditions.
本発明に用いる炭酸塩鉱物は、産業又は一般廃棄物最終
処理場の滲出水と、好気的条件下、接触させることによ
り、該滲出水中のHg、Cd、Fe、Mn、Pd等の重
金属を吸着することが可能な物質であって、具体的には
例えば、カルサイト、アラゴナイト、バテライト、不定
形等の炭酸カルシウム、ドロマイト、炭酸マグネシウム
及び珊瑚等から成る群の1種又は2種以上より選択され
ることが好ましく、特に多層構造を有する多孔質の珊瑚
を用いることが望ましい。該珊瑚とはへ方珊瑚亜絹珊瑚
科の動物の総称であり、例えばアカ珊瑚、モモイロ珊瑚
、シロ珊瑚、インパナ、ウミイチゴ等を挙げることがで
きる。The carbonate mineral used in the present invention can remove heavy metals such as Hg, Cd, Fe, Mn, and Pd in the leachate by contacting it with leachate from an industrial or general waste final treatment plant under aerobic conditions. A substance that can be adsorbed, specifically selected from one or more of the group consisting of calcite, aragonite, vaterite, amorphous calcium carbonate, dolomite, magnesium carbonate, coral, etc. It is particularly desirable to use porous coral having a multilayer structure. The term "coral" is a general term for animals belonging to the family Coralidae, and includes, for example, red coral, white coral, white coral, impana, and sea strawberry.
本発明において、重金属を含む滲出水を前記炭酸塩鉱物
に接触させる場合には、好気的条件下にて行う必要があ
る。この際単に滲出水に炭酸塩鉱物を接触させる場合に
は、滲出水中の炭酸ガス濃度が高いために、重金属が十
分に吸着されず、重炭酸塩として再溶出する。また処理
場の供用直後の滲出水は、塩分濃度が高く、イオウ細菌
の活動を抑制することができるが、長期間の供用による
塩分濃度の低下に伴なって、イオウ細菌の活動が活発に
なり、滲出水中のイオウ分が酸化して硫酸を生じる。こ
のため該硫酸が炭酸塩鉱物と反応し、石膏又は硫酸マグ
ネシウム等を生成して、炭酸塩鉱物としての機能が低下
あるいはペースト化して流路を閉塞するのである。また
前記好気的条件下では1重金属のみならず、滲出水中の
生物処理を行うことが可能であるが、生物処理と、重金
属の吸着除去とを同時に行うと、重金属の除去効率が低
下するので、前処理において生物処理を別に行っておく
のが好ましい。In the present invention, when the exudate water containing heavy metals is brought into contact with the carbonate mineral, it is necessary to do so under aerobic conditions. At this time, if the carbonate mineral is simply brought into contact with the exudate water, the heavy metals will not be sufficiently adsorbed due to the high concentration of carbon dioxide in the exudate water, and will be re-eluted as bicarbonate. In addition, the leachate immediately after a treatment plant is in service has a high salt concentration, which can suppress the activity of sulfur bacteria, but as the salinity decreases due to long-term operation, the activity of sulfur bacteria increases. , the sulfur content in the leachate oxidizes to produce sulfuric acid. For this reason, the sulfuric acid reacts with the carbonate mineral to produce gypsum or magnesium sulfate, which reduces its function as a carbonate mineral or turns it into a paste, blocking the flow path. Furthermore, under the aerobic conditions mentioned above, it is possible to perform biological treatment of not only one heavy metal but also the leachate water, but if biological treatment and adsorption removal of heavy metals are performed simultaneously, the removal efficiency of heavy metals will decrease. It is preferable to perform biological treatment separately in the pretreatment.
本発明において、前記好気的条件とは1例えばCO2濃
度が好ましくは3Qppm以下であり、更に好ましくは
、DO2濃度をlppm以上、特に3ppm以上にする
ことが望ましい。この際前記CO2濃度が30ppmを
超える場合には、重金属が重炭酸塩として溶出し、且つ
イオウ細菌が活発化する恐れがあるので好ましくない。In the present invention, the aerobic conditions are 1, for example, preferably a CO2 concentration of 3 Qppm or less, and more preferably a DO2 concentration of 1 ppm or more, particularly 3 ppm or more. At this time, if the CO2 concentration exceeds 30 ppm, it is not preferable because heavy metals may be eluted as bicarbonate and sulfur bacteria may become active.
本発明において、滲出水を炭酸塩鉱物に接触させる際に
、好気的条件を保つには、例えば散水口床法又は固定床
において湯気する方法、即ち滲出水を集水し、生物処理
後若しくは前に、炭酸塩鉱物を口床とした散水口床又は
槽に炭酸塩鉱物を充填した後、滲出水を流通あるいは回
分させ湯気する方法等を好ましく挙げることができる。In the present invention, in order to maintain aerobic conditions when leachate is brought into contact with carbonate minerals, for example, the water sprinkling bed method or the method of steaming in a fixed bed are used, in other words, the leachate is collected, and after biological treatment or Preferred methods include filling a water spout bed or a tank with carbonate minerals with carbonate minerals, and then circulating or batching the exudate water to generate steam.
本発明において、前記炭酸塩鉱物を滲出水に接触させる
時間は5分〜1週間の範囲であることが好ましい。この
際5分未満の場合には、重金属を十分に除去することが
できず、また1週間を超えて接触させても除去効果の向
上が期待できないので経済的に好ましくない。この際炭
酸塩鉱物は単独で使用する他、例えばレキ、砂等を混合
して用いることができ、更に前記接触方法において炭酸
塩鉱物を多層に分けて接触させることも可能である。In the present invention, the time period for which the carbonate mineral is brought into contact with the exudate water is preferably in the range of 5 minutes to 1 week. In this case, if the contact time is less than 5 minutes, the heavy metals cannot be removed sufficiently, and even if the contact time exceeds 1 week, no improvement in the removal effect can be expected, which is economically undesirable. In this case, the carbonate mineral can be used alone or in combination with, for example, limestone, sand, etc. Furthermore, in the above-mentioned contact method, it is also possible to contact the carbonate mineral in multiple layers.
〈発明の効果〉
本発明の吸着除去方法では、滲出液を好気的条件下にお
いて単に炭酸塩鉱物に接触させるのみで、高率よく、且
つ選択的に重金属を除去することができるので、工業的
に非常に有用である。<Effects of the Invention> The adsorption removal method of the present invention can remove heavy metals at a high rate and selectively by simply bringing the exudate into contact with carbonate minerals under aerobic conditions. very useful.
〈実施例〉
以下本発明を実施例及び比較例により更に詳細に説明す
るが、本発明はこれらに限定されるものではない。<Examples> The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the present invention is not limited thereto.
失嵐■↓
・埋立処理後8年を経過した産業廃棄物処分場の滲出水
をバイパスし、下部に散気管を備え、且つカルサイト及
びアラゴナイトの混合物コーラル20電を充填した20
cmφX100CII+のカラムに、IQ/分の速度で
8力月間通水した。その結果コーラルの石膏化は全く起
らなかった。流入時及び流出時における前記滲出水中の
重金属量及びDO1CO2量を表1に示す。Lost Storm■↓ ・20 by-passing the leachate from an industrial waste disposal site that has been landfilled for 8 years, equipped with an aeration pipe at the bottom, and filled with Coral 20, a mixture of calcite and aragonite.
Water was passed through the cmφX100CII+ column at a rate of IQ/min for 8 months. As a result, no gypsumization of coral occurred. Table 1 shows the amounts of heavy metals and DO1CO2 in the leachate at the time of inflow and outflow.
表 1
カラムに散気管を取り付けなかった以外は、実施例1と
同様に行ったところ、8力月後にコーラルは石膏化し、
ペースト状になって、通水不能となった。Table 1 The same procedure as in Example 1 was carried out except that a diffuser pipe was not attached to the column. After 8 months, the coral turned into gypsum.
It became paste-like and water could not pass through it.
失庭桝裟
滲出水に人工滲出水としてHg、C,d、Fe及びMn
夫々を1100pp並びにCO2:300 p p m
を含む人工滲出水を用いた以外は、実施例1と同様に行
った。流出時における滲出水の水質を表2に示す。Hg, C, d, Fe, and Mn as artificial exudate water in the exudate water
1100 pp each and CO2: 300 pp m
The same procedure as in Example 1 was conducted except that artificial exudate water containing . Table 2 shows the quality of the exudate water at the time of the outflow.
坦較孤又
滲出水に人工滲出水として、Hg、Cd、Fe及びMn
夫々を1100pp含む人工滲出水を用いた以外は、比
較例]、と同様に行った。流出時における滲出水の水質
を表2に示す。As artificial exudate water, Hg, Cd, Fe and Mn are added to exudate water.
Comparative Example] was carried out in the same manner as in [Comparative Example] except that artificial exudate water containing 1100 pp of each was used. Table 2 shows the quality of the exudate water at the time of the outflow.
表 2
以上の結果より、好気的条件下で行なわれた本発明の実
施例では、単に、炭酸塩鉱物に滲出水を接触させた比較
例に比して、重金属を効率良く吸着除去できることが判
った。Table 2 From the above results, it was found that in the examples of the present invention carried out under aerobic conditions, heavy metals could be adsorbed and removed more efficiently than in the comparative examples in which exudate water was simply brought into contact with carbonate minerals. understood.
Claims (1)
触させることを特徴とする重金属の吸着除去方法。A method for adsorption and removal of heavy metals, which comprises bringing carbonate minerals into contact with exudate water containing heavy metals under aerobic conditions.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2265289A JPH02203905A (en) | 1989-02-02 | 1989-02-02 | Method for adsorbing and removing heavy metals |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2265289A JPH02203905A (en) | 1989-02-02 | 1989-02-02 | Method for adsorbing and removing heavy metals |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02203905A true JPH02203905A (en) | 1990-08-13 |
Family
ID=12088776
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2265289A Pending JPH02203905A (en) | 1989-02-02 | 1989-02-02 | Method for adsorbing and removing heavy metals |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02203905A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2235663A1 (en) * | 2003-12-23 | 2005-07-01 | Universidad De Oviedo | Removal of bivalent metals dissolved in aqueous medium comprises sorption by biogenic calcium carbonate to reduce e.g. cadmium levels |
CN107935300A (en) * | 2017-11-22 | 2018-04-20 | 沈阳艾柏瑞环境科技有限公司 | A kind of process unit and method of non-embrane method processing landfill leachate |
-
1989
- 1989-02-02 JP JP2265289A patent/JPH02203905A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2235663A1 (en) * | 2003-12-23 | 2005-07-01 | Universidad De Oviedo | Removal of bivalent metals dissolved in aqueous medium comprises sorption by biogenic calcium carbonate to reduce e.g. cadmium levels |
CN107935300A (en) * | 2017-11-22 | 2018-04-20 | 沈阳艾柏瑞环境科技有限公司 | A kind of process unit and method of non-embrane method processing landfill leachate |
CN107935300B (en) * | 2017-11-22 | 2020-03-06 | 沈阳艾柏瑞环境科技有限公司 | Process device and method for treating landfill leachate by non-membrane method |
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