JPH09299962A - Treatment of waste water containing lead ton - Google Patents
Treatment of waste water containing lead tonInfo
- Publication number
- JPH09299962A JPH09299962A JP14519296A JP14519296A JPH09299962A JP H09299962 A JPH09299962 A JP H09299962A JP 14519296 A JP14519296 A JP 14519296A JP 14519296 A JP14519296 A JP 14519296A JP H09299962 A JPH09299962 A JP H09299962A
- Authority
- JP
- Japan
- Prior art keywords
- waste water
- lead
- value
- lead ion
- calcium silicate
- 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
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Removal Of Specific Substances (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、鉛イオンを含む排
水から鉛イオンを不溶物として分離除去するための処理
方法に関するものである。TECHNICAL FIELD The present invention relates to a treatment method for separating and removing lead ions as insoluble matter from wastewater containing lead ions.
【0002】[0002]
【従来の技術】従来、鉛イオンを含む排水の処理方法と
しては、一般に中和沈殿法または硫化沈殿法が採用され
ていた。しかしながら、中和沈殿法によるときは、鉛イ
オンはpH9.5で沈殿するが、その沈殿pH領域は極
めて狭いために、排水のpH管理が極めて難しいという
問題があり、また硫化沈殿法によるときは、排水のpH
を3.5以上とした上で硫化剤を添加して行えばよいの
で、pH調整域が広く排水のpH管理は容易であるが、
排水中に投入した硫化剤の分解等により発生する有毒ガ
スや溶存ガスの脱ガスを行うための煩雑な設備を必要と
するので好ましくなかった。2. Description of the Related Art Conventionally, a neutralization precipitation method or a sulfurization precipitation method has been generally adopted as a method for treating wastewater containing lead ions. However, when the neutralization precipitation method is used, lead ions precipitate at pH 9.5, but since the precipitation pH range is extremely narrow, there is the problem that pH control of wastewater is extremely difficult. , PH of drainage
Since it is only necessary to add a sulfiding agent after adjusting the value to 3.5 or more, the pH adjustment range is wide and the pH control of the wastewater is easy.
This is not preferable because it requires complicated equipment for degassing toxic gas or dissolved gas generated by decomposition of the sulfiding agent charged into the waste water.
【0003】[0003]
【発明が解決しようとする課題】本発明は鉛イオンを含
有する廃水の処理を行うに際しての上記した問題点に鑑
みてなされたものであって、排水中の鉛イオンを有毒ガ
スの発生の危険性のある添加剤を使用することなく、広
範なpH領域で不溶化して分離することができるような
処理方法を提供することを目的とするものである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems in treating wastewater containing lead ions, and the lead ions in the waste water are at a risk of generating toxic gas. It is an object of the present invention to provide a treatment method capable of insolubilizing and separating in a wide pH range without using any additive having properties.
【0004】[0004]
【課題を解決するための手段】上記の目的を達成するた
めの本発明は、鉛イオン含有排水の処理を行うに際し、
該排水のpHを5.6〜12の間に調整した後、ケイ酸
カルシウムを重量比で鉛の75倍量以上添加することに
より鉛イオンを不溶物として分離することを特徴とする
鉛イオンを含有する排水の処理方法である。Means for Solving the Problems The present invention for achieving the above-mentioned object is to provide a method for treating lead ion-containing wastewater,
After adjusting the pH of the waste water to be between 5.6 and 12, lead ions are separated as insoluble matter by adding calcium silicate in an amount of 75 times as much as lead by weight or more. This is the method for treating the wastewater contained.
【0005】本発明で使用することのできる好ましいケ
イ酸カルシウムは、CaSiO3、Ca2SiO4等で
あり、pH調整剤としては、一般的に使用されているア
ルカリ、または鉱酸でよく、pH値を5.6〜12の間
に調整し得るものであれば特に限定されるものでない。Preferred calcium silicates that can be used in the present invention are CaSiO 3 , Ca 2 SiO 4 and the like, and as a pH adjuster, a commonly used alkali or mineral acid may be used. The value is not particularly limited as long as the value can be adjusted between 5.6 and 12.
【0006】[0006]
【発明の実施の形態】以下に本発明者の行った実験例に
基づいて本発明をさらに詳細に説明する。pH値の影響の検討実験 本実験には、排水処理液として鉛イオン濃度2.7mg
/lのものを用いた。この排水500mlを撹拌機付き
反応容器(1lビーカー)に投入し、撹拌しながら、p
H値が種々の値を採るようにCa(OH)2を添加し
た。pH値の変化が殆どなくなり所定の値を安定して維
持するようになったのを確認した後、CaSiO3を1
15mg(CaSiO3/Pb=85.2)添加し、6
0分間撹拌を続けた後、生成した不溶物を固液分離して
処理終了液を得、次いで該処理終了液中の鉛イオンの濃
度を定量した。得られた結果を表1に示す。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in more detail based on the experimental examples conducted by the present inventor. Examination experiment of influence of pH value In this experiment, lead ion concentration was 2.7 mg as wastewater treatment liquid.
/ L was used. Pour 500 ml of this waste water into a reaction vessel equipped with a stirrer (1 l beaker) and p while stirring.
Ca (OH) 2 was added so that the H value could take various values. After confirming that the change in pH value almost disappeared and the predetermined value was stably maintained, CaSiO 3 was added to 1
Add 15 mg (CaSiO 3 /Pb=85.2), 6
After continuing stirring for 0 minutes, the produced insoluble matter was subjected to solid-liquid separation to obtain a treatment completed liquid, and then the concentration of lead ions in the treatment completed liquid was quantified. The results obtained are shown in Table 1.
【0007】[0007]
【表1】 試料 pH値 終了液のPbイオン濃度 番号 (mg/l) ──────────────────────────── 1 5.31 0.18 2 5.62 0.08 3 6.15 0.03 4 7.64 0.02 5 9.87 0.01 6 11.94 0.02 ────────────────────────────[Table 1] Sample pH value Pb ion concentration of the final solution Number (mg / l) ───────────────────────────── 1 5. 31 0.18 2 5.62 0.08 3 6.15 0.03 4 7.64 0.02 5 9.87 0.01 6 11.94 0.02 ─────────── ─────────────────
【0008】ケイ酸カルシウム添加の影響に対する実験 また、上記と同様の排水処理液を用い、該排水500m
lを上記と同様の反応容器に投入し、排水を撹拌しなが
らpH値が6.1になるようにCa(OH)2を添加
し、pH値の変化がなくなったのを確認した後、CaS
iO3を撹拌しながら60mg〜120mgの範囲で量
を変えて添加し、60分間撹拌を続けた後、生成した不
溶物を固液分離して処理終了液を得、該処理終了液中の
鉛イオンの濃度を測定した。得られた結果を表2に示
す。 Experiment on influence of addition of calcium silicate Also, using the same wastewater treatment liquid as above, the wastewater of 500 m
1 into a reaction container similar to the above, Ca (OH) 2 was added so that the pH value became 6.1 while stirring the waste water, and after confirming that the pH value did not change, CaS
iO 3 was added while changing the amount in the range of 60 mg to 120 mg with stirring, and the stirring was continued for 60 minutes, then the generated insoluble matter was subjected to solid-liquid separation to obtain a treatment completed liquid, and the lead in the treatment completed liquid was obtained. The concentration of ions was measured. Table 2 shows the obtained results.
【0009】[0009]
【表2】 試料 pH値 CaSiO3 CaSiO3 終了液中のPb 番号 (mg/l) /Pb比 イオン濃度(mg/l) ─────────────────────────────────── 7 6.11 60 44.4 2.40 8 6.17 70 51.9 0.68 9 6.14 85 63.0 0.36 10 6.10 100 74.1 0.11 11 6.18 110 81.5 0.05 12 6.12 120 88.9 0.02 ────────────────────────────────────[Table 2] Sample pH value CaSiO 3 CaSiO 3 Pb number (mg / l) / Pb ratio in the final solution Ion concentration (mg / l) ─────────────────── ───────────────── 7 6.11 60 44.4 2.40 8 6.17 70 51.9 0.68 9 6.14 85 63.0 0.36 10 6.10 100 74.1 0.11 11 6.18 110 81.5 0.05 12 6.12 120 88.9 0.02 ────────────────── ────────────────────
【0010】表1および表2の結果から、鉛イオン含有
排水からの鉛イオンの沈殿率は、排水のpH値およびC
aSiO3の添加量によって左右されることが分かる。
そして、排水中の鉛イオンの量を排水基準値以下にする
ためには、排水のpH値を5.6〜12の範囲に調整し
た後、CaSiO3を重量比で鉛の75倍量以上添加す
ることが望ましいことが分かる。一方CaSiO3のよ
うなケイ酸カルシウムを重量比で鉛の90倍量以上添加
しても鉛イオンの沈殿率はそれ以上向上しないので、こ
の値が添加量の上限となる。このようにpH調整後の排
水にケイ酸カルシウムを添加することにより鉛イオンの
沈殿率が向上する理由については十分に明らかではない
が、ケイ酸カルシウム中のカルシウムの一部が鉛イオン
と置換されることによるものと考えられる。From the results shown in Tables 1 and 2, the precipitation rate of lead ions from the lead ion-containing wastewater is determined by the pH value of the wastewater and the C value.
It can be seen that it depends on the addition amount of aSiO 3 .
Then, in order to reduce the amount of lead ions in the wastewater to the standard value of the wastewater or less, after adjusting the pH value of the wastewater to the range of 5.6 to 12, CaSiO 3 is added in an amount 75 times as much as the lead by weight or more. It turns out that it is desirable to do. On the other hand, even if calcium silicate such as CaSiO 3 is added in an amount 90 times as much as that of lead in terms of weight ratio, the precipitation rate of lead ions is not further improved, and this value is the upper limit of the addition amount. The reason why the precipitation rate of lead ions is improved by adding calcium silicate to the wastewater after pH adjustment is not fully clear, but some of calcium in calcium silicate is replaced with lead ions. It is thought that this is due to things.
【0011】[0011]
【実施例】次ぎに本発明の実施例について説明する。Next, an embodiment of the present invention will be described.
【0012】実施例1:、鉛イオン7.3mg/lが含
まれているナトリウムを含む塩化物溶液の排水1000
mlにNaOHを加えてpH値を8.32に調整した
後、CaSiO3580mgを添加した。その後30分
間の撹拌を行い、生成した沈殿物を分離して処理終了液
を得た。該終了液について液中の鉛イオン濃度を測定し
たところ、その値は0.06mg/lであり、十分に排
水基準値を満足するものであることが分かった。Example 1: Drainage of a chloride solution containing sodium containing lead ions of 7.3 mg / l 1000
After adjusting the pH value to 8.32 by adding NaOH to ml, 580 mg of CaSiO 3 was added. Then, the mixture was stirred for 30 minutes, and the produced precipitate was separated to obtain a treatment completed liquid. When the lead ion concentration in the liquid of the finished liquid was measured, it was found to be 0.06 mg / l, which sufficiently satisfied the wastewater standard value.
【0013】実施例2:鉛イオン1.1mg/lが含ま
れるpH値が4.5の硫酸塩溶液の排水500mlにC
a(OH)2を加えてpH値を11.05に調整した
後、Ca2SiO451mgを添加した。その後75分
間の撹拌を行い、生成した沈殿物を分離して処理終了液
を得た。該終了液について液中の鉛イオン濃度を測定し
たところ、その値は0.01mg/lであり、十分に排
水基準値を満足するものであることが分かった。Example 2 C was added to 500 ml of drainage of a sulfate solution having a pH value of 4.5 containing lead ion of 1.1 mg / l.
After adjusting the pH value to 11.05 by adding a (OH) 2 , 51 mg of Ca 2 SiO 4 was added. Then, the mixture was stirred for 75 minutes, and the generated precipitate was separated to obtain a treatment completed liquid. When the lead ion concentration in the liquid of the finished liquid was measured, it was found to be 0.01 mg / l, which was sufficiently satisfied with the drainage standard value.
【0014】[0014]
【発明の効果】以上述べたように、本発明の処理方法に
よるときは、鉛イオンを含む排水の処理を行うに際し
て、排水のpH値を5.6〜12の範囲に調整した後、
ケイ酸カルシウムを重量比で鉛の75倍量以上添加する
ことにより、鉛イオンを不溶化して容易に分離除去する
ことができる。そして本発明の方法によるときは、毒性
の強いガスを発生するような硫化剤等を用いることな
く、且つ鉛イオンを沈殿させるための排水のpH値の調
整範囲も広域であって調整が容易に行えるばかりでな
く、このpH値の領域では、亜鉛イオン、鉄(II)イ
オン等も不溶物として同時に除去することができるの
で、排水処理方法としてその利用価値は高い。As described above, according to the treatment method of the present invention, when treating the wastewater containing lead ions, after adjusting the pH value of the wastewater to the range of 5.6 to 12,
By adding calcium silicate in an amount 75 times or more that of lead by weight, lead ions can be insolubilized and easily separated and removed. When the method of the present invention is used, the adjustment range of the pH value of the wastewater for precipitating lead ions is wide without using a sulfiding agent or the like that generates highly toxic gas, and the adjustment is easy. Not only can it be performed, but zinc ions, iron (II) ions, and the like can also be simultaneously removed as insoluble matter in this pH value range, and therefore its utility value as a wastewater treatment method is high.
Claims (1)
該排水のpHを5.6〜12の間に調整した後、ケイ酸
カルシウムを重量比で鉛の75倍量以上添加することに
より鉛イオンを不溶物として分離することを特徴とする
鉛イオンを含有する排水の処理方法。1. When treating wastewater containing lead ions,
After adjusting the pH of the waste water to be between 5.6 and 12, lead ions are separated as insoluble matter by adding calcium silicate in an amount of 75 times as much as lead by weight or more. Wastewater treatment method contained.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14519296A JPH09299962A (en) | 1996-05-15 | 1996-05-15 | Treatment of waste water containing lead ton |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14519296A JPH09299962A (en) | 1996-05-15 | 1996-05-15 | Treatment of waste water containing lead ton |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09299962A true JPH09299962A (en) | 1997-11-25 |
Family
ID=15379561
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14519296A Pending JPH09299962A (en) | 1996-05-15 | 1996-05-15 | Treatment of waste water containing lead ton |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09299962A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016087493A (en) * | 2014-10-30 | 2016-05-23 | 住友金属鉱山株式会社 | Treatment method of cadmium content drainage |
JP2017192916A (en) * | 2016-04-22 | 2017-10-26 | 住友金属鉱山株式会社 | Wastewater treatment method |
-
1996
- 1996-05-15 JP JP14519296A patent/JPH09299962A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016087493A (en) * | 2014-10-30 | 2016-05-23 | 住友金属鉱山株式会社 | Treatment method of cadmium content drainage |
JP2017192916A (en) * | 2016-04-22 | 2017-10-26 | 住友金属鉱山株式会社 | Wastewater treatment method |
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