JPS6038085A - Treatment method for wastewater containing heavy metals - Google Patents

Treatment method for wastewater containing heavy metals

Info

Publication number
JPS6038085A
JPS6038085A JP14519183A JP14519183A JPS6038085A JP S6038085 A JPS6038085 A JP S6038085A JP 14519183 A JP14519183 A JP 14519183A JP 14519183 A JP14519183 A JP 14519183A JP S6038085 A JPS6038085 A JP S6038085A
Authority
JP
Japan
Prior art keywords
chromium
heavy metal
heavy metals
wastewater containing
precipitate
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
Application number
JP14519183A
Other languages
Japanese (ja)
Other versions
JPH0347156B2 (en
Inventor
Isamu Kato
勇 加藤
Itsuko Sugimoto
杉本 伊津子
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP14519183A priority Critical patent/JPS6038085A/en
Publication of JPS6038085A publication Critical patent/JPS6038085A/en
Publication of JPH0347156B2 publication Critical patent/JPH0347156B2/ja
Granted legal-status Critical Current

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  • Removal Of Specific Substances (AREA)

Abstract

PURPOSE:To efficiently remove a heavy metal by adding a trivalent chromium ion to waste water containing one or more of a heavy metal selected from a group comprising Zn, Ni, Cd, Pb, Fe and Mn to precipitate said heavy metal along with chromium. CONSTITUTION:A solution containing a trivalent chromium salt such as chromium (III) solfate, chromium (III) chloride or chromium potassium alum is added to waste water containing one or more of a heavy metal selected from a group comprising Zn, Ni, Cd, Pb, Fe and Mn to precipitate the heavy metal along with chromium. By this method, the sufficient removal of the heavy metal is enabled even in the vicinity of a neutral region and economical effect is extremely large. The coprecipitation effect of chromium developed by the aforementioned operation is considered in such a way that chromium and heavy metals are precipitated as composite hydroxide and the property of this composite hydroxide has property near to that of chromium.

Description

【発明の詳細な説明】 本発明は重金属含有廃水に3価のクロムイオンを添加し
て重金属をクロムとともに沈澱させることにより、重金
属を効果的に除去する方法を提供するにあ、す、更には
重金属の大部分が中性では難溶の水酸化物を生成しない
ために従来pH10〜IIにおいてのみ行なわれていた
重金属含有廃水の処理を中性附近の領域でも共沈により
除去可能な方法を提供するにある。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for effectively removing heavy metals by adding trivalent chromium ions to heavy metal-containing wastewater to precipitate the heavy metals together with chromium. Provides a method that enables the treatment of heavy metal-containing wastewater, which was conventionally carried out only at pH 10 to pH II, by co-precipitation even in the near-neutral range, since most of the heavy metals do not produce poorly soluble hydroxides in neutral conditions. There is something to do.

本発明の処理の対象となる廃水とはZn、Ni。The wastewater to be treated in the present invention is Zn and Ni.

Od、 Pb、 FeおよびMnからなる群から選ばれ
る一種若しくは複数を溶存する廃水である。
This is wastewater in which one or more elements selected from the group consisting of Od, Pb, Fe, and Mn are dissolved.

重金属の塩の大部分は中性では離溶性の水酸化物は生成
せず、そのためアルカリの添加によりpHを10〜11
とし水酸化物として析出させているのであるが、そのま
まのpHでは放流できないため再度pHを中性に調整す
る必要がある。そのため薬剤および設備の費用は多大で
ある。しかるに本発明によれば中性附近でも充分に重金
属の除去が可能であるのでその経済効果は極めて大きい
。このような先行技術の欠点と本発明の効果は以下に記
述する試験例と実施例とを対比すればよシ一層明瞭とな
ろう。
Most of the salts of heavy metals do not produce soluble hydroxides in neutral conditions; therefore, the pH can be lowered to 10 to 11 by adding alkali.
Although the hydroxide is precipitated as a hydroxide, the pH cannot be discharged at the same pH, so the pH must be adjusted to neutral again. Therefore, the cost of drugs and equipment is significant. However, according to the present invention, heavy metals can be sufficiently removed even in the vicinity of neutrality, so the economic effect is extremely large. The shortcomings of the prior art and the effects of the present invention will become clearer by comparing the test examples and examples described below.

なお本発明におけるクロムの共沈効果の機構は明らかで
ないが明細j#に特には示さなかった他のいくつかの実
験結果とを照合してみるとおそらくクロムと重金属類は
複合水酸化物となって沈澱し、その複合の水酸化物の性
質はクロムに近い性質を持つようになっていると推定さ
れる。。
The mechanism of the co-precipitation effect of chromium in the present invention is not clear, but when compared with some other experimental results not specifically shown in Specification J#, it is likely that chromium and heavy metals form a composite hydroxide. It is presumed that the properties of the composite hydroxide are similar to those of chromium. .

なおまた本発明の3価のクロムイオンとじては、硫酸ク
ロム(1旧、塩化クロム(ill)、 クロムカリミョ
ウノ々ンなどの3価のクロム塩溶液を用いるととができ
るが、クロム(M)を含む廃水、たとえばクロム酸や重
クロム酸を含む廃水を還元処理して用いてもよいし、還
元処理後のクロム水酸化物の脱水汚泥を、酸で溶解して
使用してもよい。
Furthermore, the trivalent chromium ion of the present invention can be obtained by using a trivalent chromium salt solution such as chromium sulfate (1), chromium chloride (ill), or chromium chloride (ill); M)-containing wastewater, for example wastewater containing chromic acid or dichromic acid, may be reduced and used, or dehydrated sludge of chromium hydroxide after reduction treatment may be dissolved with acid and used. .

試験例 硝酸亜鉛、硫酸ニッケル、硫酸カドミウム、硫酸クロム
および硝酸鉛の各201(金属として)単独溶液(pH
4〜4.5)をNaOHでpH調整を行なった場合の溶
解度を表−1に示す。
Test Example Single solutions of zinc nitrate, nickel sulfate, cadmium sulfate, chromium sulfate, and lead nitrate (as metals) (pH
Table 1 shows the solubility of 4 to 4.5) when the pH was adjusted with NaOH.

岩−Jに示すようにpH7〜8ではZn 、 Ni 、
 Cdはほとんど処理できないことが明らかである。
As shown in Iwa-J, at pH 7-8, Zn, Ni,
It is clear that Cd can hardly be processed.

なお本例ではp I−1調整のためにNaOHを用いた
がOa’(OH)2!浴溶液用いてもはy同様の結果が
得られた。
In this example, NaOH was used to adjust p I-1, but Oa'(OH)2! Similar results were obtained using a bath solution.

実施例1(比較例を含む;以下同じ) 硝酸亜鉛、硫酸ニッケル、硫酸カドミウムおよび硝酸鉛
の各20 mf/l (金属として)混合溶液(pH4
’)をNaOHでpH7,5とし沈澱処理を行々つだ。
Example 1 (including comparative examples; the same applies hereinafter) A mixed solution of zinc nitrate, nickel sulfate, cadmium sulfate, and lead nitrate each at 20 mf/l (as metals) (pH 4
) was adjusted to pH 7.5 with NaOH and subjected to precipitation.

上澄液の分析結果を表−2、AIに示す。&1に示すよ
うに共存重金属の相互共沈効果によりPbはほとんど検
出されかかったが、Zn。
The analysis results of the supernatant are shown in Table 2, AI. As shown in &1, Pb was almost detected due to the mutual coprecipitation effect of coexisting heavy metals, but Zn.

Nl、Cd はかなシ残留した。Nl and Cd remained briefly.

次に一般的共沈剤として使用される塩化第2鉄を100
1rvt(Feとして)混合液に添加して共沈処理を行
なった。結果をA2に示す。Zn。
Next, add 100% of ferric chloride, which is commonly used as a coprecipitant.
1 rvt (as Fe) was added to the mixed solution to perform coprecipitation treatment. The results are shown in A2. Zn.

Nl、Cd に対する共沈効果は認められるもののNi
、Cd に対する効果は低かった。
Although a coprecipitation effect is observed for Nl and Cd, Ni
, the effect on Cd was low.

塩化第2鉄の代りに硫酸クロムを100■μ(Orとし
て)添加して共沈処理した場合の結果を墓3に示す。ク
ロムの共沈効果は顕著であり、Zn、 Ni 、 Od
 もほぼ完全に除去できた。但し表中A】及び屋2け比
較であり、扁3が実施例に相当する。
Figure 3 shows the results when coprecipitation treatment was carried out by adding 100μ (as Or) of chromium sulfate instead of ferric chloride. The coprecipitation effect of chromium is significant, and Zn, Ni, Od
was also almost completely removed. However, in the table, A] and 2 are compared, and 3 corresponds to the example.

A3においてpHを更に高めればより重金属イオンは減
少するが、現実の問題として表の轟3程度に重金属を除
去できれば、それ以上の処理は不要である。
If the pH is further increased in A3, heavy metal ions will be further reduced, but as a practical matter, if heavy metals can be removed to the extent of Todoroki 3 in the table, no further treatment is necessary.

実施例2 硝酸亜鉛、硫酸カドミウム、硫酸ニッケル、硫酸第一鉄
および硫酸マンガンの各20■β(金属として)単独溶
液(pI−14〜4.5)に硫酸クロムを段階的に添加
し、クロムの添加附の効果を詳細に検討を行左っだ。上
澄液の分析結果を表−3に示す。処理はいずれもpl■
7.5でλ〉る。
Example 2 Chromium sulfate was added stepwise to a single solution (pI-14 to 4.5) of zinc nitrate, cadmium sulfate, nickel sulfate, ferrous sulfate, and manganese sulfate (as metals) at 20 μm each. A detailed study of the effects of the addition of . The analysis results of the supernatant are shown in Table 3. All processing is pl■
7.5 = λ〉.

表−2、表−3に示したように3価クロムは卓越した共
沈効果を有している。通常の共沈処理では対象金属に対
し共沈剤を大過剰に添加するのが一般であるが3価りロ
ム゛の場合は対象重金属とほぼ当量又はそれ以下で十分
である。
As shown in Tables 2 and 3, trivalent chromium has an outstanding coprecipitation effect. In normal coprecipitation treatment, it is common to add a coprecipitant in large excess to the target metal, but in the case of trivalent ROM, it is sufficient to use an amount approximately equivalent to or less than the target heavy metal.

実施例3 硝酸亜鉛、硫酸カドミウムおよび硫酸ニッケルの各20
 W/l (金属として)単独溶液(pH4〜45)に
硫酸クロムを添加し、さらにNaOHを添加してp)(
を9に調整して共沈処理L7た。上澄液の分析結果を第
4表に示す。
Example 3 20 each of zinc nitrate, cadmium sulfate and nickel sulfate
W/l (as a metal) Add chromium sulfate to a single solution (pH 4-45) and then add NaOH to obtain p)(
was adjusted to 9 and coprecipitation treatment L7 was performed. The analysis results of the supernatant are shown in Table 4.

第4表 第4表から、pHを高くすると、Orの添加量は少なく
ても共沈効果が優れることがわかる。
Table 4 From Table 4, it can be seen that when the pH is increased, the coprecipitation effect is excellent even if the amount of Or added is small.

Claims (1)

【特許請求の範囲】[Claims] 1、Zn、 Ni 、 Cd、 Pb、 FeおよびM
nからなる群から選ばれる一種もしくは二種以上の重金
属を含有する廃水に3価のクロムイオンを添加して重金
属をクロムとともに沈澱させることを特徴とする重金属
含有廃水の処理法。
1, Zn, Ni, Cd, Pb, Fe and M
A method for treating wastewater containing heavy metals, which comprises adding trivalent chromium ions to wastewater containing one or more heavy metals selected from the group consisting of n to precipitate the heavy metals together with chromium.
JP14519183A 1983-08-09 1983-08-09 Treatment method for wastewater containing heavy metals Granted JPS6038085A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14519183A JPS6038085A (en) 1983-08-09 1983-08-09 Treatment method for wastewater containing heavy metals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14519183A JPS6038085A (en) 1983-08-09 1983-08-09 Treatment method for wastewater containing heavy metals

Publications (2)

Publication Number Publication Date
JPS6038085A true JPS6038085A (en) 1985-02-27
JPH0347156B2 JPH0347156B2 (en) 1991-07-18

Family

ID=15379524

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14519183A Granted JPS6038085A (en) 1983-08-09 1983-08-09 Treatment method for wastewater containing heavy metals

Country Status (1)

Country Link
JP (1) JPS6038085A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113955838A (en) * 2021-09-23 2022-01-21 北京化工大学 Method for co-processing electroplating waste residue and chromium-containing heavy metal ion waste liquid

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5533673A (en) * 1978-09-01 1980-03-08 Chino Works Ltd Resistance adjustment method of temperature measuring resistor

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5533673A (en) * 1978-09-01 1980-03-08 Chino Works Ltd Resistance adjustment method of temperature measuring resistor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113955838A (en) * 2021-09-23 2022-01-21 北京化工大学 Method for co-processing electroplating waste residue and chromium-containing heavy metal ion waste liquid

Also Published As

Publication number Publication date
JPH0347156B2 (en) 1991-07-18

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