JPS582165B2 - Processing method for chromic acid waste liquid - Google Patents

Processing method for chromic acid waste liquid

Info

Publication number
JPS582165B2
JPS582165B2 JP54105217A JP10521779A JPS582165B2 JP S582165 B2 JPS582165 B2 JP S582165B2 JP 54105217 A JP54105217 A JP 54105217A JP 10521779 A JP10521779 A JP 10521779A JP S582165 B2 JPS582165 B2 JP S582165B2
Authority
JP
Japan
Prior art keywords
solution
chromium
waste liquid
waste
chromic acid
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.)
Expired
Application number
JP54105217A
Other languages
Japanese (ja)
Other versions
JPS5632329A (en
Inventor
亮了 岩元
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.)
KITAOOSAKA SEISO KK
Original Assignee
KITAOOSAKA SEISO KK
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 KITAOOSAKA SEISO KK filed Critical KITAOOSAKA SEISO KK
Priority to JP54105217A priority Critical patent/JPS582165B2/en
Publication of JPS5632329A publication Critical patent/JPS5632329A/en
Publication of JPS582165B2 publication Critical patent/JPS582165B2/en
Expired legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

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  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Treatment And Processing Of Natural Fur Or Leather (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

【発明の詳細な説明】 本発明は6価クロムを含有するクロムめっき工場より排
出される老化廃液ならびにその水溶液、またはプラスチ
ックめっきのクロム含有エッチング廃液ならびにその水
洗液において、これらの単一廃液もしくは2種以上の混
合廃液中、特に鉄、銅などの重金属を1リットル中20
g以上を含有し、そのまゝでは到底皮かくなめし用は勿
論、その他の工業にも全く使用の価値なきクロム酸含有
廃液を簡易かつ経済的に処理し、皮かくなめし用クロム
酸溶液としての使用に適するクロム酸含有廃液の処理方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is an aging waste solution discharged from a chromium plating factory containing hexavalent chromium and its aqueous solution, or a chromium-containing etching waste solution for plastic plating and its washing solution. Heavy metals such as iron and copper are contained in mixed waste liquid containing more than 20% of waste per liter.
The chromic acid-containing waste liquid, which contains more than 3.0 g of chromic acid and is of no use in leather tanning or other industries, can be easily and economically treated, and can be used as a chromic acid solution for leather tanning. The present invention relates to a method for treating chromic acid-containing waste liquid suitable for use.

公知のように、クロム資源は、わが国内においてその産
出は皆無でその全量を輸入に倚存している現状である。
As is well known, the current situation is that there are no chromium resources produced in Japan, and the entire amount is imported.

従ってクロム原料を使用する各工業においては資源愛用
の経済的立場より、徒な放棄は許されないのみならず、
更にクロム含有廃物の放棄は公害管理の立場よりも認め
られないことは熟知の事実である。
Therefore, in each industry that uses chromium raw materials, from an economic standpoint that favors the use of resources, wasteful abandonment is not only unacceptable;
Furthermore, it is a well-known fact that the abandonment of chromium-containing waste is unacceptable from a pollution control standpoint.

従って、たとえば、クロムめっきの老化廃液とか、プラ
スチックのクロム含有エッチング廃液、ならびにこれら
の水洗液の有効利用を図ることは、各所で検討されてい
る。
Therefore, for example, efforts are being made to effectively utilize aging waste liquid from chromium plating, waste liquid from chromium-containing etching of plastics, and their washing liquids.

しかしながら、これら廃液中には、鉄分とか銅分などの
重金属が常時含有されており、これらの重金属分含有量
が1リットル中log以下程度の場合には、たとえば皮
なめし剤として、そのまゝの使用は、実用上差支えない
ものと見なされている。
However, these waste liquids always contain heavy metals such as iron and copper, and when the content of these heavy metals is less than log of 1 liter, it can be used as a leather tanning agent, for example. Its use is considered to be acceptable in practice.

しかしながら、めっき工場またはエッチング工場の実状
において、貴重高価なクロム分の取扱として、経済的作
業管理上、クロム含有廃液は、所謂老化廃液となるまで
順環使用を経続するために、老化し、そのまゝでは用途
のない廃液中の重金属含有量は、実際上1リットル中2
0g以上の含量に達しているのが現状である。
However, in the actual situation of a plating factory or an etching factory, chromium-containing waste liquid is aged and used continuously until it becomes so-called aged waste liquid due to economical work management and handling of valuable chromium. In reality, the heavy metal content in waste liquid, which has no use as it is, is 2 in 1 liter.
At present, the content has reached 0g or more.

従って、これら廃液をたとえば皮なめし用として使甲せ
んとしても、クロムイオンと重金属イオンは複雑な錯化
合物を形成するために、そのまゝでは使用不可能なこと
は当該業者が充分熟知している事実である。
Therefore, even if these waste liquids were to be used, for example, for leather tanning, those in the industry are well aware that they cannot be used as they are because chromium ions and heavy metal ions form complex complexes. It is a fact.

従って、これら全く利用の方策の立たない重金属高含有
率のクロム酸廃液は、水にて適当に稀釈ならびに還元を
行い、水酸化クロムスラツジとして放棄しているのが実
状である。
Therefore, the actual situation is that these chromic acid waste liquids with a high content of heavy metals, which cannot be used at all, are appropriately diluted with water and reduced, and then discarded as chromium hydroxide sludge.

最近に至り、クロム酸含有廃液の皮なめし用えの利用法
として、廃液の加熱によるクロム酸晶析法とか、カチオ
ン交換樹脂通液法などが考案されているが、前者の方法
は発生廃硫酸の処理等に問題があり、工業的に簡易に実
施することには問題がある。
Recently, methods for using chromic acid-containing waste liquid for leather tanning have been devised, such as the chromic acid crystallization method by heating the waste liquid and the cation exchange resin flow method, but the former method However, there are problems in the processing, etc., and there are problems in implementing it industrially.

また後者の方法は、樹脂の甚だしい劣化が起こること、
ならびに硫酸による樹脂活性化などの手数が必要となり
、面倒な作業管理および運転経費の高騰のために、簡易
に実施はできない実状である。
In addition, the latter method causes severe deterioration of the resin,
In addition, it requires steps such as resin activation with sulfuric acid, and the actual situation is that it cannot be easily implemented due to troublesome work management and rising operating costs.

本発明においては、クロムめっき工場またはプラスチッ
クめっきのエッチング工場より発生するクロム酸含有老
化廃液、あるいはそれぞれの洗滌廃水よりの単一液また
は、任意混合された廃液中、重金属分が1リットル中2
0g以上の含存液より簡易な作業工程により、皮なめし
甲に適する硫酸クロム液の回収を行う方法に関するクロ
ム酸廃液の処理方法に関するものである。
In the present invention, the heavy metal content is 2 in 1 liter of aged waste liquid containing chromic acid generated from a chrome plating factory or a plastic plating etching factory, or a single liquid from each washing waste water, or a mixed waste liquid of any kind.
The present invention relates to a method for treating chromic acid waste liquid, which is related to a method for recovering a chromium sulfate liquid suitable for leather tanning using a simpler work process than containing 0 g or more of liquid.

次に本発明の趣旨について詳細に説明する。Next, the gist of the present invention will be explained in detail.

前述のように、クロムめっき工場またはプラスチックめ
っきのエッチング工場より発生する6価クロム含有酸性
廃液中、特に鉄、銅などの重金属を液1リットル当り2
0g以上を含有する廃液(この廃液には、去れそれの洗
浄水が混合されている場合もある。
As mentioned above, in the acidic waste liquid containing hexavalent chromium generated from a chrome plating factory or an etching factory for plastic plating, heavy metals such as iron and copper are particularly
Waste liquid containing 0g or more (this waste liquid may also contain washed water of any amount left over).

)に対し、先づアルカリとして、ソーダ灰またはカセイ
ソーダ液を処理液の常温下、または少しく加温した状態
の下に加え、液のpHを4〜7の範囲に調整するとき、
液中に随伴する鉄分、銅分などの重金属は塩基性炭酸塩
とか、水酸化物としてゲル状の沈澱物を生成するから、
クロム酸含有液より容易に濾別することができる。
), first add soda ash or caustic soda solution as an alkali to the treatment solution at room temperature or in a slightly heated state, and adjust the pH of the solution to a range of 4 to 7.
Heavy metals such as iron and copper that accompany the liquid form gel-like precipitates as basic carbonates and hydroxides.
It can be easily filtered out from chromic acid-containing liquids.

次に重金属を分別した6価クロム含有清澄濾液に硫酸を
加えて液のpHを0.5〜1.0の範囲に調整し、常法
のブドウ糖(C6H12O6,D−グルコース)による
還元処理、または亜硫酸ガスの導入処理による還元を行
う。
Next, sulfuric acid is added to the hexavalent chromium-containing clear filtrate from which heavy metals have been separated, and the pH of the liquid is adjusted to a range of 0.5 to 1.0. Reduction is performed by introducing sulfur dioxide gas.

このように還元処理され、次でpH調整された硫酸クロ
ム液は皮なめし用に使用することができる。
The chromium sulfate solution thus reduced and then pH-adjusted can be used for leather tanning.

すなわちクロムなめしにおいては、なめし効果を示すの
は3価クロムであり、6価クロムは無価値であり、鉄分
とか銅分などの重金属がなめし液中に存在するときは、
クロム分と反応して複雑な錯化合物が生成し、満足なる
なめし作業はできない。
In other words, in chrome tanning, it is trivalent chromium that exhibits the tanning effect, while hexavalent chromium is worthless, and when heavy metals such as iron and copper are present in the tanning solution,
It reacts with chromium to form complex complexes, making it impossible to perform a satisfactory tanning operation.

本発明においては、クロムめっきの老化廃液とか、プラ
スチックめっきのエッチング廃液として、従来有効なる
処理とか利用法が見出されなかった廃液1リットル当り
20g以上の重金属を含有する液より、工業的に実施容
易な方法により、クロム皮なめし用に適する硫酸第1ク
ロム含有液を収得することができ、皮なめし業界に対し
ても益するところ甚大なる発明に関するものである。
In the present invention, it is possible to industrially use waste liquids containing 20 g or more of heavy metals per liter of waste liquids, such as aging waste liquid from chrome plating or etching waste liquid from plastic plating, for which no effective treatment or use has been found in the past. It is possible to obtain a chromium sulfate-containing liquid suitable for chrome leather tanning by a simple method, and the invention is of great benefit to the leather tanning industry.

次に実施例を示して本発明を説明する。Next, the present invention will be explained with reference to Examples.

実施例 1 クロムめっき工場より排出されるクロムめっき廃老化液
は強酸性であり、遊離酸として、H2SO4換算で80
g/lを含んでおり、その液を分析したところ、次の数
値を示した。
Example 1 The chrome plating waste aging liquid discharged from a chrome plating factory is strongly acidic, and the free acid content is 80% in terms of H2SO4.
g/l, and when the liquid was analyzed, it showed the following values.

Cr6+Fe T−SO4 Zn Cu 比重g/l1
08 14 3.5 1.2 1.5 1.19上記廃
液の1lに対し、液温25℃において、粉状ソーダ灰の
160gを撹拌の下に添加したところ、液のpH=4に
おいて、ゲル状の沈澱を生成した。
Cr6+Fe T-SO4 Zn Cu Specific gravity g/l1
08 14 3.5 1.2 1.5 1.19 When 160 g of powdered soda ash was added to 1 liter of the above waste liquid at a liquid temperature of 25°C under stirring, a gel was formed at a pH of 4. A precipitate of 50% was formed.

次でこの沈澱含有液を涙過したところ透明なクロム含有
液を得た。
Next, this precipitate-containing liquid was filtered to obtain a transparent chromium-containing liquid.

次にこのクロム分含有液中に有在する6価クロムを還元
するために50〜60℃の温溶中で約40分間SO2ガ
スを通じて、還元した。
Next, in order to reduce the hexavalent chromium present in this chromium-containing liquid, SO2 gas was passed through the solution for about 40 minutes in a hot melt at 50 to 60 DEG C. for reduction.

還元反応の終了はヨード法で確認した。次で、約1時間
程度加熱して過剰のSO2ガスを除去した。
Completion of the reduction reaction was confirmed by the iodine method. Next, excess SO2 gas was removed by heating for about 1 hour.

得られた還元クロム液を分析したところ、次に示す結果
を得た。
When the obtained reduced chromium solution was analyzed, the following results were obtained.

(備考) SO2ガス還元法 また同様にして、前記と同じ組成の廃老化液の1lに対
し、炭酸ソーダ粉末180gを同様に添加し、液のpH
=6.5に達したとき、アルカリの添加を止め、生成重
金属沈澱を前同様に濾過した。
(Remarks) SO2 gas reduction method Also, in the same manner, 180 g of soda carbonate powder was added to 1 liter of waste aging liquid with the same composition as above, and the pH of the liquid was adjusted.
=6.5, the addition of alkali was stopped and the heavy metal precipitate formed was filtered as before.

次に得られた透明クロム酸溶液に、濃度15%の硫酸を
加えて液のpHを0.6〜0.8に調整後、ブドウ糖8
5gを加えてクロム分の還元を行い、還元終了液を分析
した。
Next, sulfuric acid with a concentration of 15% was added to the obtained transparent chromic acid solution to adjust the pH of the solution to 0.6 to 0.8.
5 g was added to reduce the chromium content, and the reduced solution was analyzed.

その組成は次に示すとおりである。Its composition is as shown below.

なお上記還元終了液はpH2〜3に調整し、皮かくなめ
し用として使用に供することができる。
The above-mentioned reduced solution can be adjusted to pH 2 to 3 and used for leather tanning.

実施例 2 プラスチックめっきのエッチング工場より排出される次
の分析値を示すエッチング廃液を実施例1におけると同
様に脱重金属ならびにブドウ糖還元法にて処理した。
Example 2 Etching waste liquid discharged from a plastic plating etching factory and showing the following analytical values was treated in the same manner as in Example 1 by the heavy metal removal and glucose reduction method.

すなわち、上記廃液1lに、炭酸ソーダ粉末195gを
添加し、液のpH=6.5に調整し、生成する重金属沈
澱を濾別した後の透明クロム酸溶液に、濃度15%の硫
酸を添加、液のpHを0.6〜0.8に調整した後に、
ブドウ糖の80gを添加して6価クロムの還元を行なっ
た。
That is, 195 g of soda carbonate powder was added to 1 liter of the above waste liquid, the pH of the liquid was adjusted to 6.5, and the resulting heavy metal precipitate was filtered off. To the transparent chromic acid solution, 15% sulfuric acid was added. After adjusting the pH of the liquid to 0.6 to 0.8,
Hexavalent chromium was reduced by adding 80 g of glucose.

この還元終了硫酸クロム液は次の分析値を示した。This reduced chromium sulfate solution showed the following analytical values.

なお上記硫酸クロム溶液は、pH2〜3に調整し、皮か
くなめし用として使用に供することができる。
The above chromium sulfate solution can be adjusted to pH 2 to 3 and used for leather tanning.

Claims (1)

【特許請求の範囲】[Claims] 1 クロムめっき工場より排出されるクロムめっき老化
液、ならびにその水溶液、およびプラスチックめっきの
エッチング工場より排出されるクロム含有エッチング廃
液ならびにその水洗液のうち、これら廃液についての単
一液、もしくは2種以上の混合液よりなるクロム酸含有
廃液成分中、特に鉄、銅などの重金属分を該廃液1リッ
トルのうち、20g以上を含有する廃液に対し、先づカ
セイソーダ若しくはソーダ灰を常温下、若しくは少しく
加温した状態にて添加し、液のpHを4〜7の範囲に調
整し、溶存重金属分をクロム酸含有廃液中より沈澱せし
め、これをr別、除去したる透明P液に対し、含存する
6価クロムを還元するために、常法の還元剤、すなわち
亜硫酸ガスによる還元処理または、先づ硫酸を添加、液
のpHを0.5〜1.0の範囲に調整後、ブドウ糖の添
加による還元処理を行った後、pHを2〜3に調整し、
皮かくなめし用として有害なる重金属ならびに6価クロ
ムを含まない皮なめし用に適する硫酸クロム溶液を、前
記廃液より簡易なる処理工程により、容易に収得するこ
とを特徴とする特に重金属分を廃液1リットル中、20
g以上を含有するクロムめつき老化液またはプラスチッ
クめっきのエッチング廃液ならびにそれぞれの水洗液よ
りなるクロム酸含有廃液より、皮カベなめし用に適する
硫酸クロム溶液を収得することを特徴とするクロム酸廃
液の処理方法。
1 A single liquid or two or more types of chromium plating aging liquid discharged from a chrome plating factory and its aqueous solution, and chromium-containing etching waste liquid discharged from a plastic plating etching factory and its washing liquid. First, caustic soda or soda ash is added to the waste liquid containing 20 g or more of chromic acid-containing waste liquid components, especially heavy metals such as iron and copper, out of 1 liter of the waste liquid at room temperature or slightly added. It is added in a warm state, the pH of the solution is adjusted to a range of 4 to 7, the dissolved heavy metals are precipitated from the chromic acid-containing waste solution, and this is separated and removed from the transparent P solution. In order to reduce hexavalent chromium, a reduction treatment using a conventional reducing agent, that is, sulfur dioxide gas, or by first adding sulfuric acid, adjusting the pH of the solution to a range of 0.5 to 1.0, and then adding glucose. After performing the reduction treatment, adjust the pH to 2 to 3,
A chromium sulfate solution suitable for leather tanning that does not contain heavy metals harmful to leather tanning and hexavalent chromium is easily obtained from the waste liquid through a simple processing process. Middle, 20
A chromic acid waste solution, which is characterized in that a chromium sulfate solution suitable for leather surface tanning is obtained from a chromic acid-containing waste solution consisting of a chromium plating aging solution or a plastic plating etching waste solution containing more than Processing method.
JP54105217A 1979-08-18 1979-08-18 Processing method for chromic acid waste liquid Expired JPS582165B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54105217A JPS582165B2 (en) 1979-08-18 1979-08-18 Processing method for chromic acid waste liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54105217A JPS582165B2 (en) 1979-08-18 1979-08-18 Processing method for chromic acid waste liquid

Publications (2)

Publication Number Publication Date
JPS5632329A JPS5632329A (en) 1981-04-01
JPS582165B2 true JPS582165B2 (en) 1983-01-14

Family

ID=14401495

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54105217A Expired JPS582165B2 (en) 1979-08-18 1979-08-18 Processing method for chromic acid waste liquid

Country Status (1)

Country Link
JP (1) JPS582165B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1198203B (en) * 1986-11-28 1988-12-21 Stoppani Luigi Spa PROCEDURE FOR THE RECOVERY OF CHROMIUM ANHYDRIDE FROM EXHAUSTED AQUEOUS SOLUTIONS OF CHROME BATHS WITH VALORISATION OF RECOVERED CHROME
IT1216507B (en) * 1988-03-23 1990-03-08 Stoppani Luigi Spa PROCEDURE FOR THE RECOVERY OF CHROMIUM DIOXIDE FROM EXHAUSTED AQUEOUS SOLUTIONS OF CHROME BATHS WITH VALORISATION OF RECOVERED CHROME.
KR100401987B1 (en) * 1998-12-16 2003-12-18 주식회사 포스코 A method for preparing chromic acid from electroplating was tewater including hexavalent chrome

Also Published As

Publication number Publication date
JPS5632329A (en) 1981-04-01

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