JPS5814270B2 - Tambakushitsu Shiboubungan Yuuodakuhaisuino Shiyorihouhou - Google Patents

Tambakushitsu Shiboubungan Yuuodakuhaisuino Shiyorihouhou

Info

Publication number
JPS5814270B2
JPS5814270B2 JP50083818A JP8381875A JPS5814270B2 JP S5814270 B2 JPS5814270 B2 JP S5814270B2 JP 50083818 A JP50083818 A JP 50083818A JP 8381875 A JP8381875 A JP 8381875A JP S5814270 B2 JPS5814270 B2 JP S5814270B2
Authority
JP
Japan
Prior art keywords
cod
treatment
precipitate
yuuodakuhaisuino
tambakushitsu
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
JP50083818A
Other languages
Japanese (ja)
Other versions
JPS5225454A (en
Inventor
佐野正勝
清水恵己
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.)
NEC Corp
Original Assignee
Nippon Electric Co 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 Nippon Electric Co Ltd filed Critical Nippon Electric Co Ltd
Priority to JP50083818A priority Critical patent/JPS5814270B2/en
Publication of JPS5225454A publication Critical patent/JPS5225454A/en
Publication of JPS5814270B2 publication Critical patent/JPS5814270B2/en
Expired legal-status Critical Current

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  • Removal Of Specific Substances (AREA)
  • Compounds Of Iron (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)
  • Soft Magnetic Materials (AREA)

Description

【発明の詳細な説明】 乳製品や食肉加工などの食品加工の総合廃水は多量のた
んぱく質および脂肪などを含み、これら廃水は高いCO
Dを示す。
[Detailed description of the invention] General wastewater from food processing such as dairy products and meat processing contains large amounts of protein and fat, and these wastewaters have a high CO2 content.
Indicates D.

これら廃水の処理方法の一つに薬品凝集沈澱法がある。One of the methods for treating these wastewaters is the chemical coagulation sedimentation method.

この処理方法はFe,AIなどの水酸化物が中性付近で
もっている正電荷の示す凝集効果を利用した処理方法で
ある。
This treatment method is a treatment method that utilizes the aggregation effect exhibited by the positive charge that hydroxides such as Fe and AI have near neutrality.

処理薬品としては一般に安価である点から鉄塩が用いら
れている。
Iron salts are generally used as treatment chemicals because they are inexpensive.

この処理方法は他の処理方法、例えば生物処理に比較し
て、処理設備が小さい利点をもつが、処理によって生成
した汚泥の沈降性が悪く、ろ過性が悪いため、汚泥の分
離処理が著しく困難であった。
This treatment method has the advantage of requiring smaller treatment equipment compared to other treatment methods, such as biological treatment, but the sludge produced by the treatment has poor settling and filterability, making it extremely difficult to separate the sludge. Met.

本発明はこれら上記弊害を改善し、乳製品や食肉加工な
どの食品加工廃水など、高いCODを示す廃水を有効に
処理する方法を提供することを目的とするものである。
It is an object of the present invention to provide a method for improving the above-mentioned disadvantages and effectively treating wastewater exhibiting high COD, such as wastewater from food processing such as dairy products and meat processing.

即ち本発明は高いCODを示す汚濁廃水に第一鉄塩およ
びアルカリ性物質を加え酸化性気体を吹き込んで第一鉄
イオンを酸化し最終的に強磁性酸化物を沈澱させると共
にこの沈澱粒子に廃水中の高COD源となっている汚濁
物質を分解吸着除去することを特徴とするものである。
That is, the present invention adds a ferrous salt and an alkaline substance to polluted wastewater exhibiting a high COD, blows in an oxidizing gas to oxidize the ferrous ions, and finally precipitates a ferromagnetic oxide. It is characterized by decomposing and adsorbing and removing pollutants that are a source of high COD.

本発明の方法において生成する沈澱物は強磁性酸化物で
あり、凝集沈澱物法で生成する水酸化沈澱物にくらべて
沈降性が非常によいと共に磁気分離が可能になり、固液
分離が非常に容易になる。
The precipitate produced in the method of the present invention is a ferromagnetic oxide, which has much better sedimentation properties than the hydroxide precipitate produced by the coagulated precipitation method, and magnetic separation is possible, making solid-liquid separation very easy. becomes easier.

即ち本発明の方法は従来の凝集沈澱法にくらべて沈澱物
の分離回収が非常に楽になり、作業効率を著しく増大す
る。
That is, in the method of the present invention, separation and recovery of precipitates is much easier than in the conventional coagulation-sedimentation method, and work efficiency is significantly increased.

また本発明の実施により生成される強磁性酸化物沈澱は
電波吸収材料、磁性流体用原料などとしての再利用が可
能であり、廃棄物の有効利用には誠に好ましいクローズ
ドサイクルをもたらす。
Further, the ferromagnetic oxide precipitate produced by carrying out the present invention can be reused as a radio wave absorbing material, a raw material for magnetic fluid, etc., resulting in a closed cycle that is very favorable for the effective use of waste.

次に本発明の処理方法を説明すると汚濁廃水中のCOD
が100 〜3000ppmを示す牛乳で白濁した廃水
中に硫酸第一鉄などの第一鉄塩を0.0 0 5 〜0
. 5 mol/7相当量を加えて溶解攪拌し、苛性ソ
ーダなどのアルカリ性物質をpHが9〜12になるよう
に加えると濃青緑色を呈した水酸化物沈澱が生成し該液
を40℃以上に加熱して空気等の酸化性ガスを吹込んで
10分から1時間酸化反応すると黒味を帯びた強磁性酸
化物沈澱が生成する。
Next, the treatment method of the present invention will be explained.
Ferrous salts such as ferrous sulfate are added to waste water cloudy with milk with a concentration of 100 to 3000 ppm.
.. Add an amount equivalent to 5 mol/7, dissolve and stir, and add an alkaline substance such as caustic soda so that the pH becomes 9 to 12. A dark blue-green hydroxide precipitate is formed, and the solution is heated to 40°C or higher. When heated and oxidized by blowing in an oxidizing gas such as air for 10 minutes to 1 hour, a blackish ferromagnetic oxide precipitate is produced.

該処理液を磁石で固液分離した上澄液は無色透明で該液
を過マンガン酸カリ法でCOD分析を行なった結果いず
れの場合もCODは20〜25ppm以下であった。
The supernatant liquid obtained by solid-liquid separation of the treated liquid with a magnet was colorless and transparent, and COD analysis of the liquid by the potassium permanganate method showed that the COD was 20 to 25 ppm or less in all cases.

このようにCODが除去されるのは、第一鉄塩、アルカ
リなどによる塩析効果でたんぼく質が分解されると同時
に第一鉄イオンの酸化反応時における酸化効果がCOD
低下に寄与しさらにスピネル型酸化物沈澱(黒色強磁性
酸化物)が生成される段階でこれら分解物が生成沈澱物
に取り込まれるためであろうと考えられる。
COD is removed in this way because proteins are decomposed due to the salting-out effect of ferrous salts, alkalis, etc., and at the same time, the oxidation effect during the oxidation reaction of ferrous ions reduces COD.
It is thought that this is because these decomposition products are incorporated into the precipitate at the stage when spinel-type oxide precipitate (black ferromagnetic oxide) is produced, which contributes to the decrease.

さらに本発明は牛乳等の分析研究を行なう場合によく使
用される重クロム酸カリおよび塩化第二水銀などの重金
属塩が混入した高いCODを示す汚濁廃水処理も可能で
あって前記処理条件下で強磁性酸化物沈澱が生成する過
程でスピネル型酸化物(強磁性酸化物)に重金属が組み
込まれるので汚濁廃水処理と同時に重金属が除去できる
特徴を有しており、重金属の種類としてはカドミウム、
鉛、銅、亜鉛、マンガン、クロム、水銀、鉄、ニッケル
、銀、すす、コバルト、チタン、バナジウム、アルミニ
ウム、ひ素などがあり、アルカリ金属以外はほとんど除
去可能である。
Furthermore, the present invention is also capable of treating polluted wastewater that exhibits high COD and is contaminated with heavy metal salts such as potassium dichromate and mercuric chloride, which are often used when conducting analytical research on milk, etc., and under the above treatment conditions. Heavy metals are incorporated into spinel oxides (ferromagnetic oxides) during the process of forming ferromagnetic oxide precipitates, so heavy metals can be removed at the same time as polluted wastewater treatment.The types of heavy metals include cadmium,
These include lead, copper, zinc, manganese, chromium, mercury, iron, nickel, silver, soot, cobalt, titanium, vanadium, aluminum, arsenic, etc., and almost all except alkali metals can be removed.

なお、本発明の処理に用いる第一鉄塩の量はCOD濃度
、重金属濃度に依存するが第一鉄イオン濃度が0. 0
0 5 mol/73以下になると強磁性酸化物沈澱
の生成が困難になる。
The amount of ferrous salt used in the treatment of the present invention depends on the COD concentration and heavy metal concentration, but when the ferrous ion concentration is 0. 0
When the amount is less than 0 5 mol/73, it becomes difficult to form a ferromagnetic oxide precipitate.

また処理温度も40℃以下では同様に強磁性酸化物沈澱
の生成が困難になり、40℃以上で処理可能であるが、
経済性を加味して好ましくは40℃〜80℃の酸化反応
温度が適している。
Furthermore, if the treatment temperature is 40°C or lower, it will be difficult to generate ferromagnetic oxide precipitates, and although treatment can be performed at 40°C or higher,
In consideration of economic efficiency, an oxidation reaction temperature of 40°C to 80°C is preferably suitable.

なお使用するアルカリ性物質としてはアルカリ金属、ア
ルカリ土類金属等の塩基性物質が用いられ、処理液のp
Hは9〜、12が好ましくpHが9以下の場合およびp
Hが12以上の場合は汚濁廃水中に含まれる重金属が除
去されない場合がある。
The alkaline substances used are basic substances such as alkali metals and alkaline earth metals.
H is preferably 9 to 12, and when the pH is 9 or less and p
When H is 12 or more, heavy metals contained in polluted wastewater may not be removed.

本発明の詳細な説明において廃水中の汚濁物質が排除率
の指標としてCODを用いたが、本発明の方法はBOD
,TOD低下にも同効果を有している。
In the detailed explanation of the present invention, COD was used as an indicator of the removal rate of pollutants in wastewater, but the method of the present invention uses BOD
, it has the same effect on TOD reduction.

以下実施例により本発明についてさらに詳細に説明する
The present invention will be explained in more detail with reference to Examples below.

実施例 I COD約400ppmを示す白濁した牛乳瓶の洗浄水1
lにFe2+濃度が0. 0 1 5 mol/lにな
るように硫酸第一鉄を溶解しIN−NaOH溶液を42
ml加えた後昇温し40℃で1時間空気を吹き込んで酸
化を行なった。
Example I Cloudy milk bottle wash water 1 showing COD of about 400 ppm
When the Fe2+ concentration is 0. Dissolve ferrous sulfate to a concentration of 0.15 mol/l and add 42% of the IN-NaOH solution.
After adding ml, the temperature was raised to 40° C. and air was blown into the solution for 1 hour to carry out oxidation.

酸化反応後黒色の強磁性沈澱物が得られた。A black ferromagnetic precipitate was obtained after the oxidation reaction.

溶液中に着磁したバリウムフエライトを入れて沈澱物を
分離した。
Magnetized barium ferrite was placed in the solution to separate the precipitate.

分離液は無色透明であった。分離後、液の一部を採取し
原子吸光光度法によって残存金属濃度を調べたが、有害
金属はFeを含めて検出限界以下であった。
The separated liquid was colorless and transparent. After separation, a portion of the liquid was sampled and the remaining metal concentration was examined by atomic absorption spectrophotometry, and the toxic metals, including Fe, were below the detection limit.

さらにCODは15ppmであって浄化率は約96%で
あった。
Furthermore, COD was 15 ppm and the purification rate was about 96%.

実施例 2 牛の生肉汁を含んだCOD約1000ppmを示す淡黄
色の廃水1lにFe2+濃度が0.05mol/lにな
るように塩化第一鉄を溶解し、10N−NaOH溶液を
12771l加えた後昇温し60℃で1時間空気を吹き
込んで酸化を行なった。
Example 2 Ferrous chloride was dissolved in 1 liter of pale yellow wastewater containing raw beef juice and having a COD of approximately 1000 ppm so that the Fe2+ concentration was 0.05 mol/l, and 12,771 liters of 10N-NaOH solution was added. The temperature was raised to 60° C. and air was blown into the solution for 1 hour to perform oxidation.

酸化反応後、黒色の強磁性沈澱物が得られた。After the oxidation reaction, a black ferromagnetic precipitate was obtained.

沈澱物を磁気分離した液は無色透明であり、原子吸光光
度法で残存金属濃度を調べたところFe濃度0.08p
pmで、他の有害金属は検出限界以下であった。
The liquid obtained by magnetically separating the precipitate was clear and colorless, and when the residual metal concentration was examined by atomic absorption spectrophotometry, the Fe concentration was 0.08p.
pm, and other toxic metals were below detection limits.

Claims (1)

【特許請求の範囲】[Claims] 1 たんぱく質・脂肪含有汚濁廃水中に第一鉄イオン濃
度が0.005mol/l以上になるように第一鉄塩を
加え溶解攪拌し、溶液中の陰イオンに対して尚量以上の
アルカリ性物質を加えpHを9〜12とし、40℃以上
に加熱保持して空気などの酸化性ガスを吹込み酸化し最
終的に強磁性酸化物沈澱(スピネル化合物)を生成させ
ると共に廃水中の汚濁物質を分解吸着除去することを特
徴とするたんぱく質・脂肪分含有汚濁廃水の処理方法。
1 Add ferrous salt to polluted wastewater containing protein and fat so that the ferrous ion concentration is 0.005 mol/l or more, dissolve and stir, and add an alkaline substance in an amount greater than the required amount to the anions in the solution. The pH is adjusted to 9 to 12, heated and held at 40°C or above, and oxidized by blowing in oxidizing gas such as air. Finally, a ferromagnetic oxide precipitate (spinel compound) is generated and pollutants in the wastewater are decomposed. A method for treating polluted wastewater containing protein and fat, which is characterized by adsorption and removal.
JP50083818A 1975-07-08 1975-07-08 Tambakushitsu Shiboubungan Yuuodakuhaisuino Shiyorihouhou Expired JPS5814270B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50083818A JPS5814270B2 (en) 1975-07-08 1975-07-08 Tambakushitsu Shiboubungan Yuuodakuhaisuino Shiyorihouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50083818A JPS5814270B2 (en) 1975-07-08 1975-07-08 Tambakushitsu Shiboubungan Yuuodakuhaisuino Shiyorihouhou

Publications (2)

Publication Number Publication Date
JPS5225454A JPS5225454A (en) 1977-02-25
JPS5814270B2 true JPS5814270B2 (en) 1983-03-18

Family

ID=13813253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50083818A Expired JPS5814270B2 (en) 1975-07-08 1975-07-08 Tambakushitsu Shiboubungan Yuuodakuhaisuino Shiyorihouhou

Country Status (1)

Country Link
JP (1) JPS5814270B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS544457A (en) * 1977-06-14 1979-01-13 Japan Metals & Chem Co Ltd Method of removing detrimental materials as arsenic and hydrogen sulfide or like
JPS546348A (en) * 1977-06-14 1979-01-18 Japan Metals & Chem Co Ltd Method of removing and recovering detrimental materials as arsenic and hydrogen sulfide or like
JPS6132931Y2 (en) * 1978-06-20 1986-09-25

Also Published As

Publication number Publication date
JPS5225454A (en) 1977-02-25

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