JP2001129565A - Treatment of wastewater containing nitrate nitrogen - Google Patents
Treatment of wastewater containing nitrate nitrogenInfo
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- JP2001129565A JP2001129565A JP31334099A JP31334099A JP2001129565A JP 2001129565 A JP2001129565 A JP 2001129565A JP 31334099 A JP31334099 A JP 31334099A JP 31334099 A JP31334099 A JP 31334099A JP 2001129565 A JP2001129565 A JP 2001129565A
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- nitrate nitrogen
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Abstract
(57)【要約】
【課題】 硝酸性窒素を含有する排水を小型の装置で簡
単に処理でき、硝酸性窒素量の変化等の負荷の変動に対
して安定な処理が可能であって、高濃度の硝酸性窒素も
効果的に処理することができる方法を提供する。
【解決手段】 硝酸性窒素を含有する被処理排水中にヒ
ドラジンと2価の銅イオンを添加して、ラネーニッケル
触媒又はルテニウム触媒と接触させ、硝酸性窒素を還元
処理する。ヒドラジン添加量は被処理排水中の硝酸性窒
素の3〜4倍当量、銅イオン添加量は被処理排水中の濃
度で0.2〜3mg/lとする。また、被処理排水はp
H11.7以上に調整することが好ましい。(57) [Summary] [PROBLEMS] To efficiently treat wastewater containing nitrate nitrogen with a small device, and to perform stable treatment against load fluctuations such as changes in the amount of nitrate nitrogen. Provided is a method capable of effectively treating even concentrations of nitrate nitrogen. SOLUTION: Hydrazine and divalent copper ions are added to wastewater containing nitrate nitrogen to be brought into contact with a Raney nickel catalyst or a ruthenium catalyst to reduce nitrate nitrogen. The amount of hydrazine added is 3 to 4 equivalents of nitrate nitrogen in the waste water to be treated, and the amount of copper ion added is 0.2 to 3 mg / l in the concentration in the waste water to be treated. The wastewater to be treated is p
It is preferable to adjust H11.7 or more.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、硝酸を大量に使用
する事業所あるいは工場から排出される排水、特に高濃
度の硝酸性窒素を含有する排水の処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating wastewater discharged from a business or a factory using a large amount of nitric acid, particularly wastewater containing a high concentration of nitrate nitrogen.
【0002】[0002]
【従来の技術】排水中に含まれる硝酸性窒素の処理方法
としては、微生物の脱窒能を利用した生物学的処理方
法、イオン交換法、逆浸透法、電気透析法等の物理化学
的処理方法、水素ガスを被処理排水中に加圧溶解させて
触媒の存在下に硝酸性窒素を還元する化学的処理方法等
がある。2. Description of the Related Art As a method for treating nitrate nitrogen contained in wastewater, there are physicochemical treatments such as a biological treatment method utilizing the denitrification ability of microorganisms, an ion exchange method, a reverse osmosis method, and an electrodialysis method. And a chemical treatment method of reducing the nitrate nitrogen in the presence of a catalyst by dissolving hydrogen gas in the wastewater to be treated under pressure.
【0003】生物学的処理方法は、ランニングコストが
安価で最も普及している方法であるが、反応速度が小さ
いため、大量の排水処理には大型の処理装置を必要とす
る。また、約1g/l以上の高濃度の硝酸性窒素を含有
する排水に適用することは難しく、被処理排水中の硝酸
性窒素濃度の変化等の処理装置に対する負荷の変動によ
って処理性能が不安定になり易い。[0003] The biological treatment method is the most widespread method because of its low running cost. However, since the reaction speed is low, a large-sized wastewater treatment apparatus requires a large-sized treatment apparatus. Further, it is difficult to apply the method to wastewater containing a high concentration of nitrate nitrogen of about 1 g / l or more. Easy to be.
【0004】物理化学的処理方法は、処理装置が小型で
あって良く、確実な処理が期待できる方法である。しか
しながら、この方法は水中の硝酸性窒素を分離・濃縮す
る方法であるため、最終的に硝酸性窒素が濃縮された液
の処理が別途必要となり、根本的には硝酸性窒素を処理
していることにならない。[0004] The physicochemical processing method is a method in which a processing apparatus may be small and reliable processing can be expected. However, since this method separates and concentrates nitrate nitrogen in water, it is necessary to separately treat a liquid in which nitrate nitrogen is finally concentrated, and basically treats nitrate nitrogen. It doesn't matter.
【0005】一方、化学的処理方法は、排水中の硝酸性
窒素の還元にクリーンな水素ガスを使用すること、生物
学的処理方法と比較して反応速度が大きいため装置が小
型化できること等の特徴がある。しかし、水素ガスの水
への溶解度が低いため、生物学的処理方法と同様、高濃
度の硝酸性窒素を含有する排水を処理することは非常に
困難である。On the other hand, the chemical treatment method uses clean hydrogen gas for the reduction of nitrate nitrogen in wastewater, and can reduce the size of the apparatus because the reaction rate is higher than that of the biological treatment method. There are features. However, due to the low solubility of hydrogen gas in water, it is very difficult to treat wastewater containing high concentrations of nitrate nitrogen, as in biological treatment.
【0006】[0006]
【発明が解決しようとする課題】本発明は、このような
従来の事情を考慮して、硝酸性窒素を含有する排水を小
型の装置で簡単に処理でき、硝酸性窒素濃度の変化等の
処理装置への負荷の変動に対して安定な処理が可能であ
って、且つ高濃度の硝酸性窒素も効果的に処理すること
ができる方法を提供することを目的とする。SUMMARY OF THE INVENTION In view of the above-mentioned circumstances, the present invention can easily treat wastewater containing nitrate nitrogen with a small apparatus, and can treat the wastewater such as a change in the concentration of nitrate nitrogen. It is an object of the present invention to provide a method capable of performing a stable treatment with respect to fluctuations in the load on the apparatus and effectively treating a high concentration of nitrate nitrogen.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するた
め、本発明が提供する硝酸性窒素含有排水の処理方法に
おいては、被処理排水にヒドラジンと2価の銅イオンを
添加して、ラネーニッケル触媒又はルテニウム触媒と接
触させることを特徴とする。In order to achieve the above object, the present invention provides a method for treating a nitrate-nitrogen-containing wastewater, which comprises adding hydrazine and divalent copper ions to the wastewater to be treated to form a Raney nickel catalyst. Alternatively, the catalyst is brought into contact with a ruthenium catalyst.
【0008】[0008]
【発明の実施の形態】本発明は、排水中に含まれる硝酸
性窒素を化学的に処理する方法であって、水素供与体と
してヒドラジンを添加し、ラネーニッケル触媒又はルテ
ニウム触媒を用いて、硝酸性窒素を化学的に窒素
(N2)に還元するものである。尚、触媒と被処理排水
の接触方法は、バッチ式でも連続式でも良い。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for chemically treating nitrate nitrogen contained in waste water, wherein hydrazine is added as a hydrogen donor and nitrate is added using a Raney nickel catalyst or ruthenium catalyst. Nitrogen is chemically reduced to nitrogen (N 2 ). The contact method between the catalyst and the waste water to be treated may be a batch type or a continuous type.
【0009】水素供与体として被処理排水に添加するヒ
ドラジンは、水への溶解度が極めて大きいので、高濃度
の硝酸性窒素を含有する排水の処理にも有効である。し
かし、添加量が多すぎると経済的に不利となるばかりで
なく、アンモニアの生成量が増加する。アンモニアが被
処理排水中に残存すると全窒素成分の除去が不充分とな
るため、アンモニアの生成を抑制することが望ましい。
一方、ヒドラジン添加量が少ないと、硝酸性窒素の還元
が不十分のままヒドラジンが枯渇し、それ以上の硝酸性
窒素の還元が進行しない。このことから、ヒドラジン添
加量は、被処理排水中の硝酸性窒素に対して3〜4倍当
量とすることが望ましい。Hydrazine, which is added to the wastewater to be treated as a hydrogen donor, has an extremely high solubility in water, and is therefore effective for treating wastewater containing a high concentration of nitrate nitrogen. However, if the addition amount is too large, it is not only economically disadvantageous but also the amount of produced ammonia increases. If ammonia remains in the wastewater to be treated, the removal of all nitrogen components becomes insufficient, so it is desirable to suppress the generation of ammonia.
On the other hand, when the amount of hydrazine added is small, hydrazine is depleted while the reduction of nitrate nitrogen is insufficient, and further reduction of nitrate nitrogen does not proceed. For this reason, the amount of hydrazine added is desirably 3 to 4 times the equivalent of nitrate nitrogen in the wastewater to be treated.
【0010】上記ラネーニッケル触媒とルテニウム触媒
は、いずれも硝酸性窒素の還元を促進する効果を有して
いるが、ラネーニッケル触媒の方がより効果的である。
ラネーニッケル触媒は、ニッケルとアルミニウムの合金
からアルミニウムを溶出することによって得られ、有機
化合物の水素化用として広く使用されている。また、ル
テニウム触媒は、アルミナ等の担体にルテニウムを担持
したものである。Although both the Raney nickel catalyst and the ruthenium catalyst have the effect of promoting the reduction of nitrate nitrogen, the Raney nickel catalyst is more effective.
Raney nickel catalysts are obtained by eluting aluminum from an alloy of nickel and aluminum and are widely used for hydrogenating organic compounds. The ruthenium catalyst is obtained by supporting ruthenium on a carrier such as alumina.
【0011】本発明方法においては、更に硝酸性窒素の
還元を促進するため、被処理排水に2価の銅イオンを添
加する。2価の銅イオンは、塩化銅、硝酸銅等の形で添
加することができる。銅イオンの添加量は、多いほど反
応が促進されるが、排水基準を定める総理府令別表2に
記載されている銅含有量が3mg/lであることを勘案
すると、被処理排水中の濃度で0.2〜3mg/lの範
囲が望ましい。In the method of the present invention, divalent copper ions are added to the wastewater to be treated in order to further promote the reduction of nitrate nitrogen. Divalent copper ions can be added in the form of copper chloride, copper nitrate or the like. The more copper ion is added, the more the reaction is promoted. However, considering that the copper content described in Appendix 2 of the Prime Minister's Ordinance that sets wastewater standards is 3 mg / l, the concentration in the treated wastewater is A range of 0.2 to 3 mg / l is desirable.
【0012】また、被処理排水のpHは11.7以上に
調整することが好ましい。被処理排水のpHが11.7
未満では、硝酸性窒素の還元が不十分となるからであ
る。尚、被処理排水のpH調整は、水酸化ナトリウム、
硫酸等を添加して行う。It is preferable that the pH of the waste water to be treated is adjusted to 11.7 or more. PH of treated wastewater is 11.7
If the amount is less than the above, the reduction of the nitrate nitrogen becomes insufficient. The pH of the waste water to be treated is adjusted by sodium hydroxide,
This is performed by adding sulfuric acid or the like.
【0013】[0013]
【実施例】実施例1 触媒の違いによる硝酸性窒素の還元処理促進作用を試験
するために、Ruをアルミナ担体に0.5重量%の割合
で担持した触媒、及びラネーニッケル触媒を用意した。【Example】Example 1 Tests the effect of different catalysts to promote nitrate nitrogen reduction
In order to make Ru the alumina carrier 0.5% by weight
, And a Raney nickel catalyst.
【0014】次に、pH12.7に調整した1mol/
lの硝酸ナトリウム溶液100mlに、塩化銅(II)溶液
(200mgCu/l)を1ml、水和ヒドラジン試薬
(20mol/l)を15ml、上記各触媒のいずれか
を乾燥重量で0.5g加え、溶液を35℃に保持しなが
ら4時間撹拌した。Next, 1 mol / mol adjusted to pH 12.7
To 100 ml of sodium nitrate solution, 1 ml of copper (II) chloride solution (200 mg Cu / l), 15 ml of hydrazine hydrate reagent (20 mol / l), and 0.5 g of each of the above catalysts were added in a dry weight of 0.5 g. Was stirred for 4 hours while maintaining the temperature at 35 ° C.
【0015】試験終了後、溶液中に残存する硝酸イオン
濃度を分析し、その結果を触媒なしの場合と共に、下記
表1に示した。表1の結果から、いずれの触媒も硝酸性
窒素の還元反応を促進する作用を有するが、中でもラネ
ーニッケル触媒が最も反応促進能力が高いことが分か
る。After the test was completed, the concentration of nitrate ions remaining in the solution was analyzed, and the results are shown in Table 1 below together with the case without a catalyst. From the results in Table 1, it can be seen that all of the catalysts have an action of promoting the reduction reaction of nitrate nitrogen, and among them, the Raney nickel catalyst has the highest reaction promoting ability.
【0016】[0016]
【表1】 Ru触媒 ラネーNi触媒 触媒なし 残存硝酸性窒素濃度(mol/l) 0.2 <2×10−5 0.95[Table 1]Ru catalyst Raney Ni catalyst Without catalyst Residual nitrate nitrogen concentration (mol / l) 0.2 <2 × 10-5 0.95
【0017】実施例2 ラネーニッケル触媒を使用し、ヒドラジンの添加量を下
記表2に示すように変化させた以外は上記実施例1と同
様にして、硝酸性窒素の還元処理を行った。即ち、pH
12.7に調整した1mol/lの硝酸ナトリウム溶液
100mlに、塩化銅(II)溶液(200mgCu/l)
を1ml、水和ヒドラジン試薬(20mol/l)を下
記表2に示す添加量、ラネーニッケル触媒を0.5g加
え、溶液を35℃に保持しながら4時間撹拌した。[0017]Example 2 Use Raney nickel catalyst and reduce the amount of hydrazine added.
Same as in Example 1 except that it was changed as shown in Table 2.
Thus, reduction treatment of nitrate nitrogen was performed. That is, pH
1mol / l sodium nitrate solution adjusted to 12.7
100 ml of copper (II) chloride solution (200 mg Cu / l)
1 ml, hydrated hydrazine reagent (20 mol / l)
0.5 g of Raney nickel catalyst was added in the amount shown in Table 2.
The solution was stirred for 4 hours while maintaining the solution at 35 ° C.
【0018】試験終了後、溶液中に残存する硝酸イオ
ン、アンモニア及びヒドラジンの各濃度を分析し、得ら
れた結果を下記表2に併せて示した。この結果から分か
るように、硝酸性窒素に対するヒドラジン添加量は、2
倍当量では硝酸性窒素の処理が不十分なまま反応が終了
するが、3倍当量以上であれば硝酸性窒素の処理は十分
に達成される。しかし、ヒドラジン添加量が増加すると
アンモニア生成量が増大する傾向にあり、残存アンモニ
ア量を抑制するためには、ヒドラジン添加量を硝酸性窒
素に対して3〜4倍当量とすることが望ましい。After the test was completed, the concentrations of nitrate ion, ammonia and hydrazine remaining in the solution were analyzed, and the results obtained are shown in Table 2 below. As can be seen from the results, the amount of hydrazine added to nitrate nitrogen was 2
With double equivalents, the reaction is completed with insufficient treatment of nitrate nitrogen, but with three equivalents or more, treatment of nitrate nitrogen is sufficiently achieved. However, as the amount of hydrazine added increases, the amount of ammonia produced tends to increase. In order to suppress the amount of residual ammonia, the amount of hydrazine added is desirably 3 to 4 times the equivalent of nitrate nitrogen.
【0019】[0019]
【表2】 ヒドラジン添加量 10ml(2倍当量) 15ml(3倍当量) 20ml(4倍当量) 残存硝酸性窒素濃度(mol/l) 0.04 <2×10−5 <2×10−5 残存アンモニア濃度(mol/l) 0.4 0.4 0.8 残存ヒドラジン濃度(mol/l) <3×10−5 2×10−4 2×10−4 [Table 2]Hydrazine addition amount 10 ml (2 equivalents) 15 ml (3 equivalents) 20 ml (4 equivalents) Residual nitrate nitrogen concentration (mol / l) 0.04 <2 × 10-5 <2 × 10-5 Residual ammonia concentration (mol / l) 0.4 0.4 0.8 Residual hydrazine concentration (mol / l) <3 × 10-5 2 × 10-4 2 × 10-4
【0020】実施例3 pH12.7に調整した1mol/lの硝酸ナトリウム
溶液及び0.1mol/lの硝酸ナトリウム溶液の各1
00mlに、それぞれ塩化銅(II)溶液(200mgCu
/l)を1ml、水和ヒドラジン試薬(200mol/
l)を硝酸性窒素の3倍当量、ラネーニッケル触媒を
0.5g加え、溶液を35℃に保持しながら4時間撹拌
した。[0020]Example 3 1 mol / l sodium nitrate adjusted to pH 12.7
Solution and 0.1 mol / l sodium nitrate solution
In 200 ml of copper (II) chloride solution (200 mg Cu
/ L) and 1 ml of a hydrated hydrazine reagent (200 mol / l).
l) with 3 equivalents of nitrate nitrogen and Raney nickel catalyst
Add 0.5 g and stir for 4 hours while keeping the solution at 35 ° C
did.
【0021】試験終了後、溶液中に残存する硝酸イオン
濃度を分析し、得られた結果を下記表3に示した。この
結果から分かるように、被処理水中の硝酸性窒素濃度の
変動に対し、安定した処理性能が得られることが確認さ
れた。After the test was completed, the concentration of nitrate ions remaining in the solution was analyzed, and the obtained results are shown in Table 3 below. As can be seen from these results, it was confirmed that stable treatment performance was obtained with respect to fluctuations in the concentration of nitrate nitrogen in the water to be treated.
【0022】[0022]
【表3】 初期硝酸性窒素濃度 0.1mol/l 1.0mol/l 残存硝酸性窒素濃度(mol/l) <2×10−5 <2×10−5 [Table 3]Initial nitrate nitrogen concentration 0.1mol / l 1.0mol / l Residual nitrate nitrogen concentration (mol / l) <2 × 10-5 <2 × 10-5
【0023】実施例4 pH12.7に調整した1mol/lの硝酸ナトリウム
溶液100mlに、下記表4に示す添加量で塩化銅(II)
溶液(200mgCu/l)を添加すると共に、水和ヒ
ドラジン試薬(20mol/l)を硝酸性窒素の3倍当
量、ラネーニッケル触媒を0.5g加え、溶液を35℃
に保持ししながら4時間撹拌した。[0023]Example 4 1 mol / l sodium nitrate adjusted to pH 12.7
Copper (II) chloride was added to 100 ml of the solution in the amount shown in Table 4 below.
Solution (200 mg Cu / l) and
The drazine reagent (20mol / l) is 3 times equivalent to nitrate nitrogen
0.5 g of Raney nickel catalyst was added and the solution was brought to 35 ° C.
While stirring for 4 hours.
【0024】試験終了後、溶液中に残存する硝酸イオン
濃度を分析し、得られた結果を下記表4に併せて示し
た。この結果から、2価銅イオンの添加は硝酸性窒素の
処理を促進する効果を有すること、その効果は銅イオン
の添加量が多いほど大きく、溶液中の濃度で約0.2m
g/l(塩化銅溶液0.1ml)以上で硝酸性窒素の還
元処理が効率良く行われることが分かる。After the test was completed, the concentration of nitrate ions remaining in the solution was analyzed, and the results obtained are shown in Table 4 below. From these results, it can be seen that the addition of divalent copper ions has the effect of accelerating the treatment of nitrate nitrogen. The effect is greater as the amount of copper ions added is greater, and the concentration in the solution is about 0.2 m.
It can be seen that nitrate nitrogen reduction treatment is efficiently performed at g / l (0.1 ml of copper chloride solution) or more.
【0025】[0025]
【表4】 塩化銅溶液添加量 0 0.1ml 1.0ml 残存硝酸性窒素濃度(mol/l) 1 <2×10−5 <2×10−5 [Table 4]Copper chloride solution addition amount 0 0.1ml 1.0ml Residual nitrate nitrogen concentration (mol / l) 1 <2 × 10-5 <2 × 10-5
【0026】実施例5 下記表5に示すpHに調整した1mol/lの硝酸ナト
リウム溶液100mlに、それぞれ塩化銅(II)溶液(2
00mgCu/l)を1ml、水和ヒドラジン試薬(2
0mol/l)を硝酸性窒素の3倍当量、ラネーニッケ
ル触媒を0.5g加え、溶液を35℃に保持しながら4
時間撹拌した。[0026]Example 5 1 mol / l sodium nitrate adjusted to the pH shown in Table 5 below
Copper chloride (II) solution (2
1 mg of hydrazine reagent (2 mg
0 mol / l) 3 times equivalent of nitrate nitrogen, Raneynicke
0.5 g catalyst was added and the solution was kept at 35 ° C. for 4 hours.
Stirred for hours.
【0027】試験終了後、溶液中に残存する硝酸イオン
濃度を分析し、得られた結果を下記表5に併せて示し
た。この結果から分かるように、溶液のpHが11.7
未満では硝酸性窒素の還元処理が不十分であるが、pH
11.7以上では残留硝酸性窒素濃度が定量下限であっ
た。After the test was completed, the concentration of nitrate ions remaining in the solution was analyzed, and the obtained results are shown in Table 5 below. As can be seen from the results, the pH of the solution was 11.7.
If it is less than the above, the reduction treatment of nitrate nitrogen is insufficient.
Above 11.7, the concentration of residual nitrate nitrogen was at the lower limit of quantification.
【0028】[0028]
【表5】 溶液のpH 10.7 11.7 12.7 13.7 残存硝酸性窒素濃度(mol/l) 0.05 <2×10−5 <2×10−5 <2×10−5 [Table 5]Solution pH 10.7 11.7 12.7 13.7 Residual nitrate nitrogen concentration (mol / l) 0.05 <2 × 10-5 <2 × 10-5 <2 × 10-5
【0029】尚、上記各実施例では、ヒドラジンとして
水和ヒドラジン試薬を使用し、また2価の銅イオンは塩
化銅の形で添加しているが、いずれも本発明においては
これらに限定するものではない。In each of the above embodiments, a hydrated hydrazine reagent is used as hydrazine, and divalent copper ions are added in the form of copper chloride. However, the present invention is not limited to these. is not.
【0030】[0030]
【発明の効果】本発明によれば、排水中に含まれる硝酸
性窒素を化学的処理方法により、小型の装置を用いて簡
単に窒素にまで還元処理でき、排水中の硝酸性窒素量の
変化等の処理装置への負荷の変動に対して安定した処理
を行うことが可能であるうえ、1g/l以上の高濃度の
硝酸性窒素も効果的に処理することができる。According to the present invention, nitrate nitrogen contained in wastewater can be easily reduced to nitrogen by a chemical treatment method using a small apparatus, and the amount of nitrate nitrogen in wastewater can be changed. In addition, it is possible to perform a stable process with respect to a change in the load on the processing apparatus, and also to effectively process a high-concentration nitrate nitrogen of 1 g / l or more.
Claims (4)
て、被処理排水にヒドラジンと2価の銅イオンを添加し
て、ラネーニッケル触媒又はルテニウム触媒と接触させ
ることを特徴とする硝酸性窒素含有排水の処理方法。In the treatment of wastewater containing nitrate nitrogen, hydrazine and divalent copper ions are added to the wastewater to be treated, and the wastewater is brought into contact with a Raney nickel catalyst or a ruthenium catalyst. Processing method.
含まれる硝酸性窒素の3〜4倍当量とすることを特徴と
する、請求項1に記載の硝酸性窒素含有排水の処理方
法。2. The method for treating nitrate nitrogen-containing wastewater according to claim 1, wherein the amount of hydrazine to be added is 3 to 4 times the equivalent of nitrate nitrogen contained in the wastewater to be treated.
中の濃度で0.2〜3mg/lとすることを特徴とす
る、請求項1又は2に記載の硝酸性窒素含有排水の処理
方法。3. The wastewater containing nitrate nitrogen according to claim 1, wherein the amount of the divalent copper ion added is 0.2 to 3 mg / l in the wastewater to be treated. Processing method.
することを特徴とする、請求項1〜3のいずれかに記載
の硝酸性窒素含有排水の処理方法。4. The method for treating nitrate nitrogen-containing wastewater according to claim 1, wherein the pH of the wastewater to be treated is adjusted to 11.7 or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31334099A JP2001129565A (en) | 1999-11-04 | 1999-11-04 | Treatment of wastewater containing nitrate nitrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31334099A JP2001129565A (en) | 1999-11-04 | 1999-11-04 | Treatment of wastewater containing nitrate nitrogen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2001129565A true JP2001129565A (en) | 2001-05-15 |
Family
ID=18040077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31334099A Pending JP2001129565A (en) | 1999-11-04 | 1999-11-04 | Treatment of wastewater containing nitrate nitrogen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2001129565A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004020347A1 (en) * | 2002-08-29 | 2004-03-11 | Sumitomo Metal Mining Co., Ltd. | Method of treating waste water containing high level nitrate-nitrogen |
-
1999
- 1999-11-04 JP JP31334099A patent/JP2001129565A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004020347A1 (en) * | 2002-08-29 | 2004-03-11 | Sumitomo Metal Mining Co., Ltd. | Method of treating waste water containing high level nitrate-nitrogen |
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