JP2000334478A - Physicochemical method for removal of nitrate nitrogen in water and denitrifying apparatus - Google Patents

Physicochemical method for removal of nitrate nitrogen in water and denitrifying apparatus

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Publication number
JP2000334478A
JP2000334478A JP19221499A JP19221499A JP2000334478A JP 2000334478 A JP2000334478 A JP 2000334478A JP 19221499 A JP19221499 A JP 19221499A JP 19221499 A JP19221499 A JP 19221499A JP 2000334478 A JP2000334478 A JP 2000334478A
Authority
JP
Japan
Prior art keywords
water
nitrate ions
nitrogen
hydrogen
nitrate
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
Application number
JP19221499A
Other languages
Japanese (ja)
Inventor
Chikashi Kamimura
親士 上村
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.)
JOHO KAGAKU KENKYUSHO KK
Information Science Research Institute
Original Assignee
JOHO KAGAKU KENKYUSHO KK
Information Science Research Institute
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 JOHO KAGAKU KENKYUSHO KK, Information Science Research Institute filed Critical JOHO KAGAKU KENKYUSHO KK
Priority to JP19221499A priority Critical patent/JP2000334478A/en
Publication of JP2000334478A publication Critical patent/JP2000334478A/en
Pending 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

PROBLEM TO BE SOLVED: To remove nitrate nitrogen contained in underground water, or the like, by blowing gaseous hydrogen into the water containing nitrate ions and electrochemically converting the nitrate ions to gaseous nitrogen on a catalyst under reducing conditions. SOLUTION: Water containing nitrate ions is pre-heated in a warming apparatus 1, a small amount of gaseous hydrogen is blown into the water in a gaseous hydrogen mixing and saturating apparatus 2 and the water is saturated with hydrogen by high-speed stirring to adjust the redox potential of the hydrogen- saturated water below that of water. In a denitrifying apparatus 3, the water is irradiated with short wavelength light such as UV on a catalyst under reducing conditions, electric current is supplied between electrodes and electromagnetic field conversion is carried out to excite and react the nitrate ions and hydrogen atoms and the nitrate ions are reduced and discharged as gaseous nitrogen into the air. The water freed of nitrate nitrogen is sent to a treated water oxidation acclimation apparatus 4, where oxygen is blown into the water in the reduced state to convert and acclimate to an oxidized state. In this way, the nitrate nitrogen included in underground water, or the like, is removed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】近年世界的な産業の発達、人口の
急増に伴ない、硝酸による水質汚染が進行し、ヨーロッ
パや日本では硝酸による地下水汚染も激化しつつある。
それは、水系の環境汚染物質になっているし尿、生活排
水等都市汚水処理水、畜産排泄物処理液、産業排出処理
水等で排出された窒素及び肥料に由来する窒素が硝酸化
成作用により最終的に硝酸に変化したものが主体であ
る。これは飲料水としてNO濃度が10ppm以下に
規制されている。本発明は、湖沼、河川水、地下水等に
溶解している硝酸態窒素を除去する技術であり、水道水
等の飲用直前における水の浄化にも応用することができ
る。特に地下水の汚染防止に効果が有り、硝酸態窒素の
除去を排水前の段階で低コストで効率良く継続除去する
分野にも応用される。また、環境問題として多くの論議
がなされる、湖沼等内水系、閉鎖水系の水質浄化を目指
し、湖沼の循環式水流システムとフィルターシステムの
組み合わせにより水系の除窒素の効率を従来なかった水
準に高めることを可能としている。このように河川、湖
沼、海域更には地下水から硝酸態窒素を除去する基礎的
技術を提供し、将来はその技術改良によって莫大な量の
水の処理が可能と考えられる。即ち、枯渇する水資源の
利用範囲を拡大する有効な手段としての展望がある。
[Industrial applications] In recent years, with the development of industry worldwide and the rapid increase in population, water pollution by nitric acid has progressed, and groundwater pollution by nitric acid in Europe and Japan is also intensifying.
This is because nitrogen discharged from human wastewater, such as human wastewater, domestic wastewater, which is a water-based environmental pollutant, livestock wastewater treatment liquid, industrial wastewater treatment water, etc., and nitrogen derived from fertilizers are finally converted by nitrification. It is mainly converted to nitric acid. This is regulated as drinking water with a NO 3 concentration of 10 ppm or less. The present invention is a technique for removing nitrate nitrogen dissolved in lakes, marshes, river water, groundwater, and the like, and can be applied to purification of water immediately before drinking tap water and the like. It is particularly effective in preventing groundwater pollution, and is also applied to the field of removing nitrate nitrogen efficiently and efficiently at low cost before drainage. In addition, with the aim of purifying the water quality of inland water systems such as lakes and marshes and closed water systems, which are widely discussed as environmental problems, the efficiency of nitrogen removal in water systems is improved to a level never before by combining a circulating water flow system and a filter system for lakes and marshes. It is possible. As described above, basic technology for removing nitrate nitrogen from rivers, lakes, marshes, sea areas, and groundwater is provided, and it is thought that an enormous amount of water can be treated in the future by improving the technology. In other words, there is a prospect as an effective means for expanding the use range of depleted water resources.

【0002】[0002]

【従来の技術と問題点】過去において産業における溶液
の硝酸除去(14件)や環境水系の水質浄化技術は多く
の特許と実用新案が提案されている。それらの技術の内
容は、し尿、畜産排泄物に含まれる窒素を除去する技術
としては、硝化作用を受ける前のアンモニア態窒素の段
階でpHを高め、アルカリ性にしてアンモニアガスとし
て揮散させ硝酸の絶対量を削減する技術。硝酸化成を受
けた窒素に対しては、イオン交換樹脂を利用する方法、
微生物にって分解させ除去する技術、生物膜槽からの汚
泥と共に水圏から除去する技術、水生植物による吸収除
去する技術、浸透式汚水処理等のように自然処理槽によ
る技術が主流である。これら自然処理槽による技術等で
は、急増する都市排水、工場排水、畜産排泄物処理水、
肥料による地下水汚染に対しては不十分である。特にア
ンモニアガスとして揮散させ方法ではアンモニア臭で匂
公害を起こすことも考えられ、一部の窒素は硝酸化成を
受けて亜硝酸、硝酸を生成する欠点も併せ持っている。
この様に現実には、河川、湖沼、海域の硝酸除去につい
ての具体的方法に行き詰まりが見られる。まして最近急
増しつつある硝酸による地下水汚染については、その除
去技術もなく、畜産排泄物からの抑制、家庭排水尿尿処
理からの排出抑制、工場排水の抑制等規制に頼らなけれ
ばならず、法的規制も考えられる状況である。特に過去
から排出され、地下水に混入された硝酸態窒素は、地域
によっては今後100年間硝酸態窒素の高濃度化が続く
と考えられ、法的規制が成されても汚染の軽減は急速に
は回復されないと考えられている。そこでこの問題に対
しては、基本的な所から手を付けなければならない。
2. Description of the Related Art Many patents and utility models have been proposed in the past for nitric acid removal of solutions in industry (14 cases) and water purification technology for environmental water systems. The contents of these technologies are as follows: As technology for removing nitrogen contained in night soil and livestock excreta, the pH is increased at the stage of ammonia nitrogen before being subjected to nitrification, alkalinized and volatilized as ammonia gas, and absolute nitric acid is removed. Technology to reduce volume. For nitrated nitrogen, a method using an ion exchange resin,
The mainstream is a technique of decomposing and removing by microorganisms, a technique of removing from the hydrosphere together with sludge from a biofilm tank, a technique of absorbing and removing by aquatic plants, and a technique using a natural treatment tank such as an infiltration type sewage treatment. The technologies using these natural treatment tanks, etc., increase rapidly increasing urban wastewater, factory wastewater, livestock wastewater,
Insufficient for groundwater contamination by fertilizers. In particular, the method of volatilization as ammonia gas may cause odor pollution due to ammonia odor, and also has a disadvantage that some nitrogen undergoes nitrification to generate nitrous acid and nitric acid.
Thus, the reality is that concrete methods for removing nitric acid from rivers, lakes, and seas are at a standstill. Even more recently, groundwater contamination by nitric acid, which has been increasing rapidly, has no technology to remove it, and must rely on regulations such as control of livestock excreta, control of domestic waste urine and urine treatment, and control of industrial wastewater. It is also a situation where regulatory restrictions are conceivable. In particular, nitrate nitrogen discharged from the past and mixed into groundwater is expected to continue to increase in concentration for some 100 years in some regions. It is not expected to be recovered. So we have to deal with this problem from the basics.

【0003】[0003]

【問題を解決するための手段】上記目的を達成するため
に、電気化学的方法による水中の硝酸を還元し脱窒する
技術を開発した。脱窒のプロセスは、脱窒槽内に少量の
水素ガスを通気し、高速撹拌して水に水素を飽和させ、
水の酸化還元電位の調整を行い、水を還元条件下に置い
て触媒上で紫外線等短波長の光照射により、通電によ
り、磁場変換により、硝酸イオンと水素原子を励起して
反応させ、硝酸を還元して窒素ガスとして空中に揮散さ
せるシステムである。化学反応は化1によっている。
Means for Solving the Problems In order to achieve the above object, a technique for reducing and denitrifying nitric acid in water by an electrochemical method has been developed. In the denitrification process, a small amount of hydrogen gas is passed through the denitrification tank, and high-speed stirring is performed to saturate the water with hydrogen.
Adjust the oxidation-reduction potential of water, place the water under reducing conditions, irradiate short-wavelength light such as ultraviolet light on the catalyst, energize it, excite nitric acid ions and hydrogen atoms by magnetic field conversion, and react with nitric acid. Is a system for reducing and evaporating as nitrogen gas in the air. The chemical reaction depends on Chemical formula 1.

【0004】[0004]

【化1】 Embedded image

【0005】硝酸窒素除去装置の構造は、第1図に示し
たように、加温装置、水素ガス混合飽和装置、脱窒装
置、処理水酸化順化装置、より成っている。
[0005] As shown in Fig. 1, the structure of the nitrogen nitrate removing device includes a heating device, a hydrogen gas mixing / saturation device, a denitrification device, and a treated hydroxylation acclimation device.

【0006】加温装置は前記の電気化学的方法による水
中の硝酸還元作用が温度の影響を大きく受けるので、硝
酸窒素除去装置に導く前に予め加温する水槽である。加
温の方法は、太陽熱利用、蒸気加温、地熱加温、電熱加
温何れでも良い。
[0006] The heating device is a water tank which is pre-heated before being introduced into the nitrogen nitrate removing device, since the nitric acid reducing action in water by the above-mentioned electrochemical method is greatly affected by the temperature. The method of heating may be any of solar heating, steam heating, geothermal heating, and electric heating.

【0007】水素ガス混合飽和装置は、水素ガス注入ノ
ズル、水素ガス混合撹拌装置より成っている。水の還元
条件を設定する水素ガスの注入は、水10lに対し水素
ガス100ml程度を添加し高速撹拌することにより、
水の酸化還元電位(Eh)=100mV以下に調整する
事が可能である。即ち、加えるガスの量は極めて少量で
目的を達成するので爆発等の危険性はないが、少量の水
素でもその集積を防止するため、ファンで槽外へガスの
強制排出を行う。
The hydrogen gas mixing and saturating device comprises a hydrogen gas injection nozzle and a hydrogen gas mixing and stirring device. Hydrogen gas injection for setting the water reduction conditions is performed by adding about 100 ml of hydrogen gas to 10 l of water and stirring at high speed.
It is possible to adjust the oxidation-reduction potential (Eh) of water to 100 mV or less. That is, there is no danger of explosion or the like since the amount of gas to be added is extremely small to achieve the purpose, but there is no danger of explosion or the like.

【0008】脱窒装置は触媒装置、紫外線等短波長光照
射装置、電流通電装置、磁場撹乱装置等から成り、装置
内を処理を要する水が通過する時点で連続的に、含まれ
ている硝酸が還元されて窒素ガスとして揮散する仕掛け
になっている。
The denitrification device comprises a catalyst device, a device for irradiating short-wavelength light such as ultraviolet light, a device for energizing current, a device for disturbing magnetic fields, and the like. Nitric acid contained in the device is continuously supplied when water requiring treatment passes through the device. Is reduced and volatilized as nitrogen gas.

【0009】触媒装置は硝酸還元反応を促す装置で、触
媒には鉄、銅、ニッケル、スズ、アンチモン、イリジウ
ム、ジルコニウム、パラジウム等の遷移金属元素を中心
とした素材が有効である。環境汚染の防止に役立つ元素
を選定する。
The catalyst device is a device for promoting a nitrate reduction reaction. The catalyst is made of a material mainly composed of a transition metal element such as iron, copper, nickel, tin, antimony, iridium, zirconium, and palladium. Select elements that will help prevent environmental pollution.

【0010】紫外線等短波長光照射装置は還元条件下の
水素原子と硝酸イオンを励起させる装置で、4000Å
以下の短波長光を照射するものである。通常は紫外線照
射灯を利用する。
A short-wavelength light irradiation device such as ultraviolet light is a device that excites hydrogen atoms and nitrate ions under reducing conditions, and is 4,000Å.
The following short wavelength light is irradiated. Usually, an ultraviolet irradiation lamp is used.

【0011】電流通電装置は還元条件下の水素原子と硝
酸イオンの励起と同時に、元素への電子受け渡しを促す
装置で、整流装置と槽内水中に露出する電極板より成っ
ている。電流は100V以下の低圧の電流を通電する。
電流の種類は直流でも交流でも良い。ただし、海水等塩
水に対しては通電処理はしない。
The current applying device is a device that promotes the transfer of electrons to the elements simultaneously with the excitation of hydrogen atoms and nitrate ions under reducing conditions, and is composed of a rectifying device and an electrode plate exposed in the water in the tank. The current is a low-voltage current of 100 V or less.
The type of current may be DC or AC. However, electricity is not applied to salt water such as seawater.

【0012】磁場撹乱装置は大型の電磁石を利用したも
のである。常に磁場の位置的変化、陰陽変化を与えるも
のである。大量の水を処理するには、反応効率を高める
必要があり、槽内の水全体の電磁場変換によって、一部
分ではなく全体の水の水素原子と硝酸イオンを予備的に
励起させて、触媒上での反応効率を高める。
The magnetic field disturbance device utilizes a large electromagnet. It always gives the positional change of the magnetic field, the yin-yang change. In order to treat a large amount of water, it is necessary to increase the reaction efficiency.Because the electromagnetic field conversion of the whole water in the tank preliminarily excites hydrogen atoms and nitrate ions of the whole water, not a part, it converts it to a catalyst. Improve the reaction efficiency.

【0013】水素と反応した硝酸態窒素は窒素ガスとな
って気化するので、残余の微量水素ガスと共にファンで
強制的に槽外へ排出する。
The nitrate-nitrogen that has reacted with hydrogen is vaporized as nitrogen gas, and is forcibly discharged out of the tank with a fan together with the remaining trace amount of hydrogen gas.

【0014】硝酸態窒素を除去した水は、まだ還元性が
強いのでそのまま放水すれば生物の棲息に影響を及ぼす
ので、処理水酸化順化装置においてエアーポンプを用い
て爆気し、十分酸素を送り込んで酸化条件に変換順化し
て利用に供する。
Since the water from which nitrate nitrogen has been removed has a strong reducing property, if it is discharged as it is, it will affect the inhabitation of living organisms. It is sent and converted into oxidizing conditions for use.

【0015】[0015]

【発明の実施例】実施例1 モデル実験による水中の硝
酸態窒素の分解除去の基本原理について実証試験を行っ
た。実験は、20ppmのNOを含む水溶液500m
lを11のビーカーに入れて、水素ガスを毎分5mlの
噴出速度で加え、磁力回転スターラーで撹拌しながら水
に水素ガスを飽和させる。10分経過後硝酸溶液が還元
条件に達したら、10℃の温度条件で、磁力回転スター
ラーで撹拌しながら鉄、銅、白金の触媒兼電極を挿入し
て2.5Vの電池で20分間電気分解を行った。その結
果鉄と銅を用いた遷移金属元素の場合はNO18pp
mの濃度に低下した。しかし、白金の場合はNO19
ppmの濃度で濃度低下の判定は不明であった。実験は
3連制としたが、何れも同様であった。(表1参照)
EXAMPLE 1 A demonstration test was conducted on the basic principle of decomposing and removing nitrate nitrogen in water by a model experiment. The experiment was performed with 500 m of an aqueous solution containing 20 ppm of NO 3.
1 into a beaker 11 and adding hydrogen gas at a jetting rate of 5 ml per minute, and saturating the water with hydrogen gas while stirring with a magnetic rotating stirrer. After the lapse of 10 minutes, when the nitric acid solution reaches the reducing condition, at a temperature condition of 10 ° C., while stirring with a magnetic rotating stirrer, insert a catalyst / electrode of iron, copper, and platinum and electrolyze with a 2.5 V battery for 20 minutes. Was done. As a result, in the case of a transition metal element using iron and copper, NO 3 18 pp
m. However, in the case of platinum, NO 3 19
The determination of the decrease in concentration at the ppm concentration was unknown. The experiment was a three-part system, but all were the same. (See Table 1)

【0016】[0016]

【表1】 [Table 1]

【0017】実施例2 実験は、20ppmのNOを含む水溶液に30℃の温
度で実施例1と同様2.5Vの通電により実験を行っ
た。その結果鉄と銅を用いた遷移金属元素の場合はNO
16ppmの濃度に低下した。(表2参照) しかし、陰陽両極に鉄、銅の電極を用いた場合は金属元
素の溶液への溶出が認められた。これらのことから、反
応を規制する条件は、温度、触媒元素の種類、磁場の強
さ、通電する電圧と電流が影響するものと考えられた。
また、触媒元素としては、鉄、銅、の他マンガン、ニッ
ケル、スズ、アンチモン、イリジウム、ジルコニウム、
パラジウム等の遷移金属元素を中心とした重金属元素が
関与するが、金属元素の溶出等も考えられ、環境汚染の
ないものを選定することが必要である。
Example 2 The experiment was conducted by applying an electric current of 2.5 V to an aqueous solution containing 20 ppm of NO 3 at a temperature of 30 ° C. as in Example 1. As a result, in the case of a transition metal element using iron and copper, NO
3 was reduced to a concentration of 16ppm. However, when iron and copper electrodes were used for both the positive and negative electrodes, elution of the metal element into the solution was observed. From these facts, it is considered that the conditions for regulating the reaction are influenced by the temperature, the type of the catalytic element, the strength of the magnetic field, the voltage and the current to be applied.
In addition, as a catalyst element, iron, copper, manganese, nickel, tin, antimony, iridium, zirconium,
Although heavy metal elements mainly including transition metal elements such as palladium are involved, elution of the metal elements is also considered, and it is necessary to select one that does not cause environmental pollution.

【0018】[0018]

【表2】 [Table 2]

【0019】実施例3 実験は、20ppmのNOを含む水溶液に30℃の温
度で実施例1と同様2.5Vの通電により実験を行った
が電極の一方の陰極を白金にした場合は金属の溶出はな
かった。この場合も硝酸態窒素は、およそNO16p
pmの濃度に低下した。(表3参照)
Example 3 An experiment was conducted by applying an electric current of 2.5 V to an aqueous solution containing 20 ppm of NO 3 at 30 ° C. at a temperature of 30 ° C. in the same manner as in Example 1. However, when one of the electrodes was made of platinum, metal was used. Was not eluted. Also in this case, the nitrate nitrogen is approximately NO 3 16p
pm. (See Table 3)

【0020】[0020]

【表3】 [Table 3]

【0021】[0021]

【効果】本発明は以上のように地下水、河川水、湖沼
水、海水に含まれる硝酸態窒素を物理化学的処理によっ
て、除去することを可能にする技術として提供した。過
去において人為的に地下水、河川、湖沼、あるいは海域
の硝酸態窒素汚染が進行し、飲用不適とされた水系にお
いても、本技術によって飲用可能な水として再生が可能
とり、その利用される範囲は非常に多岐にわたるものと
考えられる。基本的には本技術によって水に含まれる硝
酸の濃度を低下させることが証明されたが、更に技術の
改良よって、また大掛りなシステムを導入することによ
り、その効率が向上し、大量の水処理が可能である。従
って国内、海外の地下水汚染対策にも活用できる技術で
ある。
As described above, the present invention provides a technique for removing nitrate nitrogen contained in groundwater, river water, lake water, and seawater by physicochemical treatment. In the past, nitrate nitrogen contamination of groundwater, rivers, lakes, marshes, or sea areas has been artificially progressing, and even in water systems that are unsuitable for drinking, this technology can regenerate potable water, and the range of use is It is thought to be very diverse. Basically, it was proved that this technology reduces the concentration of nitric acid contained in water.However, by further improving the technology and introducing a large-scale system, the efficiency is improved, and Processing is possible. Therefore, it is a technology that can be used for domestic and overseas groundwater pollution control.

【図面の簡単な説明】[Brief description of the drawings]

図1は硝酸除去装置並びに本発明に係る水の硝酸除去工
程の各装置の連繋図である。
FIG. 1 is a connection diagram of a nitric acid removing device and respective devices in a nitric acid removing step of water according to the present invention.

【符号の説明】[Explanation of symbols]

1−加温装置、2−水素ガス混合飽和装置、3−脱窒装
置、4−処理水酸化順化装置、5−硝酸除去装置内への
給水口、6−予備加熱、7−撹拌子、8−撹拌子モータ
ー、9−水素ボンベ、10−水素ガス混合飽和装置内に
微量残余する水素がす強制排出口、11−触媒装置、1
2−紫外線等短波長光照射装置、13−磁場変換装置、
14−通電装置(整流器)、15−発生する窒素ガス排
出口、16−エアーポンプ、17−爆気、18−過乗空
気排出口、19−硝酸除去装置外への出水口、20−ガ
ス排出口以外の→印は処理水の誘導方向を示す。
1-warming device, 2-hydrogen gas mixing / saturation device, 3-denitrification device, 4-treatment hydroxylation-accumulation device, 5-water supply port to nitric acid removal device, 6-preheating, 7-stirrer, 8- Stirrer motor, 9-Hydrogen cylinder, 10-Forced discharge of residual hydrogen in the hydrogen gas mixing / saturation device, 11-Catalyst device, 1
2-short wavelength light irradiation device such as ultraviolet light, 13-magnetic field conversion device,
14-Electrification device (rectifier), 15-Emission of nitrogen gas, 16-Air pump, 17-Explosion, 18-Excess air outlet, 19-Outlet of nitric acid removing device, 20-Gas exhaust The mark → except for the exit indicates the direction of treatment water induction.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/58 C02F 1/46 101C Fターム(参考) 4D037 AA01 AA05 AA06 AB12 BA18 BA23 BB04 BB05 BB06 CA04 CA05 CA09 CA12 4D038 AA01 AA02 AA03 AB31 BA02 BA04 BB01 BB03 BB07 BB10 BB11 BB15 BB16 BB20 4D050 AA01 AB37 BA14 BB01 BC01 BC04 BC06 BC09 BC10 BD02 BD03 BD06 CA01 CA03 CA10 CA11 CA20 4D061 DA01 DA02 DA04 DA09 DC14 EA04 EB28 EB30 EB31 EC11 ED17 ED20 FA01 FA03 FA07 FA16 FA17 FA20 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) C02F 1/58 C02F 1/46 101C F-term (Reference) 4D037 AA01 AA05 AA06 AB12 BA18 BA23 BB04 BB05 BB06 CA04 CA05 CA09 CA12 4D038 AA01 AA02 AA03 AB31 BA02 BA04 BB01 BB03 BB07 BB10 BB11 BB15 BB16 BB20 4D050 AA01 AB37 BA14 BB01 BC01 BC04 BC06 BC09 BC10 BD02 BD03 BD06 CA01 CA03 CA10 CA11 CA20 4D061 DA01 FA02 EA01 EB14 DC09 FA16 FA17 FA20

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 硝酸イオンを含む水に水素ガスを通気
し、還元条件下で触媒上において電気化学的に硝酸イオ
ンを窒素ガスに変換し、気化揮散させて水の硝酸イオン
濃度を低下させる脱窒装置。
1. A method for reducing the concentration of nitrate ions in water by passing hydrogen gas through water containing nitrate ions, electrochemically converting nitrate ions to nitrogen gas on a catalyst under reducing conditions, and vaporizing and evaporating the nitrate ions. Nitrogen device.
【請求項2】 硝酸イオンを含む水に水素ガスを通気
し、還元条件下の触媒上において電極に通電することに
よる水の脱窒素技術。
2. A denitrification technique for water by passing hydrogen gas through water containing nitrate ions and supplying electricity to an electrode on a catalyst under reducing conditions.
【請求項3】 硝酸イオンを含む水に水素ガスを通気
し、還元条件下の触媒上において電磁変換することによ
る水の脱窒素技術。
3. A denitrification technique for water by passing hydrogen gas through water containing nitrate ions and performing electromagnetic conversion on a catalyst under reducing conditions.
【請求項4】 硝酸イオンを含む水に水素ガスを通気
し、還元条件下の触媒上において紫外線及光線照射する
ことによる水の脱窒素技術。
4. A technique for denitrifying water by passing hydrogen gas through water containing nitrate ions and irradiating the catalyst with ultraviolet light and light under reducing conditions.
JP19221499A 1999-06-01 1999-06-01 Physicochemical method for removal of nitrate nitrogen in water and denitrifying apparatus Pending JP2000334478A (en)

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Publication Number Publication Date
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010013677A1 (en) * 2008-07-28 2010-02-04 栗田工業株式会社 Process and equipment for the treatment of water containing organic matter
CN103449639A (en) * 2013-09-16 2013-12-18 中国海洋石油总公司 Micro-series-wound-internal circulating photoelectric catalysis oxidation wastewater treatment method
CN104163473A (en) * 2014-07-29 2014-11-26 广东威迪科技股份有限公司 Novel electrochemical treatment device for wastewater treatment and wastewater treatment method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010013677A1 (en) * 2008-07-28 2010-02-04 栗田工業株式会社 Process and equipment for the treatment of water containing organic matter
US8771522B2 (en) 2008-07-28 2014-07-08 Kurita Water Industries Ltd. Method and apparatus for treating organic matter-containing water
CN103449639A (en) * 2013-09-16 2013-12-18 中国海洋石油总公司 Micro-series-wound-internal circulating photoelectric catalysis oxidation wastewater treatment method
CN103449639B (en) * 2013-09-16 2014-11-05 中国海洋石油总公司 Micro-series-wound-internal circulating photoelectric catalysis oxidation wastewater treatment method
CN104163473A (en) * 2014-07-29 2014-11-26 广东威迪科技股份有限公司 Novel electrochemical treatment device for wastewater treatment and wastewater treatment method
CN104163473B (en) * 2014-07-29 2016-06-29 广东威迪科技股份有限公司 A kind of model electrochemical for wastewater treatment processes equipment and method of wastewater treatment thereof

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