JPH0199689A - Method for removing organic matter in water - Google Patents
Method for removing organic matter in waterInfo
- Publication number
- JPH0199689A JPH0199689A JP62253527A JP25352787A JPH0199689A JP H0199689 A JPH0199689 A JP H0199689A JP 62253527 A JP62253527 A JP 62253527A JP 25352787 A JP25352787 A JP 25352787A JP H0199689 A JPH0199689 A JP H0199689A
- Authority
- JP
- Japan
- Prior art keywords
- water
- organic matter
- oxidizing agent
- manganese dioxide
- org
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/26—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only halogen atoms as hetero-atoms
- C07C1/30—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only halogen atoms as hetero-atoms by splitting-off the elements of hydrogen halide from a single molecule
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/14—Phosphorus; Compounds thereof
- C07C2527/16—Phosphorus; Compounds thereof containing oxygen
- C07C2527/167—Phosphates or other compounds comprising the anion (PnO3n+1)(n+2)-
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/20—Carbon compounds
- C07C2527/232—Carbonates
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/16—Systems containing only non-condensed rings with a six-membered ring the ring being unsaturated
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野J
この発明は上、下水や工業用水等の水中に存在する有機
物質を除去する処理法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application J This invention relates to a treatment method for removing organic substances present in water such as water, sewage and industrial water.
従来、水中の有機物の除去方法としては、凝集沈殿ろ過
処理法、活性炭吸着処理法、生物酸化処理法等がある。Conventionally, methods for removing organic matter from water include coagulation sedimentation filtration treatment, activated carbon adsorption treatment, biological oxidation treatment, and the like.
凝集沈殿ろ過処理法では、非溶解性有機物1分子量の大
きな有機物は、適切な凝集剤の注入により除去されるが
、分子量の小さな有機物は除去されない。In the coagulation-sedimentation filtration treatment method, insoluble organic matter 1 organic matter with a large molecular weight is removed by injection of an appropriate flocculant, but organic matter with a small molecular weight is not removed.
活性炭吸着処理では、凝集沈殿ろ過処理法と逆に1分子
量の小さな有機物は除去されるが、分子量の大きな有機
物は除去されず、また吸着容量に限界があるため、活性
炭の再生、交換等のランニンクコストがかかる。生物酸
化処理法では、水温の低下により除去率が落ち、また原
水の負荷変動の処理水に対する影響が大きく、安定した
除去率が得られない。Activated carbon adsorption treatment removes organic matter with a small molecular weight, contrary to the coagulation-sedimentation filtration treatment method, but it does not remove organic matter with a large molecular weight.Also, since there is a limit to the adsorption capacity, it is necessary to carry out running operations such as regeneration and replacement of activated carbon. It costs a lot. In the biological oxidation treatment method, the removal rate decreases due to a decrease in water temperature, and changes in the load of raw water have a large effect on the treated water, making it impossible to obtain a stable removal rate.
この発明は水中の有機物の除去を、従来の凝集沈殿ろ過
処理法、活性炭吸着処理法、生物酸化処理法等の付帯設
備や再生装置を必要とする処理法ではなく、またマンガ
ン砂を接触酸化炉材として用い、接触酸化による色度の
除去を行なう処理法を改善したもので、効率的に有機物
除去を行なう処理法である。すなわち高度に活性化した
酸化接触触媒ろ材を用いたろ層の全高で、連続的に酸化
分解を行なうようにした。ランニングコストの殆んどか
からない処理法を提供することにある。This invention removes organic matter from water using conventional coagulation-sedimentation filtration treatment methods, activated carbon adsorption treatment methods, biological oxidation treatment methods that require incidental equipment and regeneration equipment, and also uses manganese sand in a contact oxidation furnace. This is an improved treatment method that removes chromaticity by catalytic oxidation, and is a treatment method that efficiently removes organic substances. That is, oxidative decomposition was carried out continuously over the entire height of the filter layer using a highly activated oxidation contact catalyst filter medium. The purpose is to provide a processing method that requires almost no running cost.
さらにはこの発明の処理法は、既存の浄水処理の一プロ
セスである、急速砂i濾過システムに適用し、本来の5
濾過機能と合わせ、有機物除去をも同時に行なえるよう
な機能を持たせることもできるようにしたものである。Furthermore, the treatment method of this invention can be applied to the rapid sand i-filtration system, which is one of the existing water purification processes, and can be applied to the original 5
In addition to the filtration function, it can also have the function of removing organic matter at the same time.
E問題点を解決するための手段J この発明は水中の有機物の除去において。EMeans to solve the problemJ This invention is used in the removal of organic matter in water.
酸化剤の存在下で、接触触媒ろ材を用いることによって
、水中の有機物を酸化分解して除去する水中の有機物除
去法である。これらの有機物量は、TOC(全有機炭素
)、にMnOm(過マンガン酸カリウム〕消費量、 E
260(紫外部吸光度260r+11)等の指標で検知
する。This is a method for removing organic matter in water by oxidizing and decomposing organic matter in water by using a catalytic filter medium in the presence of an oxidizing agent. The amount of these organic substances is TOC (total organic carbon), MnOm (potassium permanganate) consumption, E
It is detected using an index such as 260 (ultraviolet absorbance 260r+11).
この発明は、接触触媒3戸材として活性度の高い電解二
酸化マンガンのβ型やγ型二酸化マンカン粒子を用い、
適当な塩素ガスや1次亜塩素酸ナトリウム等の酸化剤の
存在下において、有機物質含有水を触媒シ戸材層に単に
通水してシ濾過するだけで、接触触媒シ戸材層で、酸化
剤の酸化作用によって、水中の有機物を酸化分解して除
去するものである。この有機物の酸化分解が接触触媒シ
戸材の層高の全層にわたって行なわれるため、有機物除
去を連続的に、かつ確実に行なうことができる。This invention uses β-type and γ-type mankan dioxide particles of electrolytic manganese dioxide, which have high activity, as a contact catalyst material.
In the presence of an appropriate oxidizing agent such as chlorine gas or primary sodium hypochlorite, water containing organic substances is simply passed through the catalytic material layer and filtered, and the catalytic material layer Organic matter in water is oxidized and decomposed and removed by the oxidizing action of an oxidizing agent. Since this oxidative decomposition of organic matter is carried out over the entire layer height of the catalytic catalyst door material, organic matter can be removed continuously and reliably.
酸化剤としては、塩素ガスや次亜塩素酸ナトリウム等の
塩素系のほかに、過酸化水素や過マンガン酸カリウム又
はより酸化力の強いオゾン等を用いることができる。As the oxidizing agent, in addition to chlorine gas, sodium hypochlorite, and other chlorine-based oxidizing agents, hydrogen peroxide, potassium permanganate, or ozone, which has stronger oxidizing power, can be used.
接触触媒シ戸材としては、従来のマンガン砂と比較して
も、比表面積が大きく、触媒活性度の高いろ材である電
解二酸化マンガンのβ型二酸化マンカン粒子、γ型二酸
化マンガン粒子が適し、さらに結晶的にβ型、γ型の2
相混在型二酸化マンガン粒子、あるいはこれらβ型、γ
型、β−γ混相型二酸化マンガン粒子の混合物を用いる
ことができるが、酸化剤の下で酸化接触触媒を行なう上
記機能以上のシ戸材であれば、これらに限定されるもの
ではない。As the catalyst material, β-type manganese dioxide particles and γ-type manganese dioxide particles of electrolytic manganese dioxide, which are filter media with a larger specific surface area and higher catalytic activity than conventional manganese sand, are suitable. Crystallographically β-type and γ-type 2
Mixed-phase manganese dioxide particles, or these β-type, γ-type
A mixture of type manganese dioxide particles and β-γ mixed phase type manganese dioxide particles can be used, but the material is not limited to these as long as it has the above-mentioned function of catalyzing oxidation in the presence of an oxidizing agent.
γ型の二酸化マンガンには、天然産のラムスプライト、
人工の電解二酸化マンガン等が用いられ、このγ型二酸
化マンガンから、熱処理温度が200℃以上になると一
部β型二酸化マンガンを生成して変態がはじまるため、
β−γ混相型二酸化マンカン、あるいはβ型二酸化マン
ガンを得ることができる。γ-type manganese dioxide includes naturally produced rum sprite,
Artificial electrolytic manganese dioxide is used, and when the heat treatment temperature reaches 200°C or higher, some β-type manganese dioxide is generated and transformation begins.
β-γ mixed phase manganese dioxide or β-type manganese dioxide can be obtained.
この発明で有機物の指標として用いられているのは、丁
OC(全有機炭素)、 KMnO,(過マンガン酸カリ
ウム)消費量、E260(紫外部吸光度)等がある。T
OCは、水中に存在する有機物中の炭素量で、有機物の
絶対量を示し、過マンガン酸カリウム消′4!&量は、
適当な条件下でKMnO,により酸化される有機物量を
、E260は紫外部波長260n+iで吸収を示す有機
物(2重結合を有する有機物)を示す、これらの有機物
量の指櫨による検知は、有機物量の除去変化割合を直線
的に表示するものであるので、有機物除去の割合が明確
に検知される。In this invention, indicators of organic matter used include OC (total organic carbon), KMnO, (potassium permanganate) consumption, and E260 (ultraviolet absorbance). T
OC is the amount of carbon in organic matter present in water, and indicates the absolute amount of organic matter, and potassium permanganate is eliminated'4! & amount is
E260 indicates the amount of organic matter that is oxidized by KMnO under appropriate conditions, and E260 indicates the organic matter (organic matter with double bonds) that exhibits absorption at an ultraviolet wavelength of 260n+i. Since the rate of change in removal of organic matter is displayed linearly, the rate of removal of organic matter can be clearly detected.
これら指標のうち、上水道水質基準として掲げられてい
るのは、過マンガン酸カリウム消費量だけである(10
+wg/ Q )。Of these indicators, only potassium permanganate consumption is listed as a water quality standard (10
+wg/Q).
近年1分析技術の発展に伴ない、微量有機物の除去方法
が検討されている。また最近は「おいしい水」というよ
うな飲料水の質的向上が求められ、飲料水中の有機物と
しても、過マンガン酸カリウム消費量として、3.0m
g/ Q以下という目漂値が定められつつある。In recent years, with the development of analytical techniques, methods for removing trace amounts of organic matter have been studied. Recently, there has been a demand for improving the quality of drinking water such as "tasting water", and as for the organic matter in drinking water, the amount of potassium permanganate consumed has increased to 3.0 m
A target value of g/Q or less is being established.
[作用・実施例]
この発明の実施する装置としては、添付図面に示すよう
に、原水タンク2と支持砂利層6上に充填した接触触媒
ろ材層5とからなるS濾過筒lを1通水路3を介して接
続し、この通水路3の途中に酸化剤注入部4を設ける。[Function/Example] As shown in the attached drawing, the device for carrying out the present invention includes an S filter cylinder 1 consisting of a raw water tank 2 and a catalytic catalyst filter layer 5 filled on a support gravel layer 6. 3, and an oxidizing agent injection part 4 is provided in the middle of this water passage 3.
前記;濾過筒lは、内径25m、二酸化マンガンろ層厚
700 m、二酸化マンガンの有効径0.43m、均等
係数1.40とした。As mentioned above, the filter cylinder 1 had an inner diameter of 25 m, a manganese dioxide filter layer thickness of 700 m, an effective manganese dioxide diameter of 0.43 m, and a uniformity coefficient of 1.40.
この実施例では、酸化剤として次亜塩素酸ナトリウムを
用い、接触触媒シ戸材として、β型二酸化マンガン粒子
、γ型二酸化マンガン粒子あるいはβ型及びγ型二酸化
マンガン混在粒子のものを用い、比較として従来のマン
ガン砂による処理法を用いた。In this example, sodium hypochlorite was used as the oxidizing agent, β-type manganese dioxide particles, γ-type manganese dioxide particles, or mixed particles of β-type and γ-type manganese dioxide were used as the catalyst material. A conventional treatment method using manganese sand was used.
酸化剤である次亜塩素酸ナトリウムの注入のコントロー
ルとしては、通水路3の途中の酸(ヒ剤注入部4に2次
亜塩素酸ナトリウムを注入し、遊離残留塩素を指標とし
て、接触触媒シ戸材層の5濾過筒1を通過した処理水7
の遊離残留塩素が、およそ0゜1mg/ Q以上である
ようにすれば、水中の有機物の除去を効率的に行なうこ
とができる。その試験結果を第1表と第2表に示す。To control the injection of sodium hypochlorite, which is an oxidizing agent, secondary sodium hypochlorite is injected into the acid (arsenic agent injection part 4) in the middle of the water passage 3, and the free residual chlorine is used as an indicator to control the contact catalyst system. Treated water 7 that has passed through the door material layer 5 filter tube 1
If the free residual chlorine in the water is approximately 0.1 mg/Q or more, organic matter in the water can be efficiently removed. The test results are shown in Tables 1 and 2.
第1表は通水条件が空間速度5V=6のとき、第2表は
通水条件が空間速度5V=lOのときを示す・
(備考)通水条件:空間速度5V=6
上記試験成績表が示すように、この発明の処理法は従来
の処理に比べて、有機物の除去に関して優れていること
がわかる。なお次亜塩素酸ナトリウム以上の酸化力を有
するオゾン等の酸化剤を用いれば、より効果的に除去す
ることができる。Table 1 shows the water flow conditions when the space velocity is 5V=6, and Table 2 shows the water flow conditions when the space velocity is 5V=1O. (Note) Water flow conditions: Space velocity 5V=6 The above test results table As shown, it can be seen that the treatment method of the present invention is superior to conventional treatments in terms of removing organic matter. Note that it can be removed more effectively by using an oxidizing agent such as ozone that has an oxidizing power greater than that of sodium hypochlorite.
この発明の適用として1例えば現在の一般的な浄水方法
である、凝集・沈殿・シ濾過システムのプロセスである
急速砂;濾過システムにおいて、急速シ濾過池のろ材を
珪砂からβ型又はγ型二酸化マンガン粒子等に置き換え
て、浄水で一般に消毒・殺菌に使われている塩素ガスや
2次亜塩素酸ナトリウムのような、既存の注入設備を利
用することによって、適当な塩素系酸化剤の存在下で;
濾過することにより、従来のシ濾過機能と共に何機物′
σを容易に除去することができ、また凝集剤の注入量を
低減することができるメリツ1へがある。Applications of this invention 1. For example, rapid sand is a process of coagulation/sedimentation/filtration system which is a common water purification method at present; In the presence of a suitable chlorine-based oxidizing agent, by using existing injection equipment, such as chlorine gas or secondary sodium hypochlorite, which are commonly used for disinfection and sterilization in water purification, by replacing manganese particles etc. in;
By filtration, it can be used in many ways in addition to the conventional filtering function.
The first advantage is that σ can be easily removed and the amount of coagulant to be injected can be reduced.
〔発明の効果]
この発明の水中に含有する有機物の除去法は、水中の有
機物含有水を酸化剤の存在下で。[Effects of the Invention] The method of removing organic matter contained in water according to the present invention removes organic matter-containing water from water in the presence of an oxidizing agent.
高度に活性化したβ型、γ型二酸化マンガン等の粒子層
からなる接触触媒シ戸材層を通過させ、有機物を酸化分
解して除去するもので、その何機物除去割合をKMnO
、消費1i、To+:。This method removes organic matter by oxidation and decomposition by passing it through a contact catalytic material layer consisting of a particle layer of highly activated β-type and γ-type manganese dioxide.
, consumption 1i, To+:.
E260等で検知することによって、有機物の除去量が
明確に検知できるという簡略化した処理法である。This is a simplified treatment method in which the amount of organic matter removed can be clearly detected by detecting with E260 or the like.
この他、従来のマンカン砂による処理法よりも除去率が
高く、さらには粒状活性炭処理法やオゾン処理法のよう
な、再生装置や付帯設備を必要とせず、既存設備を利用
でき、またランニングコストも現在の急速5濾過システ
ムと殆んと同程度であり、粒状活性炭処理法における活
性炭再生費用、オゾン処理法における電力費等のランニ
ングコストを必要とせず、コスト的にも有機物を含む水
の処理方法として極めて有効な処理法である。In addition, the removal rate is higher than the conventional treatment method using mankan sand, and furthermore, unlike the granular activated carbon treatment method or ozone treatment method, existing equipment can be used without the need for regeneration equipment or ancillary equipment, and running costs are low. It is almost the same level as the current rapid 5 filtration system, and there is no running cost such as activated carbon regeneration cost in the granular activated carbon treatment method or electricity cost in the ozone treatment method, and it is cost-effective for treating water containing organic matter. This is an extremely effective treatment method.
添付図面はこの発明の方法を実施すべき装置の系統図で
ある9
なお、図において
■ ろ渦部
2 原水タンク
3 通水路
ll 酸1ヒ剤注入部
5 接触触媒ろ材
6 支持砂利層
7 処理水
である。The attached drawing is a system diagram of the apparatus to carry out the method of the present invention.9 In the figure, ■ Filtration vortex section 2 Raw water tank 3 Water passage 11 Acid 1 arsenic injection section 5 Contact catalyst filter medium 6 Support gravel layer 7 Treated water It is.
Claims (3)
接触触媒ろ材を用いることによつて、有機物を酸化分解
して除去することを特徴とする水中の有機物除去法。(1) In the removal of organic matter from water, in the presence of an oxidizing agent,
A method for removing organic matter in water, which is characterized by oxidatively decomposing and removing organic matter by using a catalytic catalytic filter medium.
素系酸化剤、オゾン、過酸化水素、過マンガン酸カリウ
ムであることを特徴とする特許請求の範囲第1項記載の
水中の有機物除去法。(2) Organic matter in water according to claim 1, wherein the oxidizing agent is chlorine gas, a chlorine-based oxidizing agent such as sodium hypochlorite, ozone, hydrogen peroxide, or potassium permanganate. Removal method.
二酸化マンガン粒子、γ型二酸化マンガン粒子、結晶的
にβ型、γ型の2相混在型二酸化マンガン粒子の単独使
用あるいはこれら各型二酸化マンガン粒子の混合物であ
ることを特徴とする特許請求の範囲第1項又は第2項記
載の水中の有機物除去法。(3) Single use of β-type manganese dioxide particles, γ-type manganese dioxide particles, crystallized β-type and γ-type two-phase mixed manganese dioxide particles, or each of these types of manganese dioxide using electrolytic manganese dioxide as the contact catalyst filter material The method for removing organic matter in water according to claim 1 or 2, characterized in that the method is a mixture of particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62253527A JPH0199689A (en) | 1987-10-09 | 1987-10-09 | Method for removing organic matter in water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62253527A JPH0199689A (en) | 1987-10-09 | 1987-10-09 | Method for removing organic matter in water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0199689A true JPH0199689A (en) | 1989-04-18 |
Family
ID=17252607
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62253527A Pending JPH0199689A (en) | 1987-10-09 | 1987-10-09 | Method for removing organic matter in water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0199689A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0768277A (en) * | 1993-09-03 | 1995-03-14 | Ngk Insulators Ltd | Highly advanced treatment of sewage |
| KR20030065837A (en) * | 2002-02-01 | 2003-08-09 | 이세진 | Treatment of polluted water using catalysis oxidation number |
| KR100467442B1 (en) * | 2002-10-15 | 2005-01-24 | 한국염색기술연구소 | A method of treatment for dyeing wastewater by using catalyst oxidizing water |
| WO2010109838A1 (en) * | 2009-03-24 | 2010-09-30 | 株式会社アサカ理研 | Water treatment method and water treatment system |
| JP2015188823A (en) * | 2014-03-28 | 2015-11-02 | 吸着技術工業株式会社 | Treatment method and device for harmful matter-containing liquid |
| WO2024070733A1 (en) * | 2022-09-27 | 2024-04-04 | パナソニックIpマネジメント株式会社 | Water purification device |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58137492A (en) * | 1982-02-10 | 1983-08-15 | Suido Kiko Kk | Method for removing color of water |
| JPS59139991A (en) * | 1983-01-31 | 1984-08-11 | Suido Kiko Kk | Colored water disposal |
-
1987
- 1987-10-09 JP JP62253527A patent/JPH0199689A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58137492A (en) * | 1982-02-10 | 1983-08-15 | Suido Kiko Kk | Method for removing color of water |
| JPS59139991A (en) * | 1983-01-31 | 1984-08-11 | Suido Kiko Kk | Colored water disposal |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0768277A (en) * | 1993-09-03 | 1995-03-14 | Ngk Insulators Ltd | Highly advanced treatment of sewage |
| KR20030065837A (en) * | 2002-02-01 | 2003-08-09 | 이세진 | Treatment of polluted water using catalysis oxidation number |
| KR100467442B1 (en) * | 2002-10-15 | 2005-01-24 | 한국염색기술연구소 | A method of treatment for dyeing wastewater by using catalyst oxidizing water |
| WO2010109838A1 (en) * | 2009-03-24 | 2010-09-30 | 株式会社アサカ理研 | Water treatment method and water treatment system |
| WO2010109556A1 (en) * | 2009-03-24 | 2010-09-30 | 株式会社アサカ理研 | Water treatment method and water treatment system |
| JP4786771B2 (en) * | 2009-03-24 | 2011-10-05 | 株式会社アサカ理研 | Water treatment method and water treatment system |
| CN102361826A (en) * | 2009-03-24 | 2012-02-22 | 株式会社安积理研 | Water treatment method and water treatment system |
| JP2015188823A (en) * | 2014-03-28 | 2015-11-02 | 吸着技術工業株式会社 | Treatment method and device for harmful matter-containing liquid |
| WO2024070733A1 (en) * | 2022-09-27 | 2024-04-04 | パナソニックIpマネジメント株式会社 | Water purification device |
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