JPS614597A - Method for simultaneously decomposing, denitrifying and dephosphorizing organic material in sewage component and multipurpose floating filter medium used in said method - Google Patents
Method for simultaneously decomposing, denitrifying and dephosphorizing organic material in sewage component and multipurpose floating filter medium used in said methodInfo
- Publication number
- JPS614597A JPS614597A JP59125701A JP12570184A JPS614597A JP S614597 A JPS614597 A JP S614597A JP 59125701 A JP59125701 A JP 59125701A JP 12570184 A JP12570184 A JP 12570184A JP S614597 A JPS614597 A JP S614597A
- Authority
- JP
- Japan
- Prior art keywords
- filter medium
- sewage
- dephosphorization
- floating filter
- nitrogen
- 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.)
- Granted
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
Description
【発明の詳細な説明】
本発明は、最近の文化、経済、産業の急速なる発達にと
もない問題になっている富栄養化問題を解決するため、
その原因である下水成分中の有機物の分解、脱窒、脱り
ん、の方法、及び、その方法に使用する、ろ材に係るも
のである。さて、下水成分中の有機物の分解については
、色々の方法があり現在の主流となっているのは下水道
施設基準で示される標準活性汚泥法である。然しなから
、標準活性汚泥法ではBOD、COD、88等の除去に
ついては、その法的規制値を達成することは出来るが、
脱窒、及び、脱りん、は不十分で三次処理施設を設置し
て、これを除去せねばならない。[Detailed Description of the Invention] The present invention aims to solve the problem of eutrophication, which has become a problem with the recent rapid development of culture, economy, and industry.
It concerns a method of decomposing, denitrifying, and dephosphorizing organic matter in sewage components that are the cause of this problem, and a filter medium used in the method. There are various methods for decomposing organic matter in sewage components, and the current mainstream method is the standard activated sludge method specified in the standards for sewage facilities. However, although the standard activated sludge method can achieve the legally regulated values for removing BOD, COD, 88, etc.
Since denitrification and dephosphorization are insufficient, a tertiary treatment facility must be installed to remove this.
現在、窒素の処理法としては化学的処理法と生物化学的
処理法があり、前者にはアンモニアストリッピング法、
ゼオライト吸着法、堪素注入法、イオン交換法等、後者
には循環式硝化脱窒素性、メタノール注入法、潜没回転
円板法等がある。次に、脱りん、については主として金
属酸化物として脱りん、する。すなわち、凝集剤を添加
して凝集法でんする法、カル/ウムeノ・イドロキンル
・アパタイト利用の接触脱りん法、生物学的脱りん法、
及び、吸着法等がある。Currently, there are two methods for treating nitrogen: chemical treatment and biochemical treatment; the former includes ammonia stripping,
Zeolite adsorption method, hydrogen injection method, ion exchange method, etc. The latter include cyclic nitrification and denitrification method, methanol injection method, submerged rotating disk method, etc. Next, regarding dephosphorization, dephosphorization is mainly performed as a metal oxide. Namely, a method of coagulation by adding a coagulant, a catalytic dephosphorization method using cal/umenohydroquine apatite, a biological dephosphorization method,
There are also adsorption methods.
略て、現在使用されている標準活性汚泥法の下水道終末
施設等に脱窒、脱りん、の設備を具備させるためには、
はう大な敷地と多額の建設費を要し、加えて最初から脱
窒、脱りん、を考慮のうえ設計されておらないだめの無
駄、冗長的な部分が非常に多く々るのは避けられないこ
とである。In short, in order to equip sewage terminal facilities using the standard activated sludge method currently in use with denitrification and dephosphorization equipment,
Avoid the need for large sites and large construction costs, as well as the large number of wasteful and redundant parts that are not designed with denitrification and dephosphorization in mind from the beginning. This is something that cannot be done.
本発明は、旧施設の改造、増設設備を極力押え効率的に
法的規制値をクリアー出来ること、すなわち、N%P、
の処理を下水終末処理場等の二次処理施設の中で完結さ
せることを、この発明の目的とした。The present invention is capable of efficiently clearing legal regulation values while minimizing remodeling and expansion of old facilities, that is, N%P,
An object of the present invention is to complete the treatment of wastewater in a secondary treatment facility such as a sewage treatment plant.
次に、上記の問題点を解決するだめの手段として、先づ
、有機物の分解は従来どおり好機性微生−物により生物
化学的に有機物を分解させる。すなわち散気装置から空
気、又は、純酸素を噴出させた曝気槽に、ろ材の重量と
同じ浮力を持たせた、多目的浮遊ろ材を投入し、旋回流
と共に流れの中を移動はせると、その間に、多目的浮遊
ろ材の中空物体3の外面、および、ひだ4の入口部は好
気性微生物が耐着繁殖し、これらの微生物により下水成
分中の有機物の分解、及び、硝化が行われる。Next, as a means to solve the above-mentioned problems, first, the organic matter is biochemically decomposed by opportunistic microorganisms as before. In other words, when a multi-purpose floating filter material with a buoyancy equal to the weight of the filter material is placed in an aeration tank into which air or pure oxygen is blown out from an aeration device, and the material is moved through the flow with a swirling flow, the In addition, aerobic microorganisms are resistant to propagation on the outer surface of the hollow body 3 of the multipurpose floating filter medium and the inlet portion of the pleats 4, and these microorganisms decompose and nitrify organic matter in the sewage components.
該ろ材の、ひだ4の深部と、中空物体3の内側附近は、
散気装置の空気がとどかず嫌気性の状態となる。烙て、
流入した有機性窒素、アンモニヤ性窒素、亜硝酸性窒素
は、さきの好気性微生物の働きで硝化され、硝酸性窒素
に変る。この硝化された硝酸性窒素が、該ろ材の嫌気性
部分で嫌気性微生物の作用により脱窒されるのである。The deep part of the folds 4 of the filter medium and the vicinity of the inside of the hollow object 3 are as follows:
The air from the air diffuser cannot reach the air, resulting in an anaerobic condition. Roast it,
The inflowing organic nitrogen, ammonia nitrogen, and nitrite nitrogen are nitrified by the action of aerobic microorganisms and converted to nitrate nitrogen. This nitrified nitrate nitrogen is denitrified by the action of anaerobic microorganisms in the anaerobic portion of the filter medium.
次に、脱りん、についてであるが、実施例の素材は鉄製
であり、下水中を浮遊することによシ次第に腐蝕し、か
つ、ひだ4、及び、中空物体3の外面、内面に微生物が
耐着し粘性のある状態となる。素材の鉄は、その一部が
鉄イオンに変り、これが、下水中に溶解している、りん
酸と化合し、 1゜」
りん酸鉄となり沈でんする。又りん酸の一部は好気性微
生物に吸収され微生物死滅後汚泥となり沈でんする。Next, regarding dephosphorization, the material in the example is made of iron, which gradually corrodes as it floats in sewage, and microorganisms are present on the outer and inner surfaces of the pleats 4 and the hollow object 3. It becomes sticky and sticky. A portion of the iron material turns into iron ions, which combine with phosphoric acid dissolved in the sewage to become iron phosphate and precipitate. A part of the phosphoric acid is absorbed by aerobic microorganisms, and after the microorganisms die, it becomes sludge and settles.
さて、発明の効果であるが、好気性微生物による有機物
の分解、及び、硝化作用は、すでに一般に確認され標準
活性汚泥法に賞用され、嫌気性微生物による脱窒も潜没
式回転円板等の実験により、その効果は確認されている
。また、脱りん、については土壌中の粘土層は脱りん効
果が知られている。これは、粘土中に鉄イオンを多く含
むからである。従って、この多目的浮遊ろ材は、有機物
の分解、硝化、脱窒、及び、脱9ん、に効果がある。Now, regarding the effects of the invention, the decomposition of organic matter and nitrification by aerobic microorganisms have already been generally confirmed and used in the standard activated sludge method, and denitrification by anaerobic microorganisms can also be achieved using submerged rotating disks. Its effectiveness has been confirmed through experiments. Regarding dephosphorization, the clay layer in the soil is known to have a dephosphorizing effect. This is because clay contains a lot of iron ions. Therefore, this multipurpose floating filter medium is effective in decomposing organic matter, nitrification, denitrification, and denitrification.
第1図は側面図、第2図は平面図、第3図は第1図A−
A断面図。Figure 1 is a side view, Figure 2 is a plan view, Figure 3 is Figure 1A-
A sectional view.
Claims (1)
の大なる金属素材からなり、ひだ(4)、及び、浮力室
(1)を有する、ろ材を投入し、曝気槽内の散気装置に
より生起される下水の旋回流とともに、該ろ材を浮遊さ
せて、下水成分中の有機物の分解、脱窒、及び、脱りん
、を同時に行わせることを特徴とする、下水成分中の有
機物の分解、脱窒、及び、脱りん、を同時に行わせる方
法。 2 イオン化傾向の大なる金属素材からなる、中空物体
(3)、ひだ(4)、及び、浮力室(1)をスペーサー
(2)等で組み立てて作られた、下水成分中の有機物の
分解、脱窒、及び、脱りん、を同時に行わせることを特
徴とする多目的浮遊ろ材。[Claims] 1. A filter medium made of a metal material with a high ionization tendency and having pleats (4) and a buoyancy chamber (1) is placed in an aeration tank of a sewage treatment facility, etc., and aeration is carried out. A sewage system characterized in that the filter medium is suspended along with the swirling flow of sewage generated by an aeration device in the tank to simultaneously perform decomposition, denitrification, and dephosphorization of organic matter in the sewage components. A method of simultaneously performing decomposition, denitrification, and dephosphorization of organic matter in components. 2 Decomposition of organic matter in sewage components made by assembling hollow objects (3), folds (4), and buoyancy chambers (1) made of metal materials with a high ionization tendency with spacers (2), etc. A multi-purpose floating filter medium characterized by simultaneous denitrification and dephosphorization.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59125701A JPS614597A (en) | 1984-06-18 | 1984-06-18 | Method for simultaneously decomposing, denitrifying and dephosphorizing organic material in sewage component and multipurpose floating filter medium used in said method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59125701A JPS614597A (en) | 1984-06-18 | 1984-06-18 | Method for simultaneously decomposing, denitrifying and dephosphorizing organic material in sewage component and multipurpose floating filter medium used in said method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS614597A true JPS614597A (en) | 1986-01-10 |
JPH024357B2 JPH024357B2 (en) | 1990-01-26 |
Family
ID=14916574
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59125701A Granted JPS614597A (en) | 1984-06-18 | 1984-06-18 | Method for simultaneously decomposing, denitrifying and dephosphorizing organic material in sewage component and multipurpose floating filter medium used in said method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS614597A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02137999U (en) * | 1989-04-19 | 1990-11-16 |
-
1984
- 1984-06-18 JP JP59125701A patent/JPS614597A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02137999U (en) * | 1989-04-19 | 1990-11-16 |
Also Published As
Publication number | Publication date |
---|---|
JPH024357B2 (en) | 1990-01-26 |
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