JPS6031895A - High degree treatment of organic sewage - Google Patents

High degree treatment of organic sewage

Info

Publication number
JPS6031895A
JPS6031895A JP58137699A JP13769983A JPS6031895A JP S6031895 A JPS6031895 A JP S6031895A JP 58137699 A JP58137699 A JP 58137699A JP 13769983 A JP13769983 A JP 13769983A JP S6031895 A JPS6031895 A JP S6031895A
Authority
JP
Japan
Prior art keywords
treatment
sewage
org
ozone
anaerobic
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
Application number
JP58137699A
Other languages
Japanese (ja)
Other versions
JPH0659480B2 (en
Inventor
Kazuyoshi Honda
本田 一好
Kouichi Takekura
竹倉 紘一
Yasuo Yoshinaga
吉永 康男
Makoto Ueda
誠 植田
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP13769983A priority Critical patent/JPH0659480B2/en
Publication of JPS6031895A publication Critical patent/JPS6031895A/en
Publication of JPH0659480B2 publication Critical patent/JPH0659480B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • Y02W10/12

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To efficiently treat org. sewage, by a method wherein ozone treatment is applied to org. sewage which undergone biological nitration and denitrification treatment and the treated sewage is subsequently held under an anaerobic atmosphere with a specific dissolved oxygen amount or less. CONSTITUTION:After known biological nitration and denitrification treatment is applied to org. sewage, flocculative precipitation treatment due to aluminum sulfate is performed and gas (with an ozone concn. of 28mg/Nm<3>) obtained by ozonating gas containing 90vol% of oxygen is injected into the obtained supernatant water to treat the same. Subsequently, biological anaerobic treatment (with DO concn. of<=0.5mg/l) is applied to treated water in an anaerobic bed packed with honeycomb tubes. By this method, the high degree treatment of org. sewage can be performed extremely efficiently and treated water with excellent water quality is obtained but, when higher water quality is required, treatment such as sand filtering is subsequently performed.

Description

【発明の詳細な説明】 技術分野 本発明は、有機性汚水の高度処理方法区間する。[Detailed description of the invention] Technical field The present invention relates to an advanced treatment method for organic wastewater.

技術の背景 し尿や下水等の有機性汚水のBOD及び窒素化合物を除
去する方法として、生物学的硝化脱窒票決はよく知られ
ている。有機性汚水を微生物の作用による硝化及び脱窒
素処理に付する方法である。
Background of the Technology Biological nitrification and denitrification is a well-known method for removing BOD and nitrogen compounds from organic wastewater such as human waste and sewage. This is a method in which organic wastewater is subjected to nitrification and denitrification treatment by the action of microorganisms.

しかし、生物学的硝化脱窒票決では、生物学的難分解性
の有機物及び窒素化合物を除去することができないとい
う問題がある。例えば、し尿を無稀釈で処理する場合、
トータル窒素(T−N)は20〜50q/lが限界であ
シ、更に高度な処理を生物学的な方法により達成するこ
とは困難である。
However, biological nitrification and denitrification methods have a problem in that they cannot remove biologically persistent organic matter and nitrogen compounds. For example, when processing human waste without dilution,
The limit for total nitrogen (T-N) is 20 to 50 q/l, and it is difficult to achieve more advanced treatment by biological methods.

このような生物学的硝化脱窒票決によ多処理された二次
処理水を更に高度処理するための方法として、従来イオ
ン交換樹脂法、活性炭法、オゾン処理法等が知られてい
るけれども、イオン交換樹脂法及び活性炭法では、十分
な処理水が得られず、場合によっては所定の水質規準を
満足し得ないことがある。一方、オゾン処理法を適用し
、オゾンを用いて高度処理を行うと、BOD成分が増加
することが知られている。即ち、オゾンにより、二次処
理水中の生物学的難分解成分が生物学的に分解可能な有
機物に分解されるのである。しかして、このようなオゾ
ン処理においては、CODや色度等が効率的に除去され
るものの、BOD成分の増加が極めて好ましくないもの
とされていたのである。
Conventionally, the ion exchange resin method, activated carbon method, ozone treatment method, etc. are known as methods for further advanced treatment of secondary treated water that has been subjected to multiple treatments by biological nitrification and denitrification. In the ion exchange resin method and the activated carbon method, sufficient treated water cannot be obtained, and in some cases, predetermined water quality standards may not be satisfied. On the other hand, it is known that when an ozone treatment method is applied and advanced treatment is performed using ozone, the BOD component increases. That is, ozone decomposes biologically difficult-to-decompose components in the secondary treated water into biologically degradable organic substances. In such ozone treatment, although COD, chromaticity, etc. are efficiently removed, the increase in BOD components is extremely undesirable.

発明の概要 本発明者らは、上記の如き二次処理水のオゾンによる高
度処理について種々検討の過程において、オゾン処理に
より生物学的難分解性の有機物が生物学的に分解可能な
有機物に分解されると同時に、生物学的難分解性の窒素
成分もまた亜硝酸態窒素(No□−N)又は硝酸態窒素
(N OS−N )に分解されるとと、従って、オゾン
処理後更に生物学的処理をすることにより容易に有機物
と窒素を除去し得ることを見出したのである。
Summary of the Invention In the course of various studies on the advanced treatment of secondary treated water with ozone as described above, the present inventors discovered that biologically persistent organic matter was decomposed into biologically degradable organic matter by ozone treatment. At the same time, biologically persistent nitrogen components are also decomposed into nitrite nitrogen (No□-N) or nitrate nitrogen (NOS-N). They discovered that organic matter and nitrogen can be easily removed by chemical treatment.

従って、本発明は有機性汚水の高度処理方法を提供する
ものであって、との方法は有機性汚水を生物学的硝化脱
窒米処理に付し、この処理水をオゾン処理し、次いでと
のオゾン処理水を溶存酸素量0.5■/を以下の嫌気性
雰囲気下に保持することを特徴とする。
Therefore, the present invention provides an advanced treatment method for organic sewage, which involves subjecting organic sewage to biological nitrification and denitrification treatment, treating this treated water with ozonation, and then performing the following steps. The ozonated water is maintained in an anaerobic atmosphere with an amount of dissolved oxygen of 0.5 μ/cm as follows.

発明の構成の具体的説明 生物学的硝化脱窒米処理は公知のいかなる方法によって
も行うことができる。また、この処理水を直接オゾン処
理に付してもよく、あるいはこの処理水を次いで1−集
沈澱処理に付し、その上澄水をオゾン処理してもよい。
Detailed Description of the Structure of the Invention Biological nitrification-denitrification rice treatment can be performed by any known method. Moreover, this treated water may be directly subjected to ozonation treatment, or this treated water may then be subjected to 1-collection sedimentation treatment, and the supernatant water may be ozonated.

オゾン処理もまた公知のいかなる方法によっても行うこ
とができる。
Ozone treatment can also be performed by any known method.

オゾン処理は、一般には、オゾン発生器を通過させた大
気を二次処理水中に注入することによシ行われる。ある
いは、このオゾン処理は水なくとも50容量%の酸素を
含むガスをオゾン発生器によりオゾン化し、これを二次
処理水中に注入することによジ行うこともでき、この場
合にはオゾン化した大気を用いる場合に比較して生物学
的難分解性の有機物及び窒素化合物の分解がより促進さ
れるので好ましい。
Ozonation is generally performed by injecting atmospheric air passed through an ozone generator into the secondary treated water. Alternatively, this ozone treatment can also be carried out by ozonizing a gas containing at least 50% oxygen by volume using an ozone generator and injecting it into the secondary treatment water. This is preferable because the decomposition of biologically persistent organic substances and nitrogen compounds is more accelerated than in the case of using air.

本発明の方法においては、オゾン処理された処理水は、
次いで溶存酸素量(Do)0.5■/を以下の嫌気性雰
囲気下に保持される。これにより、嫌気性の生物処理が
達成されることになり、難分解成分の分解によ2り生成
したBOD成分を資化して脱窒素が進行する。このとき
、場合により、メタノール等の炭素源を添加してもよい
。あるいは、BOD成分が過剰である場合には、次いで
好気性雰囲気下に生物処理を行ってもよい。
In the method of the present invention, the ozonated treated water is
Next, the amount of dissolved oxygen (Do) is maintained in the following anaerobic atmosphere at 0.5 .mu./. As a result, anaerobic biological treatment is achieved, and denitrification progresses by assimilating BOD components produced by decomposition of difficult-to-decompose components. At this time, a carbon source such as methanol may be added depending on the case. Alternatively, if the BOD component is in excess, biological treatment may then be performed in an aerobic atmosphere.

オゾン処理水の嫌気性雰囲気下における保持はいかなる
方法によってもよい。例えば、系を密閉することにより
酸素を含むガスとの接触を断つことによって行うことも
できる。しかし、一般には、オゾン処理水d、既に生物
学的硝化脱窒素に付されているので、BOD、T−N等
はいずれも低濃度に保持されており、従って通常の活性
汚泥法のような懸濁型の方式では汚泥濃度維持が困難で
ある。
Any method may be used to maintain the ozonated water in an anaerobic atmosphere. For example, it can also be carried out by sealing the system to cut off contact with the oxygen-containing gas. However, in general, ozonated water d has already been subjected to biological nitrification and denitrification, so BOD, TN, etc. are all kept at low concentrations, and therefore, unlike the normal activated sludge method, It is difficult to maintain sludge concentration with suspension type systems.

しかして、有用な処理方式としては、例えば、/・ニカ
ムチ路−プを充填して生物膜を形成せしめるような嫌気
性3床方式や回転円板を用いる方式、又は炉材(例えば
砂)を充填して生物膜を形成せしめるような接触濾過方
式等がある。
Therefore, useful treatment methods include, for example, an anaerobic three-bed method in which a biofilm is formed by filling a pipe with nicum, a method using a rotating disk, or a method using a furnace material (e.g. sand). There are contact filtration methods that allow filling to form a biofilm.

このような本発明の方法によれば、有機性汚水の極めて
効率的な高度処理を達成することができ、優れた水質の
処理水が得られるのであるが、更に高い水質が要求され
る場合には次いで砂ν過等の処理を更に行ってもよい。
According to the method of the present invention, highly efficient advanced treatment of organic wastewater can be achieved and treated water of excellent quality can be obtained. However, when even higher water quality is required, Then, a further treatment such as sand filtration may be performed.

実施例 以下、実施例により本発明を更に説明する。Example The present invention will be further explained below with reference to Examples.

実施例1 除渣し尿を、無稀釈で、硝化液循環方式による生物学的
硝化脱窒米処理に付し、次いで硫酸ばん土によす凝集沈
澱処理した。得られた上澄水に、90容量%の酸素を含
有するガスをオゾン化したガス(オゾン濃度28111
F/ Nms )を注入してオゾン処理した後、ハニカ
ムチ二−プを充填した嫌気性3床で生物学的嫌気処理(
Do O,5tq/を以下)と次いで生物学的好気処理
とを行った。処理の条件及び各段階の処理水の水質は次
の通りであった。
Example 1 Removed human waste was subjected to biological nitrification and denitrification treatment using a nitrification solution circulation method without dilution, and then subjected to coagulation and sedimentation treatment using sulfuric acid clay. A gas obtained by ozonizing a gas containing 90% by volume of oxygen (ozone concentration 28111) was added to the obtained supernatant water.
After ozone treatment by injecting F/Nms), biological anaerobic treatment (
DoO, 5 tq/) followed by biological aerobic treatment. The treatment conditions and the quality of treated water at each stage were as follows.

オゾン処理条件 オゾン注入率 400 q/を 反応塔滞留時間 60分 生物処理条件 嫌気部滞留時間 60分 メタ/−ル添加率 301nf/を 好気部滞留時間 30分 処理水質 処理水質を下記第1表に要約して示す。Ozone treatment conditions Ozone injection rate: 400 q/ Reaction tower residence time 60 minutes Biological treatment conditions Anaerobic section residence time 60 minutes Metal/-ol addition rate 301nf/ Aerobic section residence time: 30 minutes Treated water quality The treated water quality is summarized in Table 1 below.

第 1 表 実施例2 実施例1と同一の条件下に処理を行ったが、しかしここ
では空気をオゾン化したガス(オゾン濃度8■/Nm3
)を用いてオゾン処理した。
Table 1 Example 2 The treatment was carried out under the same conditions as in Example 1, but here ozonized air (ozone concentration 8/Nm3) was used.
) was used for ozone treatment.

各段階の処理水の水質は下記の第2表に示す通りであっ
た。
The quality of the treated water at each stage was as shown in Table 2 below.

Claims (1)

【特許請求の範囲】[Claims] 1、有機性汚水を生物学的硝化脱窒素処理に付し、この
処理水をオゾン処理し、次いでこのオゾン処理水を溶存
酸素量0.511Q/を以下の嫌気性雰囲気下に保持す
ることを特徴とする有機性汚水の高度処理方法。
1. Subject organic wastewater to biological nitrification and denitrification treatment, treat this treated water with ozonation, and then maintain this ozonated water in an anaerobic atmosphere with a dissolved oxygen amount of 0.511Q/ below. Features: Advanced treatment method for organic wastewater.
JP13769983A 1983-07-29 1983-07-29 Advanced treatment method for organic wastewater Expired - Lifetime JPH0659480B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13769983A JPH0659480B2 (en) 1983-07-29 1983-07-29 Advanced treatment method for organic wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13769983A JPH0659480B2 (en) 1983-07-29 1983-07-29 Advanced treatment method for organic wastewater

Publications (2)

Publication Number Publication Date
JPS6031895A true JPS6031895A (en) 1985-02-18
JPH0659480B2 JPH0659480B2 (en) 1994-08-10

Family

ID=15204742

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13769983A Expired - Lifetime JPH0659480B2 (en) 1983-07-29 1983-07-29 Advanced treatment method for organic wastewater

Country Status (1)

Country Link
JP (1) JPH0659480B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007111698A (en) * 2006-12-26 2007-05-10 Asahi Soft Drinks Co Ltd Method for treating waste water and apparatus therefor

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5763197A (en) * 1980-10-02 1982-04-16 Ebara Infilco Co Ltd High degree treatment of organic sewage

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5763197A (en) * 1980-10-02 1982-04-16 Ebara Infilco Co Ltd High degree treatment of organic sewage

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007111698A (en) * 2006-12-26 2007-05-10 Asahi Soft Drinks Co Ltd Method for treating waste water and apparatus therefor
JP4516952B2 (en) * 2006-12-26 2010-08-04 アサヒ飲料株式会社 Wastewater treatment equipment

Also Published As

Publication number Publication date
JPH0659480B2 (en) 1994-08-10

Similar Documents

Publication Publication Date Title
JP3531481B2 (en) Wastewater treatment method and apparatus
JPH07124593A (en) Highly advanced water purifying treatment method
JPH01199694A (en) Waste water treatment by activated sludge method
CN109775903B (en) Advanced treatment method of acrylic fiber wastewater
JP3374386B2 (en) Wastewater nitrogen removal method and apparatus
JPH0788500A (en) Method for treating sewage countercurrent water
JPH06178995A (en) Anaerobic digestion treatment of organic waste water
JPS6031895A (en) High degree treatment of organic sewage
JP3377346B2 (en) Organic wastewater treatment method and apparatus
JP3402411B2 (en) Nitrogen treatment method for wastewater
JPH02164500A (en) Water purifying treatment apparatus
KR100470350B1 (en) Method for disposing of livestock waste water
JP2946163B2 (en) Wastewater treatment method
KR100325722B1 (en) A treatment method of sewage and wastewater using ozone and oxygen
JPH08267077A (en) High degree treating method of waste water
JP3178975B2 (en) Water treatment method
CN108455790A (en) A kind of biochemistry and deep treatment method of coking wastewater
JP3139337B2 (en) Method and apparatus for treating liquid waste containing high COD and high nitrogen compounds
JPH0141115B2 (en)
JPH02303598A (en) Treatment of organic matter-containing water
JPS60129194A (en) Treatment of sewage
JPH05277475A (en) Treatment method for water containing organic substance
KR100228739B1 (en) Disposal method of organic wastewater using oxygen
JP3148498B2 (en) Treatment of wastewater containing ammonia
JPH04310299A (en) Method for highly treating raw clean water and apparatus therefor