JPS58159894A - Treatment of sewage by fluidized bed type apparatus - Google Patents

Treatment of sewage by fluidized bed type apparatus

Info

Publication number
JPS58159894A
JPS58159894A JP57043427A JP4342782A JPS58159894A JP S58159894 A JPS58159894 A JP S58159894A JP 57043427 A JP57043427 A JP 57043427A JP 4342782 A JP4342782 A JP 4342782A JP S58159894 A JPS58159894 A JP S58159894A
Authority
JP
Japan
Prior art keywords
sewage
moldings
sludge
added
fluidized bed
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
JP57043427A
Other languages
Japanese (ja)
Inventor
Nobutoshi Maeda
前田 展利
Hiroshi Matoba
的場 浩
Hiroaki Ida
井田 宏明
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.)
Unitika Ltd
Original Assignee
Unitika Ltd
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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP57043427A priority Critical patent/JPS58159894A/en
Publication of JPS58159894A publication Critical patent/JPS58159894A/en
Pending legal-status Critical Current

Links

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
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PURPOSE:To improve the treating performance for sewage in a biological treatment method for sewage by a fluidized bed type apparatus, by using the moldings produced by fixing sludge with a polymer resins a fluid media. CONSTITUTION:Thermosetting resin is added to the cake obtd. by dehydrating the excess sludge produced in treatments of sewage, night soil, etc. and after granulation, the mixture is heated and cured, whereby moldings are obtd. The resins used are phenolic, melamine and urea resins, and are added to the sludge in the form of a precondensate. The resulted spherical sludge moldings have strength and low apparent specific density and float in water usually; therefore, if a prescribed amt. of such moldings are added in an aeration tank, the moldings form a fluidized and suspended state easily. If sewage is supplied continuously into such aeration tank, all the surfaces of the moldings have tachiness on account of aerobic microorganisms, and the treating performance is thus increased.

Description

【発明の詳細な説明】 本発明は、汚水の流動床式生物処理方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fluidized bed biological treatment method for wastewater.

汚水を生物学的に処理する方法としては、従来活性汚泥
法が主流であったが、最近では1回転円板法、接触暖気
法等の固定床処理方式もかなり普及している。固定床方
式の特徴は、維持管理が容易であり、汚泥発生量が少な
く、II素の硝化効率が高く、脱窒し易い等の長所があ
るが2反面単位体積当たりの処理効率が低Oい欠点があ
る。
Conventionally, the activated sludge method has been the mainstream method for biologically treating wastewater, but recently, fixed bed treatment methods such as the single rotating disk method and the contact warming method have also become quite popular. The fixed bed system has advantages such as easy maintenance, low sludge generation, high nitrification efficiency of element II, and easy denitrification, but on the other hand, the treatment efficiency per unit volume is low. There are drawbacks.

最近、固定床式処理の処理効率を上げる方法として、砂
やアンソラサイトの様な細かい粒子を用い、流動化させ
ながら粒子に汚泥を付着させて処理する方法が研究され
ている。しかしながら、砂やアンソラサイトのような細
かい粒子を均等に分散流動させることが困難であり、又
たとえ粒子の流動化を良好にした場合でも各粒子に対す
る汚泥の付着状態が悪く添加粒子の3分の1程度にしか
付着しないのが実情である。
Recently, as a method to increase the treatment efficiency of fixed bed treatment, research has been conducted on a method of treating sludge by using fine particles such as sand or anthracite and attaching sludge to the particles while fluidizing them. However, it is difficult to uniformly disperse and fluidize fine particles such as sand and anthracite, and even if the particles are fluidized well, the adhesion of sludge to each particle is poor, and 3% of the added particles The reality is that it only adheres to about 1 of these.

本発明者は、上記のような欠点を解消した流動床式生物
学的処理方法について鋭意研究を行った結果本発明を完
成するに至った。
The present inventor has completed the present invention as a result of intensive research into a fluidized bed biological treatment method that eliminates the above-mentioned drawbacks.

即ち9本発明は、汚水の流動床武生オυ処理方法におい
て、fN動媒体として汚泥を高分子樹脂で固化した成形
物を用いることを特徴とする流動床式汚水処理方法であ
る。
That is, the present invention is a fluidized bed sewage treatment method characterized in that a molded product of sludge solidified with a polymer resin is used as the fN moving medium in the fluidized bed sewage treatment method.

本発明の方法において、流動媒体として用いる成形物は
、下水やし尿等の処理で発生する余剰汚泥を脱水して得
られるケークIC熱硬化性v1脂を添加し、造粒後加熱
、硬化させたものである。使用するl!1Iil脂とし
ては、フェノール系樹脂、メラミン系at脂、尿素系樹
脂等であり、いずれも初期縮合物の形で汚泥1cIla
加するうその添加量としては。
In the method of the present invention, the molded product used as the fluidizing medium is prepared by adding cake IC thermosetting V1 fat obtained by dewatering surplus sludge generated in the treatment of sewage, night soil, etc., and heating and hardening it after granulation. It is something. l to use! 1Iil fats include phenolic resins, melamine AT fats, urea resins, etc., and all of them are used as sludge 1cIla in the form of initial condensates.
As for the amount of lie added.

乾燥汚泥に対して50〜500優程度であり、好ましく
は100〜300 %である。造粒は一般に転勤式造粒
機な用いる。ケークに樹脂を添加して均−Cfi合し、
予備乾燥後造粒する。
The amount is approximately 50 to 500%, preferably 100 to 300%, relative to dry sludge. For granulation, a transfer type granulator is generally used. Adding resin to the cake and homogenizing Cfi,
After preliminary drying, it is granulated.

なお、造粒時の含水率の調整剤として、活性廣。In addition, Active Hiro is used as a moisture content regulator during granulation.

度素、焼却残灰等を必要に応じて添加する。造粒成形物
の加熱硬化は100〜200℃で30分〜5時間程度で
行なう。造粒成形物は通常球状で、約5〜30moφ程
度、好ましくは5〜10 mmφ程度である。
Add hydrogen, incineration ash, etc. as necessary. The granulated molded product is heat-cured at 100 to 200°C for about 30 minutes to 5 hours. The granulated molded product is usually spherical and has a diameter of about 5 to 30 mm, preferably about 5 to 10 mm.

上記のごとく成形して得られた球状汚泥成形物は1強度
もあり、見掛は比重も低く9通常水に浮くものである。
The spherical sludge molded product obtained by molding as described above has a strength of 1, has a low apparent specific gravity, and usually floats on water.

球状汚泥成形物例えば5 ma+−のものを用い、曝気
槽内に所定量を添加すると、成形物は軽いので容易に流
動浮遊状態を形成する。このような曝気槽にBOD約1
20 ppmの下水を連続通水したところ、約2日日か
ら処理水のBODが低下し始め、3日後には処理水のB
ODは約20 pP”に低下した。又球状汚泥成形物を
取り出し表面を観察した結果、成形物の表面はすべて粘
着性をおびており、その粘着物を顕微鏡で観察した結果
When a spherical sludge molded product, for example, 5 ma+- is used and a predetermined amount is added to the aeration tank, the molded product is light and easily forms a fluidized floating state. In such an aeration tank, the BOD is approximately 1
When 20 ppm sewage was continuously passed through, the BOD of the treated water started to decrease from about 2 days, and after 3 days, the BOD of the treated water started to decrease.
The OD decreased to approximately 20 pP''.The spherical sludge molded product was taken out and the surface was observed, and the surface of the molded product was all sticky, and the sticky material was observed under a microscope.

好気性微生物であることを確認した。又はとんどの粒子
に微生物が付着していた。種汚泥の添加もなしにこのよ
うに早く、微生物膜層が形成し、処二区 理性能が上昇したことは驚くべきである。この坦△ 由については十分に明らかではないが9本発明の方法に
おいて流動媒体として用いる粒子が汚泥からの成形物で
あり、しかもこの汚泥は死化しているものの化学構造的
には微生物と同質であり、従って微生物生育のすぐれた
培地となるものと考えられる、 以下実施例により本発明を具体的に説明する。
It was confirmed that it was an aerobic microorganism. Or microorganisms were attached to most of the particles. It is surprising that a microbial film layer was formed so quickly and the treatment performance improved without the addition of seed sludge. Although the reason for this is not fully clear,9 the particles used as the fluid medium in the method of the present invention are formed from sludge, and although this sludge is dead, its chemical structure is the same as that of microorganisms. The present invention will be specifically explained below with reference to Examples.

実施例 し尿処理から発生する余剰汚泥脱水ケーク(含水185
%)IC)リメテロールメラミンを乾燥汚泥に対し、−
C150鵞添加して均一に混合し、予備乾燥して含水率
を下げ、造粒機にかけて、平均粒径6゛°φ0粒子造粒
する・次いT 150″′で加熱硬化  ;させ粒径約
5mmφ4L度の球状汚泥成形物を得た。
Example Excess sludge dewatered cake generated from human waste treatment (water content 185
%) IC) Limeterol melamine to dried sludge, -
Add C150 and mix uniformly, pre-dry to lower the moisture content, apply to a granulator to granulate particles with an average particle size of 6゛°φ0, and then heat harden at T150''; the particle size is approx. A spherical sludge molded product with a diameter of 5 mm and a diameter of 4 L was obtained.

この球状汚泥成形物(見掛は比重0.55 )  50
個を容積11の曝気槽に入れ、空気4 j/hでエアー
旅回させた。この曝気槽にBOD120pPDlの下水
を0.3J/hの流量で連続通水した。通水開始後2日
目から処理水のBODが低下して55Pp!11となり
、5日後には処理水BODは21 Pp!I Ic低下
した。又球状汚泥成形物の表面を観察した結果、粘着性
の好気性微生物が繁殖していた。その後約2遍間汚水を
連続通水した結果、処理水のBODはほぼ20ppmを
維持し、良好な処理状態を続行することができた。
This spherical sludge molding (apparent specific gravity 0.55) 50
The sample was placed in an aeration tank with a volume of 11, and air was circulated at 4 j/h. Sewage with a BOD of 120 pPDl was continuously passed through this aeration tank at a flow rate of 0.3 J/h. From the second day after water flow started, the BOD of treated water decreased to 55Pp! 11, and after 5 days the treated water BOD was 21 Pp! I Ic decreased. Furthermore, as a result of observing the surface of the spherical sludge molding, sticky aerobic microorganisms were found to be growing. Thereafter, as a result of continuously passing wastewater for about two hours, the BOD of the treated water was maintained at approximately 20 ppm, and a good treatment condition could be continued.

一方比較のためこの曝気槽を用い、#状汚泥成形物50
個の代りに同体積のアンソフサイトを加え同様にエアー
旋回させ、  BOD120ppmの下水を上記と同一
条件で処理した。その結果、汚水通水後2週間経過して
も処理水のBODは低下しなかった。そこで種汚泥を入
れて約2週間1kgIIシた結果処理水のBODは約7
0ppm+に低下した。その後も処理を続行したが、処
理水のBODは70ppm以下にはならなかった。
On the other hand, for comparison, using this aeration tank, #-shaped sludge molded product 50
The same volume of anthofsite was added in place of the chlorine, and air was swirled in the same manner, and sewage with a BOD of 120 ppm was treated under the same conditions as above. As a result, the BOD of the treated water did not decrease even after two weeks had passed after the wastewater was passed through. So I added 1kg of seed sludge for about 2 weeks, and as a result, the BOD of the treated water was about 7.
It decreased to 0 ppm+. Although the treatment was continued thereafter, the BOD of the treated water did not fall below 70 ppm.

特許出願人  ユニチカ株式会社Patent applicant: Unitika Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] (1)汚水の流動床式生物処理方法において、流動媒体
として汚泥を高分子樹脂で固化した成形物を用いること
を特徴とする流動床式汚水処理方法。
(1) A fluidized bed biological treatment method for sewage, characterized in that a molded product of sludge solidified with a polymer resin is used as the fluid medium.
JP57043427A 1982-03-17 1982-03-17 Treatment of sewage by fluidized bed type apparatus Pending JPS58159894A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57043427A JPS58159894A (en) 1982-03-17 1982-03-17 Treatment of sewage by fluidized bed type apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57043427A JPS58159894A (en) 1982-03-17 1982-03-17 Treatment of sewage by fluidized bed type apparatus

Publications (1)

Publication Number Publication Date
JPS58159894A true JPS58159894A (en) 1983-09-22

Family

ID=12663395

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57043427A Pending JPS58159894A (en) 1982-03-17 1982-03-17 Treatment of sewage by fluidized bed type apparatus

Country Status (1)

Country Link
JP (1) JPS58159894A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6217395U (en) * 1985-07-15 1987-02-02
JPS6227096A (en) * 1985-07-29 1987-02-05 Mitsubishi Plastics Ind Ltd Microorganism holding body
EP1234803A1 (en) * 2001-02-21 2002-08-28 Hitachi Plant Engineering & Construction Co., Ltd. Immobilized microorganisms support, method for manufacturing the same and method for environment decontamination therewith
JP2004167471A (en) * 2002-11-05 2004-06-17 Nippon Steel Chem Co Ltd Water treatment material, nitrate nitrogen treating material, and its production method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6217395U (en) * 1985-07-15 1987-02-02
JPS6227096A (en) * 1985-07-29 1987-02-05 Mitsubishi Plastics Ind Ltd Microorganism holding body
EP1234803A1 (en) * 2001-02-21 2002-08-28 Hitachi Plant Engineering & Construction Co., Ltd. Immobilized microorganisms support, method for manufacturing the same and method for environment decontamination therewith
US6916651B2 (en) 2001-02-21 2005-07-12 Hitachi Plant Engineering & Construction Co., Ltd. Heat treated immobilized microorganism support for enviroment remediation
JP2004167471A (en) * 2002-11-05 2004-06-17 Nippon Steel Chem Co Ltd Water treatment material, nitrate nitrogen treating material, and its production method
JP4545408B2 (en) * 2002-11-05 2010-09-15 新日鐵化学株式会社 Water treatment material, nitrate nitrogen treatment material and production method thereof

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