JPS60183095A - Preparation of carrier for fluidized bed biological treatment apparatus - Google Patents

Preparation of carrier for fluidized bed biological treatment apparatus

Info

Publication number
JPS60183095A
JPS60183095A JP59037272A JP3727284A JPS60183095A JP S60183095 A JPS60183095 A JP S60183095A JP 59037272 A JP59037272 A JP 59037272A JP 3727284 A JP3727284 A JP 3727284A JP S60183095 A JPS60183095 A JP S60183095A
Authority
JP
Japan
Prior art keywords
parts
carrier
particle size
polyvinyl alcohol
water
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
JP59037272A
Other languages
Japanese (ja)
Other versions
JPH0221317B2 (en
Inventor
Kozo Konishi
小西 功三
Shigemitsu Matsuoka
松岡 栄満
Takumi Kurosaka
黒坂 巧
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.)
Denka Consultant and Engineering Co Ltd
Original Assignee
Denka Consultant and Engineering Co 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 Denka Consultant and Engineering Co Ltd filed Critical Denka Consultant and Engineering Co Ltd
Priority to JP59037272A priority Critical patent/JPS60183095A/en
Publication of JPS60183095A publication Critical patent/JPS60183095A/en
Publication of JPH0221317B2 publication Critical patent/JPH0221317B2/ja
Granted 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

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To enhance the adhesiveness and inhabiting capacity of a microorganism, by adding 5-15pts.wt. of water to 100pts.wt. of perfectly saponified polyvinyl alcohol at 20-80 deg.C under stirring to form a granular fluidized bed carrier with a particle size of 5-15mm.. CONSTITUTION:5-15pts.wt. of water is added to 100pts.wt. of perfectly saponified polyvinyl alcohol at 20-80 deg.C under stirring to obtain a granular fluidized bed carrier with a particle size of 5-15mm.. The size of a carrier granule is set to 5-15mm. so as to be capable of easily separating activated sludge floc formed by waste water treatment by a screen. Concretely, 10pts.wt. of water is sprayed to 100pts.wt. of perfectly saponified polyvinyl alcohol (a polymerization degree is 1,000-2,500 and a saponification degree is 98mol% or more) at 20-80 deg.C under a stirring speed of 500-1,000rpm in a Henschel mixer and the resulting mixture is granulated for 5-20min to obtain a granular carrier with a particle size of 5-15mm..

Description

【発明の詳細な説明】 この発明は、生活廃水、し尿処理又は産業廃水処理に使
用される好気的又は鎌気的生物処理装置用の流動担体を
製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a fluid carrier for an aerobic or sickle gas biological treatment device used for the treatment of domestic wastewater, human waste or industrial wastewater.

廃水の生物学的酸化分解処理装置において固定床(接触
酸化)又は移動床(回転円板)が実用されているが、流
動床はその利点、即ち微生物膜の過剰付着によっても固
定床、移動床のように癌床の目詰まりがなく目、つ微生
物の棲息表面積を大きくできることが知られているに拘
らずあまり実用されていない。
Fixed beds (catalytic oxidation) or moving beds (rotating disks) are used in wastewater biological oxidative decomposition treatment equipment, but fluidized beds have the advantage of being overly attached with microbial films. Although it is known that this technique can increase the habitat surface area for microorganisms without clogging the cancer bed, it has not been put into practical use much.

この理由は、従来試みられた担体は、ポリエチレン又は
ポリプロピレンなどの疎水性素材で微生物の付着性が低
いこと、また付着性を改良するために提案された発泡体
も比重が軽すぎて浮上してしまい水中に万遍なく流動化
し難いという欠点があったことなどによる。また親水性
の活性炭、砂等は流動化し易い小径の場合は、活性汚泥
フロックとの分離に難点があり、大径の場合はフロフク
との分離性はよいが流動化に要する動力が大きくなると
いう欠点があった。
The reason for this is that the carriers tried in the past were made of hydrophobic materials such as polyethylene or polypropylene and had low adhesion to microorganisms, and the foams proposed to improve adhesion were also too light in specific gravity and did not float. This is due to the drawback that it is difficult to fluidize evenly in water. In addition, if hydrophilic activated carbon or sand has a small diameter that easily fluidizes, it is difficult to separate it from the activated sludge flocs, whereas if the diameter is large, the separation from the flocs is good, but the power required for fluidization increases. There were drawbacks.

本発明は微生物の付着性、棲息性に優れている一ト、流
動化に適した比重を有する親水性合成樹脂装担体の製造
法及びこの担体に活性炭微粉末をコーティングし又は及
び使用時に容易に活性化しうる微生物を予め伺着乾燥さ
せた微生物担体の製造法を提供するものである。
The present invention relates to a method for producing a hydrophilic synthetic resin-coated carrier that has excellent adhesion and habitability for microorganisms and has a specific gravity suitable for fluidization, and a method for coating this carrier with fine activated carbon powder and making it easy to use. The present invention provides a method for producing a microorganism carrier in which microorganisms that can be activated are preliminarily loaded and dried.

親木性合成樹脂としては完全鹸化ポリビニルアルコール
が最も効果的である。
Completely saponified polyvinyl alcohol is the most effective wood-philic synthetic resin.

これによって°熱水可溶、冷水不溶の性質を利用して加
温下では粒子同志が強固に結合した顆粒を形成させ、冷
水では砕けない形にすることができる上、生物学的に難
分解性であるので長期間のイー用に酎えうる。
By utilizing the property of being soluble in hot water and insoluble in cold water, it is possible to form granules in which particles are tightly bound together under heating, and not only to be able to form a shape that cannot be broken in cold water, but also to be biologically difficult to decompose. Since it is a sex, it can be used for long-term use.

更にこのものは接着性が強く、加温下で顆粒表面が容易
に溶融状態になるから微粉末活性炭をコーティングする
ことが容易であり、常温下ではこれが剥離し難いのであ
る6 また担体顆粒の大きさは、廃水処理の結果生成する活性
汚泥フロフク(2〜3mm)をスクリーンで容易に分離
できる 5〜f(mm以トで且つ水中で流動し易い15
mm以下であることが好ましく、この粒径はI;記素材
の造粒撹拌条件によって選択される。
Furthermore, this material has strong adhesive properties and the surface of the granules easily melts under heating, making it easy to coat with finely powdered activated carbon, which is difficult to peel off at room temperature6. The activated sludge fluff (2-3 mm) produced as a result of wastewater treatment can be easily separated with a screen.
The particle size is preferably 1 mm or less, and this particle size is selected depending on the granulation and agitation conditions of the material.

本発明において素材の加熱温度は20〜80℃、撹拌速
度は500〜11000rpの範囲であり、また素材1
00重都重贋添加する冷水の量は5〜15fl!量部が
適当である。
In the present invention, the heating temperature of the material is 20 to 80°C, the stirring speed is in the range of 500 to 11,000 rpm, and the material 1
The amount of cold water to add is 5 to 15 fl! The quantity is appropriate.

実施例1 ヘンシェルミキサ内で温i 20〜80 ”O1撹撹拌
度500〜11000rpの加熱攪拌下で完全鹸化ポリ
ビニルアルコ−)Lt (m 含炭1000〜2500
、帥化度88モル%以ト)lo。
Example 1 Completely saponified polyvinyl alcohol) Lt (m carbon-containing 1000-2500 rpm) in a Henschel mixer at a temperature of 20-80" O1 with a stirring degree of 500-11000 rpm.
, concentration of 88 mol% or more) lo.

重都部に対し冷水lO重酸部をスプレーし、 5〜20
分造粒して粒径 5〜15IIIIOの顆粒状担体を得
ることができた。
Spray cold water lO heavy acid parts on heavy urban areas, 5 to 20 minutes.
It was possible to obtain a granular carrier having a particle size of 5 to 15IIIO by granulation.

実施例2 実施例1で得た顆粒状担体を更に加熱攪拌しつつこれに
粒度200〜325メツシユ以[−の微粉末活性炭0.
5〜3部を徐々に添加して粒状物表面に微粉末活性炭を コーティングした顆粒状担体を得た。
Example 2 The granular carrier obtained in Example 1 was further heated and stirred and added with fine powder activated carbon having a particle size of 200 to 325 mesh or more [-0.
5 to 3 parts were gradually added to obtain a granular carrier coated with finely powdered activated carbon on the surface of the granules.

実施例3 実施例1の顆粒状担体を廃水の種類毎に有用な微生物培
養液に浸漬した後−20°Cの温度で24時間冷凍乾燥
して微生物を担持した担体を製造した。
Example 3 The granular carrier of Example 1 was immersed in a microorganism culture solution useful for each type of wastewater, and then freeze-dried at -20°C for 24 hours to produce a carrier supporting microorganisms.

実施例4 実施例2の活性炭コーティング顆粒担体を実施例3と同
様に処理して微生物担体を製造した。
Example 4 The activated carbon-coated granule carrier of Example 2 was treated in the same manner as in Example 3 to produce a microbial carrier.

1;配本発明の各40体を流動床生物処理装置に適用し
た場合、下記のような利点がある。
1; Distribution When each of the 40 bodies of the present invention is applied to a fluidized bed biological treatment apparatus, there are the following advantages.

従来の疎水性押体の場合は、好気的微生物に必要な酸素
を補給する際、生成した微生物膜剥離を避けるために間
接曝気を余儀なくされ、このため酸素の溶解効率が悪く
生物処理装置の効率が低いものであったが本発明押体は
微生物膜の付着性が強固であるから直接曝気が可能であ
り酸素の補給手段が自由になる。
In the case of conventional hydrophobic presses, when replenishing the oxygen necessary for aerobic microorganisms, indirect aeration is required to avoid the detachment of the formed microbial film, resulting in poor oxygen dissolution efficiency and problems with biological treatment equipment. Although the efficiency was low, since the microbial film of the press of the present invention has strong adhesion, direct aeration is possible and oxygen supply means are free.

未発QIJ担体の比重は被処理水比重に近いため直接曝
気によっても容易に流動化し接触効率が向にする。
Since the specific gravity of the undeveloped QIJ carrier is close to that of the water to be treated, it is easily fluidized even by direct aeration, and the contact efficiency is improved.

更に実施例(3) 、 (4)の微生物担持担体は処理
装置の馴致期間を数日に短縮できるものであり、従来の
如く工場休止時においても曝気をしなければならないよ
うな無駄を省くことができ、丁場稼動に応じて処理装置
を運転できる。
Furthermore, the microorganism-carrying carriers of Examples (3) and (4) can shorten the acclimatization period of the processing equipment to a few days, thereby eliminating the waste of conventional methods where aeration must be carried out even when the factory is shut down. The processing equipment can be operated according to the plant operation.

なお、担体表面に担持される微生物としてはメタン醗酵
菌の如き嫌気性微生物膜も担持可能である。
Note that as the microorganism supported on the surface of the carrier, an anaerobic microbial film such as methane-fermenting bacteria can also be supported.

下・糸六滓市汗騰’+hlj ■ ・11P1の表示 昭和59年特許TM第 37272 号2、発jlll
の名称 1令動床ノ1物処理装買用j+、4体の製潰法3 禎1
11−をする君 =lf性との1罪系 411.M 出納1人11 所 
東j:I’ m丁代RJ L%イT ”J till’
 l 1’ It 4 香1 ’=L。
Lower/Itoliokuji Kanteng' + hlj ■ ・Display of 11P1 1982 Patent TM No. 37272 No. 2, Issued jllll
Name of 1st year animal bed 1 material processing equipment j+, 4 body manufacturing and crushing method 3 Tei 1
You who do 11- = 1 sin system with lf sex 411. M Treasurer 1 person 11 locations
East j: I' m till RJ L% IT "J till"
l 1' It 4 incense 1'=L.

名称 デンカエンジニアリング 株式会ン1代表者 宮
 武 昭 玉 4代理人 5、補11−命令の114=Iけ (自発)6、補1]
−により増加する発IJIの数 ナシ7、補11のり、
j象 明細書中のヰ414’請東の範囲。
Name Denka Engineering Co., Ltd. 1 Representative Takeshi Miya Tama 4 Agent 5, Supplement 11 - Order 114 = Ike (Voluntary) 6, Supplement 1]
-The number of IJI increases due to N/A 7, Supplement 11 Nori,
j The range of ヰ414' in the specification.

8 補1[:の内容 別紙記載の通り。8 Supplement 1 [Contents of: As stated in the attached sheet.

ネ市 −1し己 書 1、特許請求の範囲を以下の通り補IFする。Neichi -1 Shiki's book 1. The scope of the claims is supplemented as follows.

2、特許請求の範囲 (1)完全鹸化ポリビニルアルコール l00i 量M
に対し、水5〜15重早部を温度20〜80℃の攪拌下
において添加して粒径5〜15mmの顆粒状流動床11
j体を#JI造する方法。
2. Claims (1) Completely saponified polyvinyl alcohol 100i Amount M
To this, 5 to 15 parts of water was added under stirring at a temperature of 20 to 80°C to form a granular fluidized bed 11 with a particle size of 5 to 15 mm.
How to construct a j-body #JI.

(2)完全鹸化ポリビニルアルコール +001<4i
部に対し、氷 5〜15重借部を温度20〜80℃の攪
拌ド1こおいて添加して得られる粒径5〜+51の顆粒
人血に加熱攪拌ドで微粉末活性炭を0.5〜3部を添加
して微粉末活性炭被覆顆粒状流動床担体を製造する方法
(2) Completely saponified polyvinyl alcohol +001<4i
0.5 parts of finely powdered activated carbon was added to granulated human blood with a particle size of 5 to +51% obtained by adding 5 to 15 parts of ice in a stirring oven at a temperature of 20 to 80°C. A method for producing a granular fluidized bed carrier coated with finely powdered activated carbon by adding ~3 parts.

(3)完全鹸化ポリ上ニルアルコール100重量部に対
し、水5〜15帆丑部を温度20〜80°Cの攪拌下に
おいて添加して得られる粒径5〜15IIIIllの顆
粒を適用すべき廃水の処理に有用な微生物培養液中に浸
漬した後、冷凍乾燥して微生物付着疏動床担体を製造す
る方法。
(3) Wastewater to which granules with a particle size of 5 to 15 IIIll obtained by adding 5 to 15 parts of water to 100 parts by weight of completely saponified polyvinyl alcohol under stirring at a temperature of 20 to 80°C are applied. A method for producing a microorganism-adhered scrofulous bed carrier by immersing it in a microbial culture solution useful for the treatment of spores, and then freeze-drying it.

(4)完全蝕化ポリビニルアルコール100重湯部に対
し、水5〜15重ji1部を温度20〜80℃の攪拌°
ドにおいて添加して得られる粒子−¥5〜15III+
nの1σ寧復表面に加熱攪拌下で微粉末活性炭を0,5
〜3合トを添加して再られる微粉末活性)で被覆顆粒を
、適用すべき廃水の処理に有用な微生物18−1!*弓
Jに浸漬した後、冷凍乾燥して微生物イリ着1ん動床1
1体を製造する方法。
(4) Stir 5 to 15 parts of water to 100 parts of fully corroded polyvinyl alcohol at a temperature of 20 to 80°C.
Particles obtained by adding in de- ¥5 to 15III+
0.5% of fine powder activated carbon is applied to the surface of the 1σ polygon of n under heating and stirring.
Microorganisms useful in the treatment of wastewater should be applied to the granules coated with finely powdered active microorganisms 18-1 which can be reconstituted by adding ~3 mixtures! *After soaking in the bow J, freeze-dry it to make 1 microorganism deposit 1 perturbation bed
How to make one.

Claims (4)

【特許請求の範囲】[Claims] (1)完全鹸化ポリビニルアルコール 100重吊部に
対し、水5〜15屯融部を温度20〜80°Cの攪拌ド
において添加して粒径5〜IF+amの顆粒状流動床担
体を製造する方法。
(1) A method for producing a granular fluidized bed carrier with a particle size of 5 to IF+am by adding 5 to 15 parts of water to 100 parts of completely saponified polyvinyl alcohol under stirring at a temperature of 20 to 80°C. .
(2)完全鹸化ポリビニルアルコール 100重噺部に
対し、木5・〜I5@に部を温度20〜80°Cの攪拌
下において添加して得られる粒径5〜15mmの顆粒表
面に加熱攪拌下で粒度325メツシユ以下の微粉末活性
炭を0.5〜3部を添加して微粉末活性炭被mWt粒状
流動床神体を製造する方法。
(2) Completely saponified polyvinyl alcohol 100 parts by weight are added to the surface of granules with a particle size of 5 to 15 mm obtained by adding 5 to 15 parts of wood under stirring at a temperature of 20 to 80°C. A method for producing mWt granular fluidized bed body covered with fine powder activated carbon by adding 0.5 to 3 parts of fine powder activated carbon having a particle size of 325 mesh or less.
(3)完全鹸化ポリビニルアルコール 100重敲部に
対し、水5〜15重敬部を温度20〜80°Cの攪拌下
において添加して得られる粒径5〜15m■の顆粒を適
用すべき廃水の処理に有用な微生物培養液中に浸漬した
後、冷凍乾燥して微生物4=J着流動床担体を製造する
方法。
(3) Completely saponified polyvinyl alcohol 100 parts of waste water should be treated with granules with a particle size of 5 to 15 m, obtained by adding 5 to 15 parts of water under stirring at a temperature of 20 to 80°C. A method of manufacturing a microorganism 4=J fluidized bed carrier by immersing it in a microorganism culture solution useful for treatment and then freeze-drying it.
(4)完全鹸化ポリビニルアルコール 100 重N部
に対し、水5〜15@篭部を温度20〜80℃の攪拌下
において添加して得られる粒径5〜15III11の顆
粒表面に加熱攪拌下で粒度325メツシユ以下の微粉末
活性炭を0.5〜3部を添加して得られる微粉末活性炭
被覆顆粒を、適用すべき廃水の処理に有用な微生物培養
液中に浸漬した後、冷凍乾燥して微生物+IM泣動床担
体を製造する方法。
(4) Completely saponified polyvinyl alcohol 100 parts by weight, add 5 to 15 parts of water to the surface of the granules with a particle size of 5 to 15III11 obtained by adding 5 to 15 parts of water under stirring at a temperature of 20 to 80°C. Finely powdered activated carbon-coated granules obtained by adding 0.5 to 3 parts of finely powdered activated carbon of 325 mesh or less are immersed in a microbial culture solution useful for the treatment of wastewater to which it is applied, and then freeze-dried to produce microorganisms. +Method of manufacturing an IM crybed carrier.
JP59037272A 1984-03-01 1984-03-01 Preparation of carrier for fluidized bed biological treatment apparatus Granted JPS60183095A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59037272A JPS60183095A (en) 1984-03-01 1984-03-01 Preparation of carrier for fluidized bed biological treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59037272A JPS60183095A (en) 1984-03-01 1984-03-01 Preparation of carrier for fluidized bed biological treatment apparatus

Publications (2)

Publication Number Publication Date
JPS60183095A true JPS60183095A (en) 1985-09-18
JPH0221317B2 JPH0221317B2 (en) 1990-05-14

Family

ID=12493038

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59037272A Granted JPS60183095A (en) 1984-03-01 1984-03-01 Preparation of carrier for fluidized bed biological treatment apparatus

Country Status (1)

Country Link
JP (1) JPS60183095A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272171A (en) * 2005-03-29 2006-10-12 Denka Consult & Eng Co Ltd Microbial carrier blended with nitrohumate

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55111895A (en) * 1979-02-20 1980-08-28 Achilles Corp Filter material for waste liquid treating apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55111895A (en) * 1979-02-20 1980-08-28 Achilles Corp Filter material for waste liquid treating apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272171A (en) * 2005-03-29 2006-10-12 Denka Consult & Eng Co Ltd Microbial carrier blended with nitrohumate

Also Published As

Publication number Publication date
JPH0221317B2 (en) 1990-05-14

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