JPS6344995A - Inclusion material for sludge treatment and treatment for sewage using it - Google Patents

Inclusion material for sludge treatment and treatment for sewage using it

Info

Publication number
JPS6344995A
JPS6344995A JP61190130A JP19013086A JPS6344995A JP S6344995 A JPS6344995 A JP S6344995A JP 61190130 A JP61190130 A JP 61190130A JP 19013086 A JP19013086 A JP 19013086A JP S6344995 A JPS6344995 A JP S6344995A
Authority
JP
Japan
Prior art keywords
sewage
adsorbent
wastewater
activated sludge
activated carbon
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
JP61190130A
Other languages
Japanese (ja)
Inventor
Masahito Fujita
雅人 藤田
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.)
Takuma Co Ltd
Original Assignee
Takuma 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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP61190130A priority Critical patent/JPS6344995A/en
Publication of JPS6344995A publication Critical patent/JPS6344995A/en
Pending legal-status Critical Current

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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

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  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Abstract

PURPOSE:To effectively perform the purification of sewage by sticking activated sludge contg. nitrite bacteria to an adsorbent consisting of a mixture of activated carbon and solid acid and including it with gel for inclusion. CONSTITUTION:Activated sludge contg. nitrite bacteria is stuck to an adsorbent formed by adding activated carbon to slid acid. Then this is included with gel for inclusion of sodium alginate, carageenan, polyacrylamide, etc. This mixture is brought into contact with COD component under aeration of oxygen- contg. gas. Thereby the treatment of sewage can be effectively performed.

Description

【発明の詳細な説明】 産業上の利用分野: 本発明は、活性炭と固体酸との混合物からなる吸着体に
、活性汚泥を付着させて、包括用ゲルで包括した包括体
、PよびこAを用いた汚水を浄化する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application: The present invention provides an enclosing body, P and A, in which activated sludge is adhered to an adsorbent consisting of a mixture of activated carbon and a solid acid, and the adsorbent is encased in an entrapping gel. This invention relates to a method for purifying wastewater using.

本明細慢で、活性炭とlよ、水蒸気丑たは薬品賦活した
活性炭・骨炭など、炭素を含み、多孔霞で、非イオン吸
着を主体とし之吸着金起こすものtいう。また固体酸と
は、アルミナとシリカとの反応物、カチオン交換樹脂の
ように、固体が酸、すなわち、ブレンステッドの定義で
はH”を放出するもの、ルイスの定義によれば、電子対
を受は取るものでりる。
In this specification, activated carbon refers to a substance containing carbon, such as activated carbon or bone char activated by water vapor or chemicals, which is a porous haze, and which mainly performs nonionic adsorption, but which causes adsorption of gold. A solid acid is an acid in which the solid is an acid, such as a reaction product of alumina and silica, or a cation exchange resin, which releases H'' according to Brønsted's definition, or accepts a pair of electrons according to Lewis's definition. I'll take it.

背景技術: 従来汚水の浄化に、活性汚泥法や生物膜法が用いら几て
さた。これらの方法では、比紋的分解さ几易い有機物し
か浄化できなかった。そのため、生物学的に難分解な物
質が未分解のまま残留し、河川・湖沼・海域の汚染の原
因となった。そのため、二次処理技術として、活性炭を
用いて、(2001着色物など全吸着除去する方法、固
体酸塩であるゼオライトを用いてアンモニア性窒素金除
去する方法、その他の吸着除去法が開発されている。ま
た、固体酸と好気性硝化函とを包括ゲルにより固定した
包括体(特開昭61−68198号公報)などが開示さ
れており、汚水の脱窒については、1らる程度、/)進
歩か見られる。
Background technology: Conventionally, activated sludge methods and biofilm methods have been used to purify sewage. These methods could only purify organic substances that are easily decomposed. As a result, biologically difficult to decompose substances remained undecomposed, causing pollution of rivers, lakes, and sea areas. Therefore, as secondary treatment technologies, a method for completely adsorbing and removing colored substances using activated carbon (2001), a method for removing ammonia nitrogen gold using zeolite, which is a solid acid salt, and other adsorption removal methods have been developed. In addition, an enclosing body in which a solid acid and an aerobic nitrification box are fixed with an enclosing gel (Japanese Patent Application Laid-open No. 61-68198) has been disclosed. ) Progress can be seen.

共面な生育域を待つ微生物が、neutrai i s
m 。
Microorganisms waiting for a coplanar growth area are neutrais.
m.

mutualism、 commensalism、 
amensalisrnなどと称される相伝作用を持つ
ことは、広く知られている。このうち、commens
al i smはある微生物が他の微生物のび任により
得をする場合で、例えば汚水中のアミン・アミドをNH
;に変えるヘテロトo −7(heterotorop
h )は、NH; −f NC); K変えるニトロソ
モナス属の菌により利益全党け、また、ニドl’?ソモ
ナス属の細歯はNO;をNO′Bに変えるニトロバクタ
−属の細菌により利益を受ける。またam6ngBli
smは、ある微生物が他の微生物の存在によシ害を受け
る場合で、前記NO;をNO−に変えるニトロバクタ−
属の菌はアミン・アミドをNH+4に分解するヘテロト
ローフにより#?受ける。
mutualism, commensalism,
It is widely known that it has a synergistic effect called amensalisrn. Of these, commens
al i sm is a case in which a certain microorganism benefits from the spread of other microorganisms, for example, by converting amines and amides in wastewater into NH
; Heterotorop o -7 (heterotorop
h) is NH; -f NC); Somonas microdontia benefit from Nitrobacter bacteria that convert NO; to NO'B. Also am6ngBli
sm is a nitrobacter that converts NO into NO when a certain microorganism is damaged by the presence of another microorganism.
Bacteria of the genus #? due to heterotrophs that decompose amines and amides into NH+4. receive.

なお、活性汚泥r94合、除去BO1)量の20〜80
チが余剰汚泥となるが、一般にBOD貞荷−が小さいほ
ど、また14気時間が長いほど余剰汚泥の発生量が少な
いことが知られている。
In addition, activated sludge r94, removal BO1) amount of 20 to 80
However, it is known that the smaller the BOD load and the longer the 14-hour period, the smaller the amount of surplus sludge generated.

解決しようとする問題点: 二トロソ亡ナス属菌全固体酸に付着生息させ、これを用
いて好気性条件で汚水を処理することに工り、アンモニ
ア性Nの亜硝酸化が促進されることは、すでに前記特開
昭61−68198号公報で明らかにされている。汚水
処理操作の中で、脱窒が重要であることは言うまでもな
いが、活性汚泥による有機分解を促進することが、汚水
の二次処理の場合に、さらに重要である。しかしながら
、カチオン化が不可能な有機物は固体酸にI吸着されず
、生物分解反応は促進されない。
Problem to be solved: Nitrosolanus bacteria can be made to live attached to all solid acids, and this can be used to treat wastewater under aerobic conditions, thereby promoting the nitrite oxidation of ammoniacal N. has already been disclosed in the aforementioned Japanese Patent Application Laid-Open No. 61-68198. It goes without saying that denitrification is important in sewage treatment operations, but promoting organic decomposition by activated sludge is even more important in the case of secondary treatment of sewage. However, organic substances that cannot be cationized are not adsorbed by solid acids and biodegradation reactions are not promoted.

問題点全解決するための手段: 本発明では、上記カチオン化不可能な難分解物質を吸着
剤、すなわち活性炭會副本酸に加えてなる吸着剤に、亜
硝酸化歯を含む活性汚泥を付着させ、包括用ゲルで包括
した包括体を提供する。
Means for solving all problems: In the present invention, activated sludge containing nitrite oxide is attached to an adsorbent containing the above-mentioned hard-to-decompose substance that cannot be cationized, that is, an adsorbent made by adding activated carbon to main acid. , providing an enclosing body encapsulated with an entrapping gel.

包括用ゲルを形成する材料として、アルギン酸ナトリウ
ム、カラギーナン、ポリアクリルアミド)ポリビニルア
ルコールから選んだものを用いることが望ましい。また
包括体は直径0.5〜10 ff程度のビーズにして、
また、別法として、0.1〜10aの厚さのフィルム状
にして使用することが好ましい。
As the material for forming the entrapping gel, it is desirable to use a material selected from sodium alginate, carrageenan, polyacrylamide) and polyvinyl alcohol. In addition, the inclusion body is made of beads with a diameter of about 0.5 to 10 ff.
Alternatively, it is preferable to use it in the form of a film with a thickness of 0.1 to 10 a.

亜硝酸化閑全含む活性汚泥の乾itと、吸着体の乾重敏
の比は0.1=10〜l:1で心ることが望葦しい。
It is desirable that the ratio of the dry weight of the activated sludge containing nitrite oxide and the dry weight of the adsorbent be 0.1=10 to 1:1.

作用: 上記曲硝酸化菌全含む活性汚泥と、活性炭と固体酸との
混合暖からなる吸着剤との混合吻合、改索含有ガス(g
!、気・富化空気など)の曝気下で、いわゆるC01)
成分と接触させる。
Action: Mixing anastomosis of activated sludge containing all of the above-mentioned nitrifying bacteria with an adsorbent consisting of a mixture of activated carbon and solid acid,
! , air, enriched air, etc.), so-called C01)
contact with ingredients.

C01)成分中、NfG性のものは固体酸に、中性のも
のは非イオン的に活性炭に吸着される順向があり、吸着
、ゲルたアミン・アミドなどは微生物反応によりNH;
に変わり、NH;は有機物栄養全必要としないヘテロト
ローフに属するニトロソモナス属の菌により唾硝酸に変
化する。一方活性炭は主として非イオン的VC有機物を
吸着するので、吸着した有機Wは、包括されている活性
汚泥により主力学的に酸化分解される。吸着現象は、界
面における濃度が非界面における濃度より高くなる現象
で、包括体i/cおける彼処理物質のa度上昇により、
生物学的分解が促進されるのであり、分解生成#1JN
O;、C02などは吸着剤から容易に脱着される。NO
;が、酸素不足状態で還元さnてN2になるのは周知の
と分りでめる。
C01) Among the components, NfG components tend to be adsorbed by solid acids, neutral components are non-ionically adsorbed by activated carbon, and amines and amides that are adsorbed or gel are NH by microbial reactions.
NH; is converted into salivary nitrate by bacteria of the genus Nitrosomonas, which belong to heterotrophs that do not require any organic nutrients. On the other hand, since activated carbon mainly adsorbs nonionic VC organic matter, the adsorbed organic W is oxidatively decomposed primarily by the activated sludge entrained therein. The adsorption phenomenon is a phenomenon in which the concentration at the interface becomes higher than the concentration at the non-interface.
Biological decomposition is promoted, and decomposition production #1JN
O;, C02, etc. are easily desorbed from the adsorbent. NO
; is reduced to N2 in an oxygen-deficient state.

実施例: 肉エギ、X、5.79.ペブトy 8.61. Kce
2.4 ’j、NaC(18,09、硫酸アンモニウム
14.(H’、N21(PO42,79に水を加え全量
を104とした合成汚水を、BOD容積負荷1.0にg
/vt −day で活性汚泥処理した。この処理水は
BOD50−100ダ/l。
Example: Nikuegi, X, 5.79. Pebuty 8.61. Kce
2.4 'j, NaC (18,09, ammonium sulfate 14. (H', N21 (PO42,79) and water to make the total volume 104, g
Activated sludge treatment was carried out at /vt-day. This treated water has a BOD of 50-100 da/l.

NH:態N  210〜290 q/e 、 色度(J
ISKolol−10,1: 1976年)80〜11
0度、8880〜66q/y 、 COD、、(n75
〜120M+/ e、pf’16.6〜7Jの性状金持
ち、活性汚泥による処理済水で、二次処理にかける原水
という意味で、二次汚水と定義する。
NH: State N 210-290 q/e, chromaticity (J
ISKolol-10, 1: 1976) 80-11
0 degrees, 8880~66q/y, COD, (n75
~120M+/e, pf'16.6~7J, rich in properties, treated water with activated sludge, defined as secondary sewage in the sense of raw water subjected to secondary treatment.

1.5ffi!:%アルギン酸ナトリウム水溶液と、り
らかしめ、二次汚水に馴致したニトロソモナス属萌1乾
%を含む活性汚泥を遠心分離器で約2%の濃度にa縮し
たものと、粉末活性炭(クラレケミカル社良・商品名P
W型。)と、粉末アルミノ7リケート(秋田基量りリノ
プチライト全乳鉢で粉末化したもの。)とを重量比で、 4 : 1.5 (乾鎗4準0.08) : 1 : 
1の割合で混合し、1.1重量%Card2水浴液中に
満願して球状体を作り、水洗後水切りしてビーズとした
。また、上iα型量比を作り、水洗後水切りしてビーズ
とした。また、上記重量比で各物質全混合した液にメツ
シュのグラスチック製の網(巾41、尚さlQclg、
厚さI All )を浸漬し、網表面にゲル金付着させ
た後、■、1チCaC1、水atiに浸漬し、約3 ’
Cに12時間静置し、包括体の付着したフィルム7作っ
た。これを第1図に示すカラム(液溶m1.6g)に入
れ、1日に1回、2次汚水を排出・再充填しながら、約
25°Cで、80日間、空気曝気(0,8イ/イh)の
もとで実験を行った。ただし、CL)υg績負負荷t)
、08匈/イd&y r目安とした。
1.5ffi! :% sodium alginate aqueous solution, activated sludge containing 1% dried Nitrosomonas spp. that has been mixed with secondary wastewater and condensed to a concentration of about 2% in a centrifuge, and powdered activated carbon (Kuraray Chemical Co., Ltd.) Good/Product name P
W type. ) and powdered alumino 7 silicate (pulverized in an Akita base weighing linopetilite whole mortar) in a weight ratio of 4: 1.5 (dry spear 4 quasi 0.08): 1:
They were mixed at a ratio of 1.1% by weight to form spheres in a 1.1% by weight Card2 water bath solution, washed with water, and then drained to form beads. In addition, the upper iα type ratio was prepared, and the beads were washed with water and drained to obtain beads. In addition, a mesh glass net (width 41, furthermore, lQclg,
Thickness I All ) was immersed to adhere gel gold to the surface of the mesh.
C for 12 hours to form a film 7 to which the inclusion body was attached. This was placed in the column shown in Figure 1 (1.6 g of liquid solution), and air aeration (0,8 Experiments were conducted under I/Ih). However, CL)υg result negative load t)
, 08 匈/Id&yr as a guideline.

第1図に2いて、透明ポリ塩化ビニル製鉛+M、有底中
少円筒(1)のほぼ中心部に−IA直管(1a)が立設
さ才L1 樅気用空気が、ブロワ−(3)により圧縮さ
れ、調節弁(3a)により流量調節され、鉛直管(1a
)を降下して、散気法(1りから円筒(1)内に泡出す
る。円筒内には包括体、固定化ビーズ(IC)と、前記
二次汚水が保持されており、所望の曝気汚水処理が行わ
れる。また、透明ビニル襄鉛直有底の中空四角筒(2)
には、通常複数の、前記包括体を付着したフィルム(2
C)が、適宜間隔金とり懸垂しており、鉛直円筒(1)
の場合と同様に、プロワ−(3)により圧縮された空気
が、調節弁(3b)を経て、鉛直管(21L)ft。
In Fig. 1, a -IA straight pipe (1a) is installed approximately in the center of a transparent polyvinyl chloride lead +M bottomed medium-sized cylinder (1). 3), the flow rate is adjusted by the control valve (3a), and the vertical pipe (1a
) and bubbles are bubbled out from the aeration method (1) into the cylinder (1). The cylinder holds the enclosing body, immobilized beads (IC), and the secondary wastewater, and the desired Aerated sewage treatment is carried out.In addition, a hollow rectangular cylinder made of transparent vinyl with a vertical bottom (2)
Usually, a plurality of films (2
C) is suspended with appropriate spacing, and the vertical cylinder (1)
As in the case of , the air compressed by the blower (3) passes through the control valve (3b) and enters the vertical pipe (21L) ft.

下降し、散気法(2b)を介し角筒(2)内の汚水中に
噴出する。
It descends and is ejected into the waste water inside the rectangular tube (2) via the aeration method (2b).

試験結果を纒めて第1表に示す。The test results are summarized in Table 1.

実施例1は、平均直径3.Offの製型f20Ggのビ
ーズ’t、1.61の前記二次汚水中に懸濁した場合の
試験結果である。実施例2は前記手段により作成したフ
ィルム(製型−1118Oft 、ただしプラスチック
支持体重量を除く。)全プラスチック支持体に固定した
まま1.61の前記二次汚水中に浸漬した場合の試・倹
結果である。実施例3は、比較のため、前記亜硝酸化醒
のみをアルギン酸ナトリウムで、実施例1および2と同
様にゲル化包括体とした試験結果である。
Example 1 has an average diameter of 3. These are the test results when beads of Off mold f20Gg were suspended in the secondary wastewater of 1.61. Example 2 shows the test results when a film (mold-1118Oft, excluding the weight of the plastic support) prepared by the above method was immersed in the secondary wastewater of 1.61 while fixed to a plastic support. This is the result. For comparison, Example 3 is the result of a test in which sodium alginate was used as the nitrite oxidation agent, and the gelled inclusion was used in the same manner as in Examples 1 and 2.

Bol)(q/6)、conMn(q/#)、色度、N
用B tH(wg/e )のいずれにおいても、処理効
率は、実施例1が最も優れ、次いで実施例2、実施例8
の1頃である。
Bol) (q/6), conMn(q/#), chromaticity, N
In terms of B tH (wg/e ), Example 1 has the best treatment efficiency, followed by Example 2 and Example 8.
It was around the 1st of the year.

発明の効果: 本発明は、活性汚泥と、活性炭と固体酸とからなる吸着
剤と全混合して同一ゲル内に包括固定化した包括体およ
び、これを用いて汚水、特に−変法性汚泥処理を終えた
、BODが比較的少なくNH”、f4素含itの多い二
次汚水を処理する汚水処理法からなるものである。
Effects of the invention: The present invention provides an enclosing body in which activated sludge and an adsorbent consisting of activated carbon and solid acid are completely mixed and encased and immobilized in the same gel, and the use of this to improve sewage, especially modified sludge. This method consists of a wastewater treatment method that treats secondary wastewater that has undergone treatment and has a relatively low BOD content and a high content of NH'' and f4 elements.

本発明の包括体は微生物(二次汚水処理の場合、特に、
ニトロソモナス属などの亜硝酸生成菌)を高一度に含ん
でおり、固体酸部分がアンモニアを吸着し、活性炭部分
が、非イオン有機成分を吸着し、酸化、消化が終われば
、脱着してビーズ外に排出されて吸着面の再生が行われ
る。このことにより、イオン型と非イオン型の2種の生
物分解かり能である。
The inclusion body of the present invention is a microorganism (in the case of secondary sewage treatment, in particular,
The solid acid part adsorbs ammonia, the activated carbon part adsorbs non-ionic organic components, and once oxidation and digestion are complete, they are desorbed and released into beads. It is discharged outside and the suction surface is regenerated. This results in two types of biodegradability: ionic and non-ionic.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の汚水処理用包括体の試験装置の概略
構造金示す流れ図である。 (1)・・・ポリ塩化ビニル筒 (2)・・・中空四角
筒(IC)・・・固定化ビーズ  (2e)・・・フィ
ルム(3)・・・ブロワ− 出 願 人   株式会社タ り マ 第1図 手続補正書自発 汚水処理法 補正をする者 事件との関係    特許用11人 住所(J+”! :升)大阪市北区堂鮨派1丁目3番2
3号氏名(名称)  株式会社 タ り マ代  理 
 人 日付 昭和  年  月  日 補正の対象 明細書のヴ6用の名称の欄、(1)  発
明の名称 「汚泥処理用包括体お工びこれを用いた汚水
処理法」とある金、「汚水処理用包括体およびこれを用
いた汚水処理法」と補正する。 (2)  特許請求の範囲を下記の通り補正する。 l 活性炭と1体酸との混合物からなる吸着体に亜硝酸
化菌を含む活性汚泥を付着させ、包括用ゲルにより包括
し九汚水処理用包括体。 2 包括用ゲルが、アルギン酸ナトリクム、カラギーナ
ン、ポリアクリルアミド、ポリビニルアルコールから選
んだものからなる時計請求の範囲第1項記載の包括体。 3 包括体が、直径0.5〜10mのビーズである特許
請求の範囲第1項ま免は第2項に記載の包括体。 4 包括体か、支持体の表面に厚み0.1〜10厘のフ
ィルム状に固定されている時計請求の範囲第3項に記載
の包括体。 5 被包括体が、乾活性汚泥と乾吸着体の重量比が0.
1 : 10ないし1:lである特I7!F請求の範囲
第1項から第4項のいずれか1に記載の包括体。 6 活性炭と固体酸との混合物からなる吸着体に亜硝酸
化菌を含む活性汚泥を付着させ、包括用ゲルにエリ包括
し之包括体を、被処理汚水中に懸濁させ、酸素含有ガス
を該汚水中に吹込んで、流動状むで生物分解を記こさせ
る汚水処理方法。 7 活性炭と固体酸との混合物からなる吸着体に亜硝酸
化菌を含む活性汚泥を付着させ、包括用ゲルにエリ包括
し九包括体を、支持体に固定し、液処理汚水中VC浸漬
し、酸素含有ガスを該汚水中に吹込んで生物分解を起こ
させる汚水処理力法。
FIG. 1 is a flowchart showing the general structure of a test device for a wastewater treatment package according to the present invention. (1)...Polyvinyl chloride tube (2)...Hollow square tube (IC)...Immobilized beads (2e)...Film (3)...Blower Applicant: Tari Co., Ltd. Figure 1 Procedural Amendment Document Relationship with the Case of Person Who Amends the Sewage Treatment Act Voluntary Sewage Treatment Act Address of 11 persons for patent purposes (J+”!: square) 1-3-2 Dozushiha, Kita-ku, Osaka City
No. 3 Name (Name) Tarima Co., Ltd. Agent
Person date Showa year Month Date subject to amendment Name column for V6 of the specification (1) Title of the invention The name "Sludge treatment comprehensive body and sewage treatment method using the same" and "Sewage treatment amended to ``Inclusive bodies for use and sewage treatment methods using the same''. (2) The scope of claims shall be amended as follows. 1. Activated sludge containing nitrite-oxidizing bacteria is attached to an adsorbent made of a mixture of activated carbon and monoacid, and the mixture is wrapped in a gel for sewage treatment.9. 2. The wrapping body according to claim 1, wherein the wrapping gel is made of a material selected from sodium alginate, carrageenan, polyacrylamide, and polyvinyl alcohol. 3. The enclosing body according to claim 1 or 2, wherein the enclosing body is a bead having a diameter of 0.5 to 10 m. 4. The wrapping body according to claim 3, wherein the wrapping body is fixed to the surface of the supporting body in the form of a film having a thickness of 0.1 to 10 mm. 5 The inclusion body has a weight ratio of dry activated sludge to dry adsorbent of 0.
Special I7 that is 1:10 to 1:l! F. The package according to any one of claims 1 to 4. 6. Activated sludge containing nitrite-oxidizing bacteria is attached to an adsorbent made of a mixture of activated carbon and solid acid, and the enclosing body is suspended in the wastewater to be treated, and the enclosing body is suspended in the wastewater to be treated. A sewage treatment method that involves injecting fluid into the sewage to record biological decomposition. 7. Activated sludge containing nitrite-oxidizing bacteria is attached to an adsorbent made of a mixture of activated carbon and solid acid, and the 9-encompassed body is encapsulated in an entrapping gel, fixed on a support, and immersed in VC in liquid-treated wastewater. , a wastewater treatment method in which oxygen-containing gas is blown into the wastewater to cause biodegradation.

Claims (1)

【特許請求の範囲】 1 活性炭と固体酸との混合物からなる吸着体に亜硝酸
化菌を含む活性汚泥を付着させ、包括用ゲルにより包括
した汚泥処理用包括体。 2 包括用ゲルが、アルギン酸ナトリウム、カラギーナ
ン、ポリアクリルアミド、ポリビニルアルコールから選
んだものからなる特許請求の範囲第1項記載の包括体。 3 包括体が、直径0.5〜10mmのビーズである特
許請求の範囲第1項または第2項に記載の包括体。 4 包括体が、支持体の表面に厚み0.1〜10mmの
フィルム状に固定されている特許請求の範囲第3項に記
載の包括体。 5 被包括体が、乾活性汚泥と乾吸着体の重量比が0.
1:10ないし1:1である特許請求の範囲第1項から
第4項のいずれか1に記載の包括体。 6 活性炭と固体酸との混合物からなる吸着体に亜硝酸
化菌含む活性汚泥を付着させ、包括用ゲルにより包括し
た包括体を、被処理汚水中に懸濁させ、酸素含有ガスを
該汚水中に吹込んで、流動状態で生物分解を起こさせる
汚水処理方法。 7 活性炭と固体酸との混合物からなる吸着体に亜硝酸
化菌を含む活性汚泥を付着させ、包括用ゲルにより包括
した包括体を、支持体に固定し、被処理汚水中に浸漬し
、酸素含有ガスを該汚水中に吹込んで生物分解を起こさ
せる汚水処理方法。
[Scope of Claims] 1. An enclosing body for sludge treatment, in which activated sludge containing nitrite-oxidizing bacteria is adhered to an adsorbent made of a mixture of activated carbon and a solid acid, and the adsorbent is encased in an entrapping gel. 2. The entrapping body according to claim 1, wherein the entrapping gel is made of a material selected from sodium alginate, carrageenan, polyacrylamide, and polyvinyl alcohol. 3. The enclosing body according to claim 1 or 2, wherein the enclosing body is a bead having a diameter of 0.5 to 10 mm. 4. The wrapping body according to claim 3, wherein the wrapping body is fixed to the surface of the support body in the form of a film having a thickness of 0.1 to 10 mm. 5 The inclusion body has a weight ratio of dry activated sludge to dry adsorbent of 0.
An inclusion according to any one of claims 1 to 4, wherein the ratio is 1:10 to 1:1. 6. Activated sludge containing nitrite-oxidizing bacteria is attached to an adsorbent made of a mixture of activated carbon and solid acid, and the enclosing body enclosed by an entrapping gel is suspended in wastewater to be treated, and oxygen-containing gas is introduced into the wastewater. A wastewater treatment method that causes biodegradation in a fluid state by injecting water into the water. 7 Activated sludge containing nitrite-oxidizing bacteria is attached to an adsorbent made of a mixture of activated carbon and solid acid, and the enclosing body is encapsulated with an entrapping gel, fixed to a support, immersed in wastewater to be treated, and oxygenated. A sewage treatment method in which a gas contained in the sewage is blown into the sewage to cause biodegradation.
JP61190130A 1986-08-13 1986-08-13 Inclusion material for sludge treatment and treatment for sewage using it Pending JPS6344995A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61190130A JPS6344995A (en) 1986-08-13 1986-08-13 Inclusion material for sludge treatment and treatment for sewage using it

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61190130A JPS6344995A (en) 1986-08-13 1986-08-13 Inclusion material for sludge treatment and treatment for sewage using it

Publications (1)

Publication Number Publication Date
JPS6344995A true JPS6344995A (en) 1988-02-25

Family

ID=16252891

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61190130A Pending JPS6344995A (en) 1986-08-13 1986-08-13 Inclusion material for sludge treatment and treatment for sewage using it

Country Status (1)

Country Link
JP (1) JPS6344995A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408133A (en) * 2013-08-18 2013-11-27 北京工业大学 Anaerobic ammoxidation sludge embedding immobilization method
CN109019876A (en) * 2018-09-21 2018-12-18 曲阜师范大学 A kind of fixation psychrophile for sewage treatment carbonizes sludge carrier filler and its application

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408133A (en) * 2013-08-18 2013-11-27 北京工业大学 Anaerobic ammoxidation sludge embedding immobilization method
CN109019876A (en) * 2018-09-21 2018-12-18 曲阜师范大学 A kind of fixation psychrophile for sewage treatment carbonizes sludge carrier filler and its application

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