JPS5946192A - Suppression of filiform bacteria growth in activated sludge - Google Patents

Suppression of filiform bacteria growth in activated sludge

Info

Publication number
JPS5946192A
JPS5946192A JP57154579A JP15457982A JPS5946192A JP S5946192 A JPS5946192 A JP S5946192A JP 57154579 A JP57154579 A JP 57154579A JP 15457982 A JP15457982 A JP 15457982A JP S5946192 A JPS5946192 A JP S5946192A
Authority
JP
Japan
Prior art keywords
aeration tank
tank
chlorine
activated sludge
aeration
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
JP57154579A
Other languages
Japanese (ja)
Inventor
Masami Miyagawa
宮川 将美
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.)
SANKYO NYUGYO KK
Original Assignee
SANKYO NYUGYO 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 SANKYO NYUGYO KK filed Critical SANKYO NYUGYO KK
Priority to JP57154579A priority Critical patent/JPS5946192A/en
Publication of JPS5946192A publication Critical patent/JPS5946192A/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

Landscapes

  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To selectively suppress the development of filiform bacteria in activated sludge, by charging the amount of chlorine corresponding to 5-60ppm of the amount of inflow filthy water at an arbitrary position of the aeration tank of a microbic oxidizing apparatus having said aeration tank. CONSTITUTION:By the apparatus comprising a tank 16 for sodium hypochlorite, a tank 17 for hydrochloric acid and a measuring tank 18 for supplying the fixed amount of each of them, a mixed liquid (a 12% sodium hypochlorite solution and an 18% hydrochloric acid solution are usually used) is charged through a passageway 19 in the vicinity 5 of the filthy water inflow part of an aeration tank 4. After solid matter is removed in a primary precipitation pool 2, inflow filthy water is charged by fixed quantities in the aeration tank 4. The aeration tank 4 is filled with MLSS in the concentration of 1,000-10,000ppm. Treated water is separated from sludge in a precipitation pool 8. The former is drained outside the apparatus, while the latter is partially returned as returned sludge through a passageway 12 to the aeration tank 4.

Description

【発明の詳細な説明】 この発明は活性lf5泥中の糸状微イ1物のイIY丁を
抑制することによって、パルキンクを防+Iシ、i−ブ
Cはバルキングを改善治癒するための方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to a method for preventing and curing bulking by suppressing filamentous microorganisms in activated lf5 mud. It is something.

有機物fJ[水を微牛物酸化処]111する方法として
kl、〆rG t’k ’/Ij泥法、曝気式ラクーン
法、またはこJしらの折衷方式が汎用されている。これ
らのカメ人はH(111の除去がきわめて容易にj−J
なえる反面、ともずね。
As a method for oxidizing organic matter (water), the mud method, the aerated raccoon method, or a hybrid method thereof are commonly used. These turtle people are very easy to remove H (111)
On the other hand, Tomozune.

は汚泥の体積が増加(膨化)し、いわゆるバルキング(
■うulking )を惹き起こすため、/り泥と処J
111水の分#:lが十分に行なえず、または不11丁
能になることがある。このバルキングは活性汚泥中に糸
状微生物が多量に繁殖することによって惹き起こされ、
あらゆる種類の有機物を含む排水の前記方法による処理
に121りってしばしば発生するものであるが、特に豆
腐、みそ、しよう浦等の大豆を加工する一1場及び牛乳
をカロニする」1場のjul水処理施没においては、は
とんどすべてがバルキングを惹き起こし、これを改善す
る有効な方法が全くないまま放置されているのが実情で
ある。このようなバルキング状態のまま前記処理方法を
実施するには、1曝気槽の容積を拡大するしか方法がな
く、シかも、曝気槽を拡大したからといって、バルキン
グが改善されるという保証もなく、全くその対策に苦慮
していたのである。
The volume of sludge increases (swells), resulting in so-called bulking (
■In order to cause ulking)
111 Water content #:l may not be carried out sufficiently or may become ineffective. This bulking is caused by the proliferation of filamentous microorganisms in activated sludge.
This often occurs when wastewater containing all kinds of organic matter is treated using the above method, but especially in the processing of soybeans such as tofu, miso, and soybeans, and in the processing of milk. The reality is that almost all water treatment methods cause bulking, and there is no effective way to improve this problem. In order to carry out the above treatment method in such a bulking state, the only way is to expand the volume of the aeration tank, and even if the aeration tank is expanded, there is no guarantee that the bulking will be improved. Instead, they were having a hard time figuring out how to deal with it.

本発明者は、バルキングの原因となるスフエロチルヌ(
5phacro(ilus )、ベギアトア(Bcgg
iatoa )等の糸状微生物の生育を選択的に抑制す
る方法について研究した結果、一定量の塩素を曝気槽に
継続的に投入すると前記糸状微生物が激減し、バルキン
グが改善治チ愈されることを見出し本発明を完1戊した
The present inventor discovered that Sphelotilnus (a cause of bulking)
5phacro (illus), begia toa (Bcgg)
As a result of research into methods for selectively suppressing the growth of filamentous microorganisms such as A. Heading This invention has been completed.

すなわち、この発明は、曝気槽を有する微生物酸(比処
理装置において、流入7r5水h(に勾し5〜60pp
TI]に相当する塩素用を1曝気槽内の1F意1工′1
所に投入することにより、活性汚泥中の糸状(i23生
物の生育を選択的に抑制し、Yj■1↑11/lj泥の
バルキングを予1力、改傳治癒することを目的として開
発したものである。
That is, the present invention uses a microbial acid (specific treatment device) having an aeration tank, in which 5 to 60 pp of water is added to an inflow of 7 r5 h
TI) for chlorine equivalent to 1F in an aeration tank.
This product was developed with the aim of selectively suppressing the growth of filamentous (i23) organisms in activated sludge, preventing bulking of Yj ■ 1↑ 11/lj mud, and modifying and curing the bulking of Yj ■ 1↑ 11/lj mud. It is.

この発明でいう曝気槽とは、tl;1性汚泥方式、11
基気式ラグーン方式またはその他の方式を問わず71)
水と汚泥(Sluclgc )を混合してIll気(A
cralion )してYnlR物を分解する容2Kを
いい、iノfつて、この発明の方法が用いられる装置は
Ill泥と処理水とを分離するだめの沈、IB5 c也
、返送tlj泥回路舌のイ・1・:1:設4ifiの有
無、または表面[I¥気力式、深層1曝気力式等の曝気
方式の差にこだわるものではない。
The aeration tank referred to in this invention is tl;1 type sludge system, 11
71) Regardless of the base air lagoon method or other methods.
Mixing water and sludge (Sluclgc)
clarion) to decompose YnlR materials, and the apparatus in which the method of this invention is used is a sink for separating mud and treated water, IB5 cya, return tlj mud circuit tongue. It does not matter whether or not there is an IFI, or the difference in aeration methods such as the surface [I\\air force type and the deep layer 1 aeration force type.

この発明に係る活↑11t71j泥中の微生物抑制力υ
、は、大豆加工及び乳業IJ1゛水に特に動電を自する
が、そ)(IJL )食品、製紙、アルコール3:’+
’: 舌のイー11だ物を1゜体とする排水に使用して
も十分に効果をイjするものである。
Activity related to this invention ↑11t71j Microbial suppression power in mud υ
(IJL) Food, paper manufacturing, alcohol 3: '+
': It is sufficiently effective even when used to drain water from the tongue.

この発明において113J気槽内に投入する塩素h1は
流入’/’′J水lに利し5〜60 p+111の範囲
であり、必要塩素)i;ば、バルキングの程度(状態)
、流入lf5水の1+01)(生化学的酸素要求量、I
+1ncl+c聞C;II(〕XggC11)cIna
nd ) Qi、曝気槽のMLSS (5uspcnc
lcd 5oliclsIn Tl+c Mixccl
 Liquor ) 用等に従って次のように決定され
る。
In this invention, the chlorine h1 introduced into the 113 J air tank is in the range of 5 to 60 p+111 for the inflow '/'' J water l, and the required chlorine) i;
, 1+01 of inflow lf5 water) (biochemical oxygen demand, I
+1ncl+c C; II (]XggC11) cIna
nd) Qi, MLSS of aeration tank (5uspcnc
lcd 5oliclsIn Tl+c Mixccl
Liquor) is determined as follows according to the usage etc.

(])  rJ(月)が5001)T)Ill、曝気4
hi cr) MLS Sが35001) pan (
Ja−トこの条件を標σt1a度という。)のとき必要
な塩素用は5〜20 ppmの範囲である。
(]) rJ (month) is 5001) T) Ill, aeration 4
hi cr) MLS S is 35001) pan (
This condition is called the standard σt1a degree. ), the required amount of chlorine is in the range of 5 to 20 ppm.

すなわちバルキングの程度に応じて前記の範11J″1
で投入塩素1mを増11する。単にバルキングを予防す
るためなら5〜l Q ppmで十分であるが、バルキ
ングを改善冶疼するに&−j: 、更に増量する必要が
ある3 (2)  1301)及びN+L S Sが標専i濃度
をはずシまた場合にはほぼ次式によって必要塩素量の範
囲の」1限を決定する。
That is, depending on the degree of bulking, the above range 11J''1
Increase the input chlorine by 1m by 11. If it is simply to prevent bulking, 5 to 1 ppm is sufficient, but to improve bulking, it is necessary to further increase the amount. If the concentration is excluded, the limit of the required amount of chlorine is determined approximately according to the following equation.

C:投入塩素11;の上限値[、pp+n 〕、 C−
、fi OX:流入/fl水(7) I((、)l) 
[’ p pan 〕、   X−,:う000Y  
:  MLSS  〔pp+n 〕 、       
           ’l′ −1・ 1 0,00
0この場合にも(1)と同様に、’/fjNILのバル
キング状態によ!75−Cく60の範1月1でjl、マ
、1’i’+投人塩素)、:を決定する。
C: Upper limit of input chlorine 11 [, pp+n], C-
, fi OX: inflow/fl water (7) I((,)l)
['p pan], X-,: U000Y
: MLSS [pp+n],
'l' -1・1 0,00
0 In this case, as in (1), depending on the bulking state of '/fjNIL! 75 - Determine jl, ma, 1'i' + thrown chlorine), : in the range of January 1 of 60-C.

この発明に用いる塩素は、((体の塩素ガスはかりでは
なく次曲、塩素酸ナトリューム、サラン扮、高度サラン
扮等り効塩素を含イ1する物(2jならイ■IJでも用
いることができる。このjル)合、塩素ガスの代わりに
次1]11塩素酸ナトリュームと塩酸の混合溶液を用い
た吉きが、効果、使い易さ及びコスト等のあらゆる点で
良い結果をもたらす曇とがわかった。
The chlorine used in this invention is not a body chlorine gas scale, but a substance containing effective chlorine, such as sodium chlorate, sarang, advanced saran, etc. In this case, using a mixed solution of sodium chlorate and hydrochloric acid instead of chlorine gas has the advantage of providing good results in terms of effectiveness, ease of use, and cost. Understood.

しかも次曲塩素酸と塩酸の混合比率が、鈍物TIとして
1内至3対1のとき最良であ−)だ。塩素カスに代えて
次用J塩素酸と塩酸の混合溶液をIllいることが最良
の結果をもたらす理由は、必ずしも明確ではないが、塩
素ガスだけを投入すると、曝(((・8内で塩素ガスが
直ちに消費まプこは空中に飛散してしまい、また次i1
1+塩素酸ナトリューノ、(サラン扮、商1リザラシ粉
ても同し)だけでは、イ)効J(,1素として働<1!
、18度が、1゛1−過きるがらであると思われる。、
従って、前記次j111塩素酸と塩酸の比イ・;が次曲
塩素酸力」I3勅す場合(N ;10(’:e i 2
11(、”、1! →(”、 4: 1−N a Cl
i 11120において次I++:塩素酸と塩素が几(
rする場合)に最良の糸11.宋をも/とらずことにな
るのである。
Moreover, it is best when the mixing ratio of chloric acid and hydrochloric acid is 1 to 3 to 1 as a blunt TI. The reason why replacing chlorine scum with a mixed solution of chloric acid and hydrochloric acid gives the best results is not necessarily clear, but if only chlorine gas is introduced, The gas will be consumed immediately, and the gas will be scattered in the air, and the next i1
1 + Chloric Acid Natriuno, (same as sarang, quotient 1 rizarashi powder) alone, a) Effect J (, 1 element < 1!
, 18 degrees is considered to be 1゛1-too much. ,
Therefore, if the ratio of chloric acid and hydrochloric acid is given by
11(, ”, 1! →(”, 4: 1-N a Cl
i 11120, the following I++: chloric acid and chlorine are
11. The best yarn for r. This meant that the Song dynasty was also not included.

次に木411明を実施する微生物酸化処理装置1!膚の
肥(賂を図面に)1(づいて説明する。
Next, microbial oxidation treatment equipment 1 that implements wood 411 light! Skin fat (drawing a bribe) 1 (I will explain it next.

第1図は話↑/1/り九方式の)「J−の−例を小ずi
!’I。
Figure 1 shows an example of the story ↑/1/ri9 method)
! 'I.

略図(中面図)であり図において1は1IlL人ll)
水の流路で2は最初の沈澱池である。このI(シ初の沈
IN)l山2で固形物を収り除き、流路3により1Jl
L人〆Ij水を一定i、l、−4一つ曝気槽4に投入す
る。この113.4気J:Hlji 4は全体が4室に
I×画されてお・り流入〆rj水投入11伺近5から矢
印のように/lj水がfli!+環11)環気1ノ圭た
後、lrシ終沈澱を小流1人117がらオーバーフo 
−して最終沈澱池8に流れ込む構造になっている。1曝
気槽4内に(dMl、8sがJ、OOO−] (1,(
10U l1pln 117)’l’J−a テ11、
′11.Jブこさノ1ている。そして沈澱池8で処理水
と汚泥Q;1、分)う111さノL +)ii M−は
装置外へh(流さ)するが、一方後習は流路12を通り
一部は出1曝気i;“’7ioへ貯留さり、;豹′白1
j己消化した後流路11により115.q気J:+il
、・4・\」林送1rjl己としてJJろ送される。ま
た、i、−;j路12のl’r泥の一部は余剰メI、泥
としてlり泥濃析1:Hb7 l 3 ’\貯留され貌
、水装置14により脱水さitクーギ状にして装置外へ
除去さiする。
This is a schematic diagram (inside view), and in the diagram, 1 is 1Ill person)
In the water flow path, 2 is the first settling basin. This I (the first sedimentation IN) is collected in l mountain 2, and 1 J l is removed by flow path 3.
A certain amount of water (i, l, -4) is poured into the aeration tank 4. This 113.4 Qi J: Hlji 4 is divided into 4 rooms as a whole, and the inflow 〆rj water input 11 from the nearby 5 as shown by the arrow /lj water is fli! + ring 11) After the ring air is removed, the lr final sediment is overflowed with a small stream of 117.
- and then flows into the final sedimentation tank 8. 1 In the aeration tank 4 (dMl, 8s is J, OOO-] (1, (
10U l1pln 117)'l'J-a Te11,
'11. J Bukosano 1 is here. Then, in the sedimentation tank 8, the treated water and sludge Q; Aeration i; “'7io is stored;; leopard white 1
j After self-digestion, 115. Qi J: +il
,・4・\” Hayashi is sent to JJ as 1rjl himself. In addition, some of the l'r mud in route i, -; and remove it from the device.

ま″た、第2図は曝気式ラグーンカ式のソロ−の一例を
示す+1!!を略図(中面図)である。、−のj↓、1
合に&;i: /+ii、路3によりjA7.人llj
水か1曝気)、、Hjlj4に投入さノし、一定111
Jl!、l 112に気された後、11′)、j気をや
め−51ご時間静置して7t#己と処理水を、分ν)1
1シた後1.1澄をゲート15を開成して装置外へ流し
出すものである。
In addition, Figure 2 is a schematic diagram (inside view) of +1!! showing an example of an aerated lagoonka type solo., - j↓, 1
If &;i: /+ii, by path 3 jA7. personllj
Water or 1 aeration),, put into Hjlj4, constant 111
Jl! , l After applying 112, 11'), j Stop taking care - 51 hours and let it stand for 7t # and treated water, min ν) 1
After 1.1 liters of water have passed, the gate 15 is opened and the 1.1 clear water is poured out of the apparatus.

次に本発明の実施に使用する次II+!塩素l11をノ
トリ−:r、 −lyと塩4、のl昆合溶l(々製造装
置20について説明すると第1図及び第2図に」っ・い
て16は次曲塩素酸ナトリュームのタンク、17は塩酸
のタンクであり、18は各々を一定:1:供給するため
の定F1(ijソンブである。そしてこの装置により1
)1■記ild合溶l皮(」用゛帛の1.4.y合は/
欠曲塩ゴ?、酸ブ[・リ−1−)、12%溶液と塩酸1
8%溶液が用いらり、る、2 )は流路19kt−、J
:す11)l気イ’j”j 4 ’/) 7”) 水流
入l 11・l’ h 5 K 投入す)l Z+、1
.うにな・)Cいる。
Next, the next II+! used to implement the present invention! 16 is a tank for sodium chlorate, 17 is a tank of hydrochloric acid, and 18 is a constant F1 (ij sombe) for supplying each constant: 1:
)1.
Missing song salt go? , acid b[·li-1-), 12% solution and hydrochloric acid 1
8% solution is used, 2) is the flow path 19kt-, J
:S11) l air i'j"j 4 '/) 7") Water inflow l 11・l' h 5 K input) l Z+, 1
.. Una・)C is here.

このt明に:1、・いて塩素を投入するt:1:+ +
すt ii: II)、・) /、C)、211H4内
のfly、(:・の箇Jす1てよいが、曲′畠&:lt
+i7、人lI、水投入j]イ・i、IJ5れ二投入す
る。流入ff、水投入11イ・I’ 、Ji S &:
I:れ1)k11′白が最も人i、jに増111’lす
る’L’r 1.Q:/、:cので、J’fll’l−
、’!’;を投入i、てこのf、I・+iで糸状微ll
物の!η′1り11゛1を抑制Jるのである。。
At this t: 1, add chlorine t: 1: + +
St ii: II), ・) /, C), fly in 211H4, (:・) is fine, but the song 'Hata &:lt
+i7, person lI, add water j] i, i, IJ5, pour in water. Inflow ff, water input 11 I・I', Ji S &:
I:re1)k11'White increases to the most people i and j111'l'L'r 1. Q:/, :c, so J'fll'l-
,'! '; Insert i, lever f, I +i to make thread-like
Of things! This suppresses η'1 by 11'1. .

しカI、 土1r:、最1% E’Q +l+lQ を
山−a−rI’ t ルカー戊< ?1層At+;泥力
式、l’l’l’I’l ’/’r泥ン’f −y I
f )−’、カ21いS’)ノ11.’、 、/〒k(
二&、l、塩素の投入用jす1庖最終沈I1.Q油流入
11イ、t 、li 6と−する力が良い場合もある。
ShikaI, soil 1r:, the highest 1% E'Q +l+lQ is mountain-a-rI't Luker 戊<? 1 layer At+; mud force type, l'l'l'I'l '/'r mud'f -y I
f)-', F21S')No11. ', , /〒k(
2 &, l, 1 tbsp for adding chlorine, final sedimentation I1. Q oil inflow 11 a, t, li 6 - forces may be good in some cases.

ここ・\塩素を投入すると、II)4気槽4内の内容!
白ケ1、あまり1曝気さiすることなく塩素と其1r(
T沈呂lll+ 8−\冶9人するの−C1塩素の飛1
1tがほとんどなくA洋−)て〆すρ己と塩、+、;の
1&角東が1うγに1jわれるので、バルキングがひど
い場合(糸状微/l14)がきわめて多11(に繁りi
+’i lているJJ、1合)に効里があることがある
。同(1・な111jll+で、塩素を返送l’; 記
にll′l接没人するIJ、j合もある。この場合に←
t ny′<(セ1111に塩素を没入するのでにj−
なく、沈澱池8またIr、1. /U: # i也8 
カ’:) IB、4 気槽4 ・\、4 結す)L テ
いル+!A 、j)” 2’Jt1己山11)C気押1
.110土/cI(1、」材送〆す11+冒%lii 
、1.’、パ・1ゾ11中へ投入するので、llj泥と
塩、)2の接)Illl!がり」にl S)に’i J
i:cえるという効里がある。1実h[1j例1 活t
/Ilすl)1力式の処理に;1□°1による例(1)
  装置の11!を略 ll1l、ti気槽容:1i’、 8 (1(l nj
’が20 (I’m・、1’ −、ill’目槽A・ら
第・1槽にl<、 +l1Ii仲結さ]1でいる、1侠
澱槽の容:11・冒1 fl m“11 +1i、、気
ツノ式(11、水1国り、<気)1式、。
Here \ When chlorine is added, II) 4 contents in tank 4!
1 white powder, 1r of chlorine and 1r without much aeration (
T Shero lll + 8-\Y9 people do - C1 Chlorine fly 1
Since there is almost no 1t and the 1 & corner east of ρ and salt, +, ; are divided into 1 and γ, there are very many cases where bulking is severe (thready / l14).
+'i l JJ, 1 go) may be effective. Same (1・111jll+, return chlorine l'; There is also a case of IJ, j where ll'l is attached to the person. In this case, ←
t ny′<(Since chlorine is immersed in cell 1111,
Without settling tank 8 or Ir, 1. /U: # iya8
Ka':) IB, 4 Air tank 4 ・\, 4 Connect) L Tail+! A, j)"2' Jt1 Kiyama 11) C Kishi 1
.. 110 soil/cI (1,'' material transport 11 + %lii
, 1. ', because I'm going to put it in Pa 1 Zo 11, llj mud and salt,) 2's connection) Illll! Gari'ni l S)ni'i J
i: It has the effect of being helpful. 1 actual h [1j example 1 active t
/Ilsul) For processing of 1 force type; Example (1) using 1□°1
Equipment 11! Abbreviation ll1l, ti air tank volume: 1i', 8 (1(l nj
' is 20 (I'm, 1' -, ill' is in the first tank A, etc. l<, +l1Ii is connected] 1, the content of the 1st tank: 11, 1 fl m “11 +1i,, Kitsuno style (11, Water 1 country, <Ki) 1 style,.

(2)    7I!c  人〆リノ1(乳’i’−1
11水と1、)11・眉11水ノ市、r′7−C約1 
Ll fl Ll +、、、”+l+y 、 Iff)
I) );l、ip’J !’i 0 (+  ++1
on  。
(2) 7I! c Hitoshijireno 1 (milk 'i'-1
11 Mizu and 1,) 11. Mayu 11 Mizunoichi, r'7-C approx. 1
Ll fl Ll +,,,”+l+y, If)
I));l,ip'J! 'i 0 (+ ++1
On.

(:Ll  lr; liの1に/児 MLssの、借厄が2 D tl tl■)111、検
<;7’:、、すると糸状菌(1,!:Lでベギノ′ト
ノ′と川、u+:ll/′、)の凸、、−のIL状に曳
’;!&r L、、白金」Iに−〉けると糸イI引り1
,1eのメス゛吟リンダ−に汲んでHll1l間:’+
’r1置し°Cも全<  l’:FIJ’SVつo−L
l 、 SVI  61、jlii ′LI−不能(u
 l/1./、+不能)であ−)/〔0 (4)J4+i素の没入及び結1]! 12%の次亜塩素酸ナトリュームと18%の塩酸を用い
両者の混合比を3=・lとして前記次亜塩素酸ナトリュ
ームと塩酸の混合溶液ル″メ造装置r1°により、流入
汚水に対し最初15 pprnの塩素rdから流入汚水
1]付近に投入を111始し、糸状菌の減少につれて添
加塩累衛を減らした。塩素の投入は24時間連続して行
った。汚泥の経時的前記汚泥を経時的に検鏡したところ
、10日目頃から糸状菌の長さが短かくなり、20日目
頃から糸状菌の量が目立って減った。1ケ月目にはズー
グレア(Zoogloea )主体の汚泥になし、固着
フ1νのj車止が増した。その1(塩素f’llを”A
kらし/ヒが、糸状菌の増殖U、なく、またNo、ss
が増加してもきわめて沈降性もよ< 、?ill+t’
l1Mのギーvリーオーバーの心配も全く無くなった。
(:Ll lr; li's 1 / child MLss's borrowing is 2 D tl tl ■) 111, Ken<;7':,, then filamentous fungi (1,!:L with Begino'Tono' and River, The convexity of u+:ll/', ) is drawn in the shape of IL of -;! &r L,,Platinum" I -> When I put it, I pull the thread I I 1
, pump into the female cylinder of 1e and between Hll1l:'+
'r1 place °C also all <l':FIJ'SVtsuo-L
l, SVI 61, jlii 'LI-unable (u
l/1. /, +impossibility) de-)/[0 (4) J4+i elementary immersion and conclusion 1]! Using 12% sodium hypochlorite and 18% hydrochloric acid at a mixing ratio of 3=·l, a mixed solution of sodium hypochlorite and hydrochloric acid was initially applied to the inflowing sewage using the liquid-forming device r1°. 15 pprn of chlorine was added to the vicinity of the influent sewage 1], and the amount of added salt was reduced as the number of filamentous bacteria decreased.Chlorine was added continuously for 24 hours. When microscopically examined over time, the length of filamentous bacteria became shorter from around the 10th day, and the amount of filamentous fungi decreased noticeably from around the 20th day.In the first month, the sludge was mainly composed of Zoogloea. None, the number of fixed f'1ν j vehicle stops increased. Part 1 (Chlorine f'll was added to "A")
There is no growth of filamentous fungi, no, ss
Even if the amount increases, it is still extremely sedimentary. ill+t'
I no longer have to worry about l1M's glee overflow.

実施例2 曝気戊うグーン力式の処理装置による例 (1)装置の概略 1曝気槽の容11)が21) 00 mの一槽のみで、
表面曝気方式。115I気++!j間は18時間7′市
1y。
Example 2 An example using an aeration-type treatment device (1) Approximate outline of the device 1 The capacity of the aeration tank 11) is 21) 00 m, and only one tank is used.
Surface aeration method. 115I ki++! J time is 18 hours 7' city 1y.

(2)流入汚水 人1り(上として−1,j腐)1ノ1水で約8001/
市y、+1(月)は約1.(100ppm。
(2) Inflow of sewage for 1 person (-1,j rot) 1 no 1 water is approximately 8001/
City y, +1 (month) is approximately 1. (100ppm.

(:3+  iri泥の状況 Mr、5salが6000 ppm、検鏡すると糸状菌
が密植し、5V50== 1 (1(1、SVI j’
J、’1il’)’:Lイ’能であ−)だ。
(:3+ iri mud situation Mr, 5sal is 6000 ppm, microscopic examination shows that filamentous fungi are densely planted, 5V50 == 1 (1 (1, SVI j'
J, '1il')': L'i'no de-)'.

(4)塩素の役人及びf¥l’i尤 実施例1と同じ方法により流入/’j水に利し塩素の投
入用を25 pl)mから投入を開始した。
(4) Injecting chlorine into the inflow water using the same method as in Example 1 was started from 25 pl) m.

汚泥の経時的な変化は次のとおりであつフt。Changes in sludge over time are as follows.

経時的な検♀り・、結果は40日目頃から目立って糸−
状閉が少なくなり、 MLS8が増したにも拘らず沈降
性がきわめて良好になり、以後塩素Filを減らしても
、バルキングが起ることがなかった。
Testing over time・The results were noticeable from around the 40th day.
Even though the MLS8 increased, the sedimentation properties became very good, and no bulking occurred even after reducing the chlorine content.

前記したようにこの発明に係る活性汚泥の糸状菌抑制力
法によれi、塩素を一定用曝気槽白に投入するだけで、
バルキングを改′@泊疼することができるばかりでなく
、単に、忙(川の塩素の投入を相、続するだけでバルキ
ングを完全に予防することができ、しかもこの程度の塩
素の投入[dでは塩素による他の公害を引き起こすこと
もtlい1、また、塩素は酸化信用があるので1曝気、
hll、′の/り泥の自己消化をイ足ilHすることが
でき、lり泥中1友きの労力及びに1Y費をf’ii’
+ρ111.することができる効1よち自j−る。
As mentioned above, according to the activated sludge filamentous bacteria suppressing power method according to the present invention, by simply adding chlorine to the aeration tank white,
Not only can bulking be improved, but bulking can be completely prevented simply by successively adding chlorine from the river; However, chlorine may cause other pollution1, and since chlorine has oxidation properties,1 aeration,
The self-extinguishment of the mud can be completed quickly, and the labor and cost of the mud can be reduced by f'ii'.
+ρ111. The effect that can be achieved is 1.

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

第1図はli’:性7’r泥方式のソ[1−の・−例を
/J<ず概略図、EB82図ばII′4気j(ラグーン
カ式の〕I+−の・−例を小す概略図である。 1・・・流入lfj水のjA:、i1′8.2・・・最
i割の化7..j+h屯、3・・・流、路、4・・・曝
気槽、5・・・流入lり水投入11伺近、6・・・iI
a終沈Ill jlJL /、ii、 人l 1イ・]
J!i、7 ”’ h’J、i% :、、、CSQ t
1!t i’ljl、人ll。
Figure 1 is a schematic diagram of the /J<zu example of the li': 7'r mud method, and EB82 is a schematic diagram of the example of It is a small schematic diagram. 1... jA of inflow lfj water:, i1'8.2... Maximum i percent conversion 7..j + h ton, 3... flow, path, 4... aeration Tank, 5...Inflow water input 11, 6...iI
a end sinking Ill jlJL /, ii, person l 1i・]
J! i,7 ”'h'J,i%:,,,CSQ t
1! t i'ljl, peoplell.

Claims (1)

【特許請求の範囲】[Claims] 1.1曝気槽を右する微生物酸(比処理装置において、
流入汚水量にり・1し5〜60 ppmに相当する塩素
量、を曝気1itv内の1モ意箇所に投入することを特
徴とする活性tυ泥中の糸状微生物抑制方法。 11、曝気槽が活性汚泥方式である特5′[請求の範囲
第1項記載の活性汚泥中の糸状微生物抑制方法。 1、  I曝気槽が曝気式ラグーン(曝気式酸化池)方
式である特許請求の範囲第1項記載の活性汚泥中の糸状
微生物抑制方法。 1■  塩素の投入場所が流入汚水投入1−1付近であ
る特;j’l’ jl’l求の範囲第1拍記戦の糸状微
生物抑制力ことを特徴とする特許請求の範囲第1項記戦
の〆X計り汚泥中の糸状微生物抑制方法。 ■、投入する塩素が気体である粕許請求の範囲第1項記
載の活慴汚泥中の糸状微生物抑制方法、ν1[、投入す
る塩素が次曲塩素酌プトリュートと塩酸の混合液体であ
る!IIJ許31’l求の範囲第1項記戦の活性汚泥中
の糸状微生物1111制力法。 49次亜塩素酸ナトリュームと塩酸の比率が純物質とし
て1乃至37J ]の割合である特i’l請求の範囲第
■I項記載の活性汚泥中の糸状微生物抑制力〆去。
1.1 Microbial acids in the aeration tank (in specific treatment equipment,
A method for inhibiting filamentous microorganisms in activated tυ mud, characterized by introducing an amount of chlorine equivalent to 5 to 60 ppm based on the amount of inflowing sewage into one point in one aeration unit. 11. The method for inhibiting filamentous microorganisms in activated sludge according to claim 1, wherein the aeration tank is of an activated sludge type. 1. The method for inhibiting filamentous microorganisms in activated sludge according to claim 1, wherein the aeration tank is of an aeration lagoon (aeration oxidation pond) type. 1. Claim 1 characterized in that the place where chlorine is introduced is near the inflow sewage input 1-1; A method for suppressing filamentous microorganisms in X-measured sludge. (2) A method for inhibiting filamentous microorganisms in activated sludge according to claim 1, in which the chlorine to be added is a gas; 1111 method for controlling filamentous microorganisms in activated sludge as described in Section 1 of IIJ Permit 31'l. 49. The inhibitory power of filamentous microorganisms in activated sludge according to claim 1, wherein the ratio of sodium hypochlorite and hydrochloric acid is 1 to 37 J as pure substances.
JP57154579A 1982-09-07 1982-09-07 Suppression of filiform bacteria growth in activated sludge Pending JPS5946192A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57154579A JPS5946192A (en) 1982-09-07 1982-09-07 Suppression of filiform bacteria growth in activated sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57154579A JPS5946192A (en) 1982-09-07 1982-09-07 Suppression of filiform bacteria growth in activated sludge

Publications (1)

Publication Number Publication Date
JPS5946192A true JPS5946192A (en) 1984-03-15

Family

ID=15587297

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57154579A Pending JPS5946192A (en) 1982-09-07 1982-09-07 Suppression of filiform bacteria growth in activated sludge

Country Status (1)

Country Link
JP (1) JPS5946192A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04126593A (en) * 1990-09-17 1992-04-27 Shikoku Chem Corp Method for dissolving bulking due to filamentous fungus in apparatus for treating waste water
JP2005319386A (en) * 2004-05-07 2005-11-17 Seiko Pmc Corp Method for suppressing swelling
CN109179652A (en) * 2018-08-16 2019-01-11 海天水务集团股份公司 A kind of low C/N is than organic wastewater denitrifying method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04126593A (en) * 1990-09-17 1992-04-27 Shikoku Chem Corp Method for dissolving bulking due to filamentous fungus in apparatus for treating waste water
JPH0585239B2 (en) * 1990-09-17 1993-12-06 Shikoku Chem
JP2005319386A (en) * 2004-05-07 2005-11-17 Seiko Pmc Corp Method for suppressing swelling
CN109179652A (en) * 2018-08-16 2019-01-11 海天水务集团股份公司 A kind of low C/N is than organic wastewater denitrifying method

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