JPS58202097A - Treatment of ammonia liquor with activated sludge - Google Patents
Treatment of ammonia liquor with activated sludgeInfo
- Publication number
- JPS58202097A JPS58202097A JP57079132A JP7913282A JPS58202097A JP S58202097 A JPS58202097 A JP S58202097A JP 57079132 A JP57079132 A JP 57079132A JP 7913282 A JP7913282 A JP 7913282A JP S58202097 A JPS58202097 A JP S58202097A
- Authority
- JP
- Japan
- Prior art keywords
- treatment
- activated sludge
- rice bran
- aeration tank
- days
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Abstract
Description
【発明の詳細な説明】 の迅速lgl儂処理方法に関するものである。[Detailed description of the invention] The present invention relates to a rapid lgl treatment method.
女水は,石縦を乾貿してコークスを製造する除に腺科の
石炭の約10〜15N発生する.安水はフェノール.ク
レゾール,キシレノールなどの肩嶺智およびアンモニア
化合物,シ・l/化合物,ジダン化合物,チオ値鹸化合
物.#L化物などの無慎化合物會含有しておfi,CO
Dも5, 0 0 0〜10、000 1)I)m
と高<、 ’!*. *Ik褐色を呈しておシ,仁の
ま\で社公共水域に排出することができない。Mesui produces about 10 to 15N of coal, which is produced during the dry trade of stone and coke production. Anhydrous water is phenol. Cresol, xylenol, etc., and ammonia compounds, cylindrical compounds, didane compounds, and thiovalent compounds. #Contains unscrupulous compounds such as chloride, CO
D is also 5,000~10,000 1)I)m
and high <, '! *. *It exhibits a brown color and cannot be discharged into public water bodies due to its unrefined state.
この安水の無筈化処理は,蒸留法などによりア泥MJ1
理を行なうのが通富の方法である。This ammonium water treatment is carried out by distillation method etc.
The method of Tsutomi is to practice the principles.
安水の活性汚泥処理は,フェノール系化合物。Activated sludge treatment of ammonium water uses phenolic compounds.
ロダン化合物などのOOD成分の大部分を分解除去する
1費なプロセスであるにもか\らず%都市下水などの活
性汚泥処理の設備, ym. m条条件などt.そのま
\模倣している.しかし、安水は都市下水などに比べて
組成的に複雑であり、また。Although it is an inexpensive process that decomposes and removes most of the OOD components such as rhodan compounds, it is necessary for activated sludge treatment equipment for municipal sewage, ym. m-line conditions etc. t. I'm just imitating it. However, cheap water is compositionally more complex than municipal sewage, etc.
シアン化合物.憾化物など活性汚泥の+IA舵を組合す
る成分を含有しているので.S市下水などの油性汚泥の
設備仕様,管理,操業技術などt,そのtま安水に適用
するには限界がある。Cyanide. Because it contains components such as pollutants that combine with the +IA rudder of activated sludge. There are limits to the equipment specifications, management, and operating technology for oily sludge such as S City sewage, but there are limits to its application to oily sludge.
このため、従来の安水活性汚泥処理1よ、原因不明の処
堆不閾が発生しやすく,また、処理不一が発生すると.
原因,対策および回傷技術などが明らかにされていない
ため、その回復方法は試行錯1的であり、回復に1〜6
り月の長期間を賛することがある。For this reason, compared to the conventional ammonium water activated sludge treatment 1, unexplained treatment failure thresholds are likely to occur, and if treatment failure occurs.
Because the causes, countermeasures, and injury techniques have not been clarified, recovery methods are based on trial and error, and recovery takes 1 to 6 days.
Sometimes people praise the long period of the moon.
さらに、処理不一が発生した場合の1要な問題点け、処
理不調の多くのケースにおいて、ロダン化合物の分解性
が低下し処理水質が感化することである。この処理水中
のロダン化合1ハ鉄凝集t′数θ1.活a辰奴着法など
の物理化学的処理によっても除去困難でしハ現在のとこ
ろ、活性汚泥処理以外の方法では経済的にしかも効率的
に除去する(支術が確立されていない、従って、このよ
うな場合、活性汚泥処理の後に鉄凝果沈澱法、活性板l
IX鳥法などの退願処理設偽を設置してもロダン化合物
は、この処理設備t−素通りして除去することができな
い。Furthermore, one important problem when treatment failure occurs is that in many cases of treatment failure, the decomposability of the rhodan compound decreases and the quality of the treated water becomes sensitive. The iron aggregation t' number θ1 of the rhodan compound 1 in this treated water. It is difficult to remove it even with physical and chemical treatments such as activated sludge treatment, and at present, methods other than activated sludge treatment have not been established to remove it economically and efficiently. In such cases, after activated sludge treatment, iron coagulation precipitation method, activated plate l
Even if a withdrawal processing system such as the IX Bird Method is installed, the rodan compound cannot be removed by passing through the processing equipment.
このロダン化合壷を分解する菌(ロダン資化菌)fJ、
、)エノールなどを分解する鉋に比べてN殖性が着しく
遅く、発明者の研九によると毒性vIJ質。Bacteria that decomposes this Rodan compound jar (Rodan assimilating bacteria) fJ,
,) Compared to a plane that decomposes enol etc., N-fertilization is slow and slow, and according to the inventor Kenkyu, it is toxic.
P IIなどのンヨツクによルロダン員化−の機能が低
下した場合、これらのVヨソクを取9臓い友俵。If the function of the drug is reduced due to drugs such as P II, these V drugs should be removed.
60日も要することが明らかになっている。この期間は
、処理水のCl0D、 ロダン濃度が高い状態が続くこ
とになる。It has been revealed that it will take up to 60 days. During this period, the Cl0D and rhodan concentrations in the treated water will remain high.
もう一つの重要な問題点は、製鉄所から発生するOOD
量のうち安水関係に起因するOODが約50〜70%と
最も高い比率を占めてお9、安水の活性汚泥処理の不調
が発生し、処理不調が長期化すると環境排出規制を遵守
できなくなる懸念がある。Another important issue is OOD generated from steelworks.
Out of the amount, OOD caused by ammonium water accounts for the highest proportion of approximately 50 to 70%9.If malfunctions occur in the activated sludge treatment of ammonium water and the treatment malfunction continues for a long time, environmental discharge regulations cannot be complied with. There are concerns that it will disappear.
発明者らは、すてに安水のIIJI埋に適した処理技術
を確立しているが、処理率al11に対して祉必ずしも
十分対処できなかった。そこで本発Ql[、従来法を改
善するために安水の活性汚泥処理が不調になったときに
従来の方法よシも著しく短期間に回復させる技術を完成
するに至ったものである。Although the inventors have already established a treatment technology suitable for IIJI burial of ammonium water, they have not always been able to adequately cope with the treatment rate al11. Therefore, in order to improve the conventional method, the present company has completed a technology that allows the activated sludge treatment using ammonium water to recover in a significantly shorter period of time than the conventional method when it becomes malfunctioning.
安水の活性汚泥の機能を阻害する成分によるショック、
あるい紘異常pHによるショックによる活性汚泥の処理
不調は、これらのショックにより活性汚泥を構成してい
る2クチリヤ(資化III)がかな)死滅していること
に起因している。Shock caused by components that inhibit the function of activated sludge in ammonium water,
The malfunction of activated sludge treatment due to the shock caused by the abnormal pH is due to the fact that the 2 Kutilya (Assimilation III) constituting the activated sludge is killed by these shocks.
し友がって、処理不調が正常な処理状態に回復するため
には、まず、ショックにょ9減少したバクテリヤを増殖
させて正常な処理を行なってい九時の状IIK回復しな
けれにならない。In order for the processing disorder to return to the normal processing state, the bacteria that have been reduced by 9 levels due to the shock must first be allowed to proliferate and the normal processing to be carried out to restore the state to the normal state.
処理不調の活性汚泥を正常な状態に回復させる方法社、
処理不調になった原因を取り除いて活性汚泥処理のpH
s温度、DOなどを適正な条件に管理する方決がt%普
遍的である。Method Company, which restores poorly processed activated sludge to normal condition.
Improve the pH of activated sludge treatment by removing the cause of treatment failure.
The most common method is to control temperature, DO, etc. under appropriate conditions.
しかし、活性汚泥は各種バクテリヤの集合体であり、各
ノセクテリャの性状がかな多異なっていることが考えら
れる。たとえば、先に説明したようにロダン資化菌の増
殖速mu非常に遅く1例えばフェノール系化合物を分解
するツマクチリヤの約1/4oである。したがって、安
水の活性汚泥処理の不調を短期間に1復させる九めに社
、ロダン資化lIOように増殖速度の遅いバクテリヤの
増殖速1を促進する必要がある。However, activated sludge is a collection of various bacteria, and it is thought that the properties of each bacteria are quite different. For example, as explained above, the growth rate mu of Rodan assimilating bacteria is very slow, for example, about 1/4 of that of Tumakuchiria, which decomposes phenolic compounds. Therefore, it is necessary to accelerate the growth rate of bacteria that have a slow growth rate, such as Rodan Assimilation IIO, in order to quickly restore the malfunction of activated sludge treatment using ammonium chloride.
従来の不go關復方法は、活性汚泥処理の条件すなわち
、温1. DOなどを管理しバクテpH。In the conventional waste recovery method, the activated sludge treatment conditions are 1. Control DO etc. and bacterium pH.
リヤの自然増殖を期待するに過ぎず、このような方法で
は処理不調の回復線、先に説明したように復させるため
KAバクテリヤ特に、ロダン資化−の増殖を促進させて
l&処理不調短期間に°回復させる方法について研究を
行なった。However, in this method, in order to recover from the processing failure, as explained earlier, the growth of KA bacteria, especially Rodan assimilation, is promoted and the treatment failure is short-term. We conducted research on ways to recover.
一般に、/?バクテリヤ微量のピタきン、金属塩。in general,/? Bacterial traces of pitaquin, metal salts.
酵素などが存在すると増殖適度が促進されることが知ら
れている0発明者らは、この点に着目し。It is known that the presence of enzymes and the like promotes moderate growth.The inventors focused on this point.
ビタミン、金槁塩、酵素などt安水活性汚泥処理の曝気
槽に添加し、バクテリヤの増殖速[を#J定した結果、
ロダン資化菌を例にとると無添加の場 。As a result of adding vitamins, gold salt, enzymes, etc. to the aeration tank of T-ammonium water activated sludge treatment, the growth rate of bacteria was determined.
If we take Rodan assimilating bacteria as an example, it is an additive-free environment.
合に比べて増殖速度が約2〜5倍も促進されることを知
見した。これらの結果から、@性汚泥処理O不調が発生
した場合、ビタミン、11素、金属塩などを添加すると
不調が短期間に回復することが考えられる。It was found that the proliferation rate was promoted by about 2 to 5 times compared to that in the case where From these results, it is considered that when @-type sludge treatment O malfunction occurs, the malfunction can be recovered in a short period of time by adding vitamins, element 11, metal salts, etc.
そこで、実際に不調が発生し良活性汚泥処JlK添加し
え結果、ロダン化合物の分解不良の紬復は。Then, a malfunction actually occurred, and as a result of the addition of JLK to the activated sludge treatment, Tsumugi was able to recover from the poor decomposition of the rhodan compound.
従来の方法が20〜60日間も要し九のに対してビタイ
ン、金輌塩、酵嵩などを添加することによ多7〜10日
間で回復した。The conventional method took 20 to 60 days, but by adding vitamine, gold salt, yeast, etc., the disease recovered in 7 to 10 days.
しかし、実設備の処理不調にこの方法を適用すると大t
oビタイン、#累などを必要とし、コスト的に間Mがあ
り実用化はかなシ困離で漬る。そこで発明者らはピメミ
ン、′#素などに代るもので女−で且つ大量に入手でき
るものについて検討しえ給米、米ヌカーfi最適である
ことを見出した。However, if this method is applied to processing problems in actual equipment, it will cause a huge amount of trouble.
It requires a bitine, #cumulative, etc., and its cost is long, making it difficult to put it into practical use. Therefore, the inventors investigated alternatives to pimemin, rice flour, etc., which are suitable for women and can be obtained in large quantities, and found that they are optimal for use in rice feeding and rice bran.
米ヌカの成分は1表−1に示すように多種類のピタ建ン
、無機質、栄養嵩等を含有してお′1.また1表−1の
成分の他にオレイン酸、リノールH。As shown in Table 1, rice bran contains many types of pita nuts, minerals, nutritional bulk, etc.'1. In addition to the components listed in Table 1-1, oleic acid and linole H are also included.
ノ臂ルアテンIII!ナト0J11肪酸のグリセリンエ
ステル。Noel Aten III! Glycerin ester of nato0J11 fatty acid.
スクアレン、ステリンなどを含んでおplこれら#i表
−10成分とJiig様にバクテリヤの増殖を促進する
作用がある。Contains squalene, sterine, etc. These #i Table 10 ingredients and Jiig-like have the effect of promoting bacterial growth.
表−! 米ヌカ成分の一例 (100f中)この米ヌカ
をもちいて安水活性汚泥処理の不一を°回復させる方法
は、非゛にに簡単である。すなわち%活性汚泥処理の曝
気槽に米ヌカを所ににその′を一散布すれは良い、米ヌ
カの畝布瀘は処理不一の−kによって異なるが、処理不
一が軽嵐の場合は、−気m1m/当9に米X力tlEI
K10〜30ft約5日間8に、また、処理不一がm征
の場合は、1日に500〜1,0(10fmlt3日〜
10日間程I[散布すれは良い。Table-! Example of rice bran component (100 f) The method of using this rice bran to recover from defects in aqueous activated sludge treatment is extremely simple. In other words, it is good to spray rice bran once in the aeration tank of activated sludge treatment. , -ki m1m/to 9 US X force tlEI
K10~30ft for about 5 days 8, and if the processing is uneven, 500~1,0 per day (10fmlt3 days~8)
Spraying is good for about 10 days.
米メカの散布により曝気槽の泡が直ちに消えると同時に
嫁化瀘元−位(ORP)が低下する。The bubbles in the aeration tank disappear immediately due to rice spraying, and at the same time, the ORP decreases.
ORFの低下度合は、米ヌカの添加量によって異なるが
約l′o〜200 mV 程度低下する。この01L
P低下は、活性汚泥が米ヌカを分解していることを示唆
している。しかし、活性汚泥による米ヌカの分解をさら
に促進するとともに処理不調を迅速に回復させるために
[ORPの大巾低下を抑制する必要がある。その方法と
して曝気量の増量により0RPt適正値に回復させる方
法が良い、しかし、米ヌカの添加量が大量の場合、適正
値に回復しにくい場合がある。そこで曝気量の増量によ
)適正値下の少くと450mv以内に回復させればはと
んどの場合に米ヌカの分解がI[ill!に進み。The degree of decrease in ORF varies depending on the amount of rice bran added, but it decreases by about 1'o to 200 mV. This 01L
The decrease in P suggests that the activated sludge is decomposing rice bran. However, in order to further promote the decomposition of rice bran by activated sludge and to quickly recover from processing failures, it is necessary to suppress the large decrease in ORP. A good way to do this is to restore the 0RPt to the appropriate value by increasing the amount of aeration. However, if a large amount of rice bran is added, it may be difficult to restore the 0RPt to the appropriate value. Therefore, if the amount of aeration is increased (by increasing the amount of aeration), the decomposition of rice bran will be reduced in most cases if it is restored to at least 450 mV below the appropriate value. Proceed to.
処理不調の回復を促進することができることがわかった
。It was found that it can promote recovery from processing disorders.
次に、実施例により米ヌカ添加による活性汚泥処理の不
14m復方法について説明する。Next, a method for recovering activated sludge by adding rice bran will be explained using an example.
同一規模、処理条件の2台の実験用活性汚泥処理装置を
もちいて表−2に示す条件により安水の活性汚泥処理を
行い、処理不i!i1Mを起させるため曝気槽OpHを
7.0から4,5に下げ、この状態を12時間保持した
。このpHV :llツクによル活性汚泥の酸素消費速
度は、正常時に比べて約90〜95X4低下し、第1図
に永すようにCODが急上昇し、又第2図に示すように
ロダン化合物は。Using two experimental activated sludge treatment equipment of the same scale and treatment conditions, activated sludge treatment of ammonium water was carried out under the conditions shown in Table 2. In order to cause i1M to occur, the aeration tank OpH was lowered from 7.0 to 4.5, and this state was maintained for 12 hours. As a result of this pHV, the oxygen consumption rate of the activated sludge decreased by approximately 90 to 95x4 compared to normal conditions, the COD increased rapidly as shown in Figure 1, and the rhodan compound increased as shown in Figure 2. teeth.
はとんど分解しなくなル完全な不調状態になった。It almost stopped disassembling and became completely unwell.
図中ムは、不調の活性汚泥処理の曝気槽1+vl当ル米
ヌカを12日から14日目に1日に300tづツ3日r
I17J敏布t、、罎iq曽のonpを+150〜20
0JJ]V K、りHを7.0±12に制御管埋した場
合の経過を示した。一方1図中Bは米ヌカを散布せずに
曝気槽のpHを7.0±0.2.ORP’1200土1
6mvに1御管理して簀水の処理を行なった場合の経過
を示し友」
なお、活性汚泥処理ムは、米ヌカt−敗布すると曝気槽
のORPが設定値(+200mV)から+50〜−50
111Y まで低下するが、曝気kcD増倉によ30R
Pf:+tso 〜200uiv の範囲に制#、管
理を行なった。In the figure, 300 tons of rice bran per day was added for 3 days from the 12th to the 14th.
I17J Minpu t,, 罎iqso's onp +150~20
0JJ] The progress when the control tube was buried at 7.0±12 for VK and RIH is shown. On the other hand, in Figure 1 B, the pH of the aeration tank was set to 7.0±0.2 without spraying rice bran. ORP'1200 Sat 1
In addition, in activated sludge treatment, if rice bran is destroyed, the ORP of the aeration tank will be +50 to - from the set value (+200 mV). 50
It drops to 111Y, but with aeration kcD Masakura 30R
Control and management were performed within the range of Pf: +tso to 200 uiv.
その結果、第1図 及び第2図 に示すように、pHシ
曹ツク畿の処理水の00D、ロダン化合−の#IIfが
pHショック前に回復するのに要する期間は、米ヌカを
散布した場合が散布後約7日間で1復するOK対し、米
ヌカを散布しない楊合−轄−約35日間も要した。As a result, as shown in Figures 1 and 2, it was found that the period required for 00D and #IIf of the rhodan compound to recover before the pH shock in the treated water of the pH-treated Sootsukuki area was longer than the period required for the rice bran to be sprayed. While the case recovered after about 7 days after spraying, it took about 35 days for Yanghe, who did not spray rice bran.
仁れらのことから、処理不調の活性汚泥処理のm気槽に
米ヌカを散布するとともに01’LP値を適正に維持す
ると処理不−の回復に著しく効果があることが明らかに
なった。It has become clear from Nire et al. that spraying rice bran on an activated sludge treatment tank with malfunctioning treatment and maintaining an appropriate 01'LP value is extremely effective in recovering from poor treatment.
また、米ヌカ散布の別の幼果は、第3図 及び第4因
に−気槽の活性汚泥の鏡度(ML88)。In addition, other young fruits sprayed with rice bran are shown in Figures 3 and 4.
- Mirror quality of activated sludge in the air tank (ML88).
沈降性(SV、・、 8V1 )などの性状を示してい
るが、米ヌカを散布すると(凶中人)約5.00011
1m>111(2)MLS8が約7日後には約10.O
OOPpj1mK増加し、tた沈降性の尺度である8V
1 は、pHクシシック時約110であったものが、
米ヌカ散布後、約108目には約55まで低下し、活性
汚泥の沈降性が着しく向上した。It shows properties such as sedimentation (SV,..., 8V1), but when rice bran is sprayed (Kyochunin), it is about 5.00011
1m>111(2) MLS8 becomes about 10.0m after about 7 days. O
OOPpj1mK increased to 8V, a measure of sedimentation.
1 had a pH of about 110 at the time of oxidation, but
After spraying rice bran, it decreased to about 55 at about 108 days, and the sedimentation property of activated sludge improved significantly.
一方、米ヌカ散布しない場合は(図中B)%pmショッ
クによる鵡理不−が回復してもML88の増加、+3V
1 の低下などの効果が表われない。On the other hand, if rice bran is not sprayed (B in the figure), even if the unreasonableness caused by %pm shock is recovered, ML88 increases and +3V
No effects such as a decrease in 1 are observed.
このように、米ヌカ散布紘、処理不調の回復期間の短縮
の他に、活性汚泥O増殖性、沈降性の同上に著しく効果
があることが判明した。In this way, it has been found that in addition to shortening the recovery period for rice bran spraying and treatment failures, it is also significantly effective in improving activated sludge O proliferation and settling properties.
なお、処理不調のtgln法として、−気槽に米ヌカ散
布と同峙に、塩化第二鉄の水耐液t−活性汚泥!&堰に
添加しても良い、塩化第2鉄の添加方法は。In addition, as a TGLN method for treatment failure, water-resistant liquid t-activated sludge of ferric chloride is used in addition to rice bran spraying in the air tank! & How to add ferric chloride, which can be added to the weir.
−気槽に直接散布しても艮いし、また、供給原水に塩化
第2鉄を添加して活性汚泥処理のm気槽に供給しても良
い、さらに、塩化第2鉄の添加方法として、活性汚泥処
理設備の汚泥沈降槽のセンターフェルに添加しても良い
、この方法は、汚泥沈降槽における活性汚泥の沈降性を
良くするとともに、@気槽に返送される活性汚泥ととも
に鉄塩も曝気槽に返送されるので、鉄塩がバクテリヤ増
燻作用管促進する効果がある。- It may be applied directly to the air tank, or ferric chloride may be added to the raw water to be supplied to the air tank for activated sludge treatment.Further, as a method for adding ferric chloride, It can be added to the center fel of the sludge settling tank of activated sludge treatment equipment.This method improves the settling properties of activated sludge in the sludge settling tank, and also aerates iron salts along with the activated sludge returned to the air tank. Since it is returned to the tank, the iron salt has the effect of promoting bacterial smoke-enhancing action.
なお、塩化第2鉄の添加によ)m気槽のPMが適正値(
PH7,0±0.5)より低くなった場合、水酸化カル
シウムなどのアルカリ剤t−曝気槽、供lll1原水、
活性汚泥の沈降槽のセンターフェルに添加してGIHを
調整すれに良い。In addition, by adding ferric chloride, the PM of the m-air tank can be adjusted to the appropriate value (
If the pH is lower than 7.0 ± 0.5), use an alkaline agent such as calcium hydroxide in an aeration tank, supply lll1 raw water,
Good for adjusting GIH by adding it to the center fel of activated sludge settling tank.
以上説明したように本発明は安水の活性汚泥処理におけ
る不一時に活性汚泥処理のm気槽に米ヌカを添加すると
ともKORP値を適正に維持する簡単な方法によ)処理
不調を迅速KIJ後することがてきる。As explained above, the present invention uses a simple method for temporarily adding rice bran to the activated sludge tank in the activated sludge treatment of ammonium chloride water and maintaining the KORP value appropriately. I can do it later.
第1図 は、活性汚泥処理水のOOD、又第2図 は、
關ダン化合物の経時変化を示したもので。
Aは米ヌカを散布した場合、Bは米ヌカを散布しない場
合である。
第3図 は、m気槽の活性汚泥411.44図は、8V
1をそれぞれ示したものである。
代理人 弁理士 秋 沢 政 光
他2名
″<t +tn
昭和57年 6月22日特許庁 長 官 殿
1、=4′−件の表示
特願昭57−第 79132号
3、補正をする者
′4谷注との関係 出願人
住所(居所) 東京都千代田区大手町2丁目6番3号氏
名(名称) (665)新日本製鐵株式会社4、代
理 人
居 所 東京都中央区日本僑兜町12番1号大洋ビル5
、 Ml i)、 @ 6 の日付昭和 年 月
日(発送)11−絶埋山通in
補正の内容
明細書を下記の通り訂正する。
(1)第5頁第13行、「例えば」とあるのを削除する
。
(2) 第6頁第15行、「とを知見した。」を「と
が判明した。」と訂正する。
(3)第8頁表−1中、「無機質(2)」とあるのを、
「無機質(rnν)」と訂正する。
(4)第13頁表−2中、下から3行目、r(svtl
lo)Jとあるのを削除する。
t17 I’ll 昭和
57年9月Z日特許庁長官 殿
1 “IYイ′(の表示
特願昭57−第 79132 号
安水の活性汚泥処理方法
3、補正をする者
14件との関係 出 願 人
住所(居−所)東京都千代田区大手町2丁目6番3号氏
名(名称) (665)新日本製鐵株式会社4、代 理
人
居 所 東京都中央区[」本僑兜町12番1号大洋ビル
袖11−命令
5、□の日付昭和57年8 月31日(発送・)6、補
正により増加する発明の数 な し補 正 の
内 容
1、 明細書牙14頁第2〜7行を下記の通り訂正する
。
す図である。」
2 図面牙1図乃至第4図を別紙の通り訂正する。Figure 1 shows the OOD of activated sludge treated water, and Figure 2 shows the OOD of activated sludge treated water.
This shows the changes over time in the Sedan compound. A is when rice bran is sprayed, and B is when rice bran is not sprayed. Figure 3 shows activated sludge in m-air tank 411.44 shows 8V
1 are shown respectively. Agent: Patent attorney Masamitsu Akizawa and 2 others”<t +tn
June 22, 1980 Director General of the Japan Patent Office 1 = 4' - Indication of Patent Application No. 79132 3, Person making the amendment' 4 Relationship with the note Applicant Address (Residence) Tokyo 2-6-3 Otemachi, Chiyoda-ku Name (665) Nippon Steel Corporation 4.
Address: 5 Taiyo Building, 12-1, Nihonkukabu-cho, Chuo-ku, Tokyo
, Mli), @ 6 Date: Showa Year, Month, Day (Shipping) 11 - Zetsubuyamadori in The statement of contents of the amendment is amended as follows. (1) Delete "for example" on page 5, line 13. (2) On page 6, line 15, ``I discovered that.'' is corrected to ``It became clear that.'' (3) In Table 1 on page 8, replace “Inorganic (2)” with
Correct it to "inorganic (rnν)". (4) Page 13, Table 2, 3rd line from the bottom, r (svtl
lo) Delete J. t17 I'll September 1980 Z, Commissioner of the Japan Patent Office, 1 "IY I'" (Representation of Patent Application No. 79132, Ammonium Water Activated Sludge Treatment Method 3, Relationship with 14 Amendments by Persons Making Amendments) Address: 2-6-3 Otemachi, Chiyoda-ku, Tokyo Name (665) Nippon Steel Corporation 4, Agent Address: Honkatocho, Chuo-ku, Tokyo No. 12 No. 1 Taiyo Building Sode 11 - Order 5, Date of □ August 31, 1982 (shipped) 6, Number of inventions increased by amendment None.
Content 1, lines 2 to 7 on page 14 of the specification are corrected as follows. This is a diagram. 2. Figures 1 to 4 of the drawings are corrected as shown in the attached sheet.
Claims (1)
c賑して、活性汚泥処理の曝気輸に米ヌカを添加すると
共に、米ヌカの添加にj9低下する敵化遺元電位(oa
p)に対応して%−気凰を増販する仁とによ50RP[
を適正値下の少くと450ムIIV以内に1復させ処理
を打なうことを特徴とする安水の活性汚泥処理方法。(1) Treatment rate wI4W in ammonium O activated sludge treatment
In addition to adding rice bran to the aeration process for activated sludge treatment, the addition of rice bran caused a drop in the potential (oa).
In response to p), increase sales of %-Kiou 50RP
A method for treating activated sludge with ammonium sludge, characterized in that the treatment is carried out by returning the ammonium sludge once to within 450 μm IIV, which is at least below the appropriate value.
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57079132A JPS58202097A (en) | 1982-05-13 | 1982-05-13 | Treatment of ammonia liquor with activated sludge |
| IT4827183A IT1173711B (en) | 1982-05-13 | 1983-05-11 | PROCEDURE FOR TREATING WASTE WATER FROM INDUSTRIAL PLANTS WITH ACTIVE MUD |
| FR838307942A FR2527585B1 (en) | 1982-05-13 | 1983-05-11 | PROCESS FOR THE TREATMENT OF INDUSTRIAL WASTEWATER WITH ACTIVATED SLUDGE |
| CA000427980A CA1197633A (en) | 1982-05-13 | 1983-05-12 | Process for treating industrial wastewaters by activated sludge |
| GB08313090A GB2121398B (en) | 1982-05-13 | 1983-05-12 | Process for treating industrial wastewaters by avtivated sludge |
| DE3317577A DE3317577C2 (en) | 1982-05-13 | 1983-05-13 | Process for the activated sludge treatment of waste water |
| AU14528/83A AU548300B2 (en) | 1982-05-13 | 1983-05-13 | Treating industrial waste waters by activated sludge |
| US06/902,069 US4698158A (en) | 1982-05-13 | 1986-08-27 | Process for treating industrial wastewaters by activated sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57079132A JPS58202097A (en) | 1982-05-13 | 1982-05-13 | Treatment of ammonia liquor with activated sludge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58202097A true JPS58202097A (en) | 1983-11-25 |
| JPS6211639B2 JPS6211639B2 (en) | 1987-03-13 |
Family
ID=13681419
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57079132A Granted JPS58202097A (en) | 1982-05-13 | 1982-05-13 | Treatment of ammonia liquor with activated sludge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58202097A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05285491A (en) * | 1992-04-14 | 1993-11-02 | Nippon Steel Corp | Coke oven effluent treatment method |
| WO2013118530A1 (en) * | 2012-02-09 | 2013-08-15 | 千代田化工建設株式会社 | Plant waste water treatment method and treatment system |
-
1982
- 1982-05-13 JP JP57079132A patent/JPS58202097A/en active Granted
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05285491A (en) * | 1992-04-14 | 1993-11-02 | Nippon Steel Corp | Coke oven effluent treatment method |
| WO2013118530A1 (en) * | 2012-02-09 | 2013-08-15 | 千代田化工建設株式会社 | Plant waste water treatment method and treatment system |
| JP2013158760A (en) * | 2012-02-09 | 2013-08-19 | Chiyoda Kako Kensetsu Kk | Treatment method and treatment system for plant wastewater |
| EA025954B1 (en) * | 2012-02-09 | 2017-02-28 | Тийода Корпорейшн | Plant waste water treatment methods and treatment systems |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6211639B2 (en) | 1987-03-13 |
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