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JPS6161694A - Treatment of waste water - Google Patents

Treatment of waste water

Info

Publication number
JPS6161694A
JPS6161694A JP59182781A JP18278184A JPS6161694A JP S6161694 A JPS6161694 A JP S6161694A JP 59182781 A JP59182781 A JP 59182781A JP 18278184 A JP18278184 A JP 18278184A JP S6161694 A JPS6161694 A JP S6161694A
Authority
JP
Japan
Prior art keywords
raw water
treatment
water
cod
treated 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
JP59182781A
Other languages
Japanese (ja)
Other versions
JPH0157638B2 (en
Inventor
Kozo Konishi
小西 功三
Kaneo Mizuno
水野 金夫
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 JP59182781A priority Critical patent/JPS6161694A/en
Publication of JPS6161694A publication Critical patent/JPS6161694A/en
Publication of JPH0157638B2 publication Critical patent/JPH0157638B2/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 increase the efficiency of the titled process by regulating raw water to the pH that the treatment efficiency becomes maximum before introducing the raw water into a treatment apparatus and thereafter introducing it into a biological treatment apparatus. CONSTITUTION:The pH value that the treatment efficiency becomes maximum is obtained in every waste water by means of preliminary experiment and the pH of raw water is regulated to the obtained pH and thereafter it is treated. In case of providing two or more stages of treatment vessels, COD contained in treated water of each stage on and after the second stage is adopted as the indication and raw water is passed so that the pH in which COD is made minimum becomes optimum pH. In regulating pH of raw water, NaOH or NH4OH is used as alkali and inorganic acid is used as acid.

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、生物学的廃水処理において、原水を処理装
置の導入前に処理効率が最大となる至適pH値に調整し
てから生物処理装置に導入する方法及び二段以降におい
ては、導入する原水を処理水CODが最小になるpH値
に制御して処理する方法に関するものである。 従来、生物学的廃水処理の至apHは中性であるとの固
定概念があり、従って廃水の種類を問わず中性になるよ
うに中和処理していたのが一般である。 また、廃水の浄化過程においてpHが上昇することが経
験的に知られていたが、浄化効率低下の要因として認識
されておらず従って制御することも行われていない。 更に、処理槽を二段以上に区分して各段の生物相を廃水
の浄化過程に合った形にして行うことは既に実施されて
いるが、各段のpHを至適pHに制御して効率を向上せ
んとする試みも行われていなかった。 本発明の目的は、廃水の種類(含有される基質)によっ
て異なる生物処理効率を最大にするように原水のpHを
調整することである・本発明は廃水4σに予@実験によ
って至適pH値を求め、この値に原水pHをWA整して
処理するものである。 更に処理梢を二段以上設δする場合は第2段以降各段の
処理水中のCODを指標としてCODを蔽小にするpH
を至1pHとして通液する。 原木のpH!l!11!’は、アルカリとしてはNa0
)1又はNH,OHであり、酸としては素側りが用いら
れるが像生物の機能阻害を少なくする意味で炭酸、硫酸
が好ましく有機酸は汚濁負荷をと昇させるので好家しく
ない。 以下1本発明における至適pHを決定する実験例を説明
する。 実験例1 流動床接触酸化装置を用いて キャラメル、ドロップの製菓廃水を原水とした場合の原
木pHと処理水P)Iとの関係を求めた結果は図のよう
であった。 原水 :  BoD 7000 181文 、 Goo
 3100  膳g/1.pH=3.0 Iズj e Ilt接触酸化処理条件。 流動床部容積 5.34文、担体充埴率30%栄養JI
  N : 0.05/BOD  重忙部 P : 0
.01/BOD重ji)部 +/、c気JIi2.θ又/分(105rn’ /BO
D−kg)空硲速11’  33 +1iL/am’ 
・分MLSS   11150〜2050  B/fL
原水滞留時間23.5h、 (BOD負荷B、fi3k
g/流動床ゴ・日) 原木のpH調整はNaOH水rd液で行った。 印出の敬字は処理水のCOD値[mg/gL+ 、 (
)内はBoD偵
This invention provides a method for biological wastewater treatment in which raw water is adjusted to an optimum pH value that maximizes treatment efficiency before introduction into a treatment device, and then introduced into the biological treatment device, and in the second and subsequent stages, the raw water is introduced into the biological treatment device. The present invention relates to a method of treating raw water by controlling the pH value to a value that minimizes the COD of treated water. Conventionally, there has been a fixed concept that the maximum aph in biological wastewater treatment is neutral, and therefore, regardless of the type of wastewater, it has generally been neutralized to make it neutral. Furthermore, although it has been empirically known that pH increases during the purification process of wastewater, it has not been recognized as a factor that reduces purification efficiency, and therefore no control has been carried out. Furthermore, although it has already been done to divide the treatment tank into two or more stages and adjust the biota in each stage to a form suitable for the wastewater purification process, it is difficult to control the pH of each stage to the optimum pH. No attempt was made to improve efficiency. The purpose of the present invention is to adjust the pH of raw water so as to maximize the biological treatment efficiency, which varies depending on the type of wastewater (substrate contained). is determined, and the pH of the raw water is adjusted to this value. In addition, when two or more stages of treated treetops are installed, the pH is adjusted to minimize the COD using the COD in the treated water of each stage from the second stage as an index.
The solution is passed through the solution until the pH reaches 1. Log pH! l! 11! ' is Na0 as an alkali
) 1, NH, OH, and as the acid, carbonic acid and sulfuric acid are preferable in order to reduce the inhibition of the functions of the living organisms, and organic acids are not suitable as they increase the pollution load. An experimental example for determining the optimum pH in the present invention will be described below. Experimental Example 1 The relationship between the pH of raw wood and treated water P)I was determined using a fluidized bed catalytic oxidation device using caramel and drop confectionery wastewater as raw water. The results were as shown in the figure. Raw water: BoD 7000 181 sentences, Goo
3100 servings/1. pH=3.0 Izj e Ilt catalytic oxidation treatment conditions. Fluidized bed volume 5.34 sentences, carrier filling rate 30% Nutrition JI
N: 0.05/BOD Heavy duty section P: 0
.. 01/BOD heavy ji) part +/, cki JIi2. θ/min (105rn'/BO
D-kg) Empty speed 11' 33 +1iL/am'
・Minute MLSS 11150~2050 B/fL
Raw water residence time 23.5h, (BOD load B, fi3k
g/fluidized bed g/day) The pH of the raw wood was adjusted with a NaOH aqueous solution. The printed honorifics are the COD value of the treated water [mg/gL+, (
) is BoD Detective

【1g1文】である。 1多において原水pH6以上では処理水のpHは低下し
、6以下では上昇している。pH=4.8のとき処理水
のpHは7〜8となってpHの上昇率が最大になり、更
に処理水CODも最も低い結果が得られた。 なお、中和処理を施さない場合は、処理水質がCOD 
9Hmg/見から次第に恵化し遂には2825@g/文
になった。また、原水pH−11,3の場合には、処理
水がpHな7前後に低下するが、流動床内の液粘度が上
昇し遂にはゼリー状となった。 以上の実験結果から処Fllへの4入前の原水の指摘p
H値は5前後であると決定できる。 原水のpHを5に調整して通液し処理したところ所期の
結果が得られた。 実験例2 前記実施例1の流動床接触酸化装置から得られた処理水
を原水としてPR調節しておき、これを天然轢固定床接
触酩化装置で生物処理試験した結果は以下の如く〒あっ
た。 原水二・BOD745脂gel、COD573mg/4
1゜処理条件 礫瀉床部容810.51. i1!充填率55%空気1
k  12.5 mfi/sin (80m’/BOD
 kg)、 滞留時間30 h 2段以陣の処理水のpoは処Jf前より上昇しpH81
iII後に収斂するので指摘pHの検索は焦意味である
。従って処理水中のCODを短時間で計測できるCOD
計を検出器として検出し、COD仙を蔽小にするpHを
指摘pHとするのがよい。 大発明においては1段及び2段以上の場合も計算機制御
により上記至適P)Iに基いてフィードフォワード’ 
aj制御することによって一層効果を発揮できる。 なお、本発明は培養法による有用化合物の生産の場合に
も適用できる。
[1g1 sentence]. When the raw water pH is 6 or more, the pH of the treated water decreases, and when the pH is 6 or less, it increases. When pH=4.8, the pH of the treated water was 7 to 8, the rate of increase in pH was the highest, and the COD of the treated water was also the lowest. In addition, if neutralization treatment is not performed, the treated water quality will be COD.
It gradually improved from 9Hmg/view to 2825@g/text. In addition, in the case of raw water pH -11.3, the pH of the treated water decreased to around 7, but the liquid viscosity in the fluidized bed increased and finally became jelly-like. Based on the above experimental results, it is pointed out that the raw water before entering the treatment Fll is
The H value can be determined to be around 5. When the pH of the raw water was adjusted to 5 and the solution was passed through the solution, the desired results were obtained. Experimental Example 2 The treated water obtained from the fluidized bed catalytic oxidation device of Example 1 was subjected to PR adjustment as raw water, and it was subjected to a biological treatment test using a natural road fixed bed catalytic drunkenning device.The results were as follows. Ta. Raw water 2, BOD745 fat gel, COD573mg/4
1゜Processing conditions Gravel bed volume 810.51. i1! Filling rate 55% air 1
k 12.5 mfi/sin (80m'/BOD
kg), residence time 30 h The po of the treated water in the second stage increased from before the treatment and reached pH 81.
Since it converges after iII, the search for the indicated pH is a focal point. Therefore, COD that can measure COD in treated water in a short time
It is preferable to use a meter as a detector to detect the pH, and set the pH at which the COD value is suppressed as the indicated pH. In the great invention, even in the case of one stage and two or more stages, feed forward' is based on the above optimal P)I by computer control.
By controlling aj, the effect can be further improved. Note that the present invention can also be applied to the production of useful compounds by culture methods.

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

図は未発り1実験例における原水pHと処理水pHとの
関係及びCODの変化を示すグラフである。
The figure is a graph showing the relationship between the pH of raw water and the pH of treated water and the change in COD in one experimental example.

Claims (2)

【特許請求の範囲】[Claims] (1)生物学的廃水処理において、原水のpHに対して
処理水のpHが高くなる範囲内で、pH上昇率が最大と
なる原水のpHを至適pHとして処理装置に導入する以
前に調整して通液することを特徴とする廃水の処理方法
(1) In biological wastewater treatment, within the range where the pH of the treated water is higher than the pH of the raw water, the pH of the raw water where the pH increase rate is the highest is set as the optimal pH and adjusted before introducing it into the treatment equipment. A wastewater treatment method characterized by passing the liquid through the wastewater.
(2)処理槽を多段に分割して行う生物学的廃水処理に
おいて、第1段においては原水のpHに対して処理水の
pHが高くなる範囲内でpH上昇率が最大となる原水の
pHを至適pHとして処理装置に導入する以前に調整し
て通液し、第2段以降においては処理水のCOD値が最
小となるpHに調整して通液することを特徴とする廃水
の処理方法。
(2) In biological wastewater treatment performed by dividing the treatment tank into multiple stages, in the first stage, the pH of the raw water is adjusted to the maximum pH increase rate within the range where the pH of the treated water is higher than the pH of the raw water. A wastewater treatment method characterized by adjusting the pH to an optimum pH before introducing the wastewater into a treatment device and passing the solution through the process, and adjusting the pH to a pH that minimizes the COD value of the treated water in the second and subsequent stages. Method.
JP59182781A 1984-09-03 1984-09-03 Treatment of waste water Granted JPS6161694A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59182781A JPS6161694A (en) 1984-09-03 1984-09-03 Treatment of waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59182781A JPS6161694A (en) 1984-09-03 1984-09-03 Treatment of waste water

Publications (2)

Publication Number Publication Date
JPS6161694A true JPS6161694A (en) 1986-03-29
JPH0157638B2 JPH0157638B2 (en) 1989-12-06

Family

ID=16124305

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59182781A Granted JPS6161694A (en) 1984-09-03 1984-09-03 Treatment of waste water

Country Status (1)

Country Link
JP (1) JPS6161694A (en)

Also Published As

Publication number Publication date
JPH0157638B2 (en) 1989-12-06

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Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term