JPH0347158B2 - - Google Patents
Info
- Publication number
- JPH0347158B2 JPH0347158B2 JP12734986A JP12734986A JPH0347158B2 JP H0347158 B2 JPH0347158 B2 JP H0347158B2 JP 12734986 A JP12734986 A JP 12734986A JP 12734986 A JP12734986 A JP 12734986A JP H0347158 B2 JPH0347158 B2 JP H0347158B2
- Authority
- JP
- Japan
- Prior art keywords
- wastewater
- anaerobic reactor
- inflow
- reactor
- anaerobic
- 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.)
- Expired - Lifetime
Links
- 239000002351 wastewater Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 230000007423 decrease Effects 0.000 claims description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- 241000894006 Bacteria Species 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 244000005700 microbiome Species 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 150000007524 organic acids Chemical class 0.000 description 3
- 235000005985 organic acids Nutrition 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は下水や産業廃水を微生物を利用して浄
化する水処理装置の流入負荷分配制御装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to an inflow load distribution control device for a water treatment system that purifies sewage or industrial wastewater using microorganisms.
(従来の技術)
下水や産業廃水などの有機性廃水は活性汚泥や
嫌気性微生物などの微生物の作用によつて浄化さ
れる。特に近年では嫌気性微生物を利用した嫌気
性処理が省エネルギーの観点から注目されてい
る。(Prior Art) Organic wastewater such as sewage and industrial wastewater is purified by the action of microorganisms such as activated sludge and anaerobic microorganisms. Particularly in recent years, anaerobic treatment using anaerobic microorganisms has attracted attention from the viewpoint of energy conservation.
この嫌気性処理法は、嫌気性微生物の働きで有
機物を分解処理する方法であり、有機性廃水中の
炭水化物、脂肪、タンパク質を主に揮発性有機酸
に分解する液化過程と、揮発性有機酸を主に炭酸
ガスとメタンに分解するガス化過程の二段階の反
応から構成されている。液化反応を行なわせる細
菌は酸生成菌、ガス化過程を行なわせる細菌はメ
タン菌と呼ばれる。このように嫌気性処理ではメ
タンを50〜70%含む発酵ガスが得られ、その有効
利用を図ることによつて、省エネルギー化が進め
られる。 This anaerobic treatment method decomposes organic matter using the action of anaerobic microorganisms. It mainly consists of a two-step gasification process in which carbon dioxide is decomposed into carbon dioxide and methane. Bacteria that perform the liquefaction reaction are called acid-producing bacteria, and bacteria that perform the gasification process are called methane bacteria. In this way, anaerobic treatment yields fermentation gas containing 50 to 70% methane, and by utilizing it effectively, energy conservation can be promoted.
このような水処理システムでは特に下水処理の
ように多量の廃水を浄化するような場合は、複数
のリアクタを持つ構成が一般的である。従来この
ような水処理システムでは複数のリアクタへの流
入廃水量が均等になるように制御されていた。こ
の従来例では運転管理が非常に容易である反面、
次のような欠点があつた。すなわち、微生物は何
らかの原因で浄化能力が低下することがあり、こ
れは現在の技術では避けられない。浄化能力が低
下した場合には流入負荷を軽減させる運転管理を
行ない、さらに浄化能力のより一層の低下を防止
する必要がある。しかし複数のリアクタへ流入廃
水量を均等に分配する従来例ではこのような対処
ができなかつた。このため、何らかの原因で浄化
能力が低下したリアクタではさらに浄化能力が低
下し、処理水質が悪化する。 In such water treatment systems, a configuration having a plurality of reactors is common, especially when purifying a large amount of wastewater such as in sewage treatment. Conventionally, in such water treatment systems, the amount of wastewater flowing into a plurality of reactors is controlled to be equal. In this conventional example, operation management is very easy, but on the other hand,
It had the following shortcomings: That is, the purification ability of microorganisms may decrease for some reason, and this cannot be avoided with current technology. When the purification capacity decreases, it is necessary to carry out operational management to reduce the inflow load and further prevent the purification capacity from further decreasing. However, in the conventional example where the amount of inflowing wastewater is evenly distributed to multiple reactors, such measures cannot be taken. For this reason, in a reactor whose purification ability has decreased for some reason, the purification ability is further decreased and the quality of the treated water deteriorates.
(発明が解決しようとする問題点)
すなわち、リアクタへの流入廃水量を制御でき
ず、浄化能力の低下による処理水質の悪化が生じ
ることがあつた。(Problems to be Solved by the Invention) In other words, the amount of wastewater flowing into the reactor could not be controlled, and the quality of treated water sometimes deteriorated due to a decrease in purification ability.
したがつて、本発明の目的は、嫌気性リアクタ
内の高さ方向のPH分布から嫌気性リアクタの処理
能力をとらえ、この処理能力に応じて流入廃水量
を制御するようにして、常に良好な処理水が得ら
れるようにした水処理装置の流入負荷分配制御装
置を提供することにある。 Therefore, the purpose of the present invention is to grasp the processing capacity of the anaerobic reactor from the PH distribution in the height direction within the anaerobic reactor, and to control the amount of inflow wastewater according to this processing capacity, so as to always maintain a good condition. An object of the present invention is to provide an inflow load distribution control device for a water treatment device that allows treated water to be obtained.
(問題点を解決するための手段)
本発明は廃水流入管路から分岐された複数の流
入管路毎にそれぞれ嫌気性リアクタを設けた水処
理装置の流入負荷分配制御装置に関するもので、
前記廃水流入管路に流れる廃水の流量を測定する
流量計を設けると共に、前記各嫌気性リアクタ毎
にその内部の高さ方向のPH分布をそれぞれ測定す
るPH計を設ける。また演算装置として、これら各
PH計の測定値を入力し各嫌気性リアクタ毎にその
処理能力としてPH値が低下し始める高さをそれぞ
れ求める手段と、各嫌気性リアクタ毎に求められ
た処理能力に応じて前記廃水流入管路に流れる流
入廃水の、各嫌気性リアクタに対する分配量を決
定する手段とを持つものを用いる。
(Means for Solving the Problems) The present invention relates to an inflow load distribution control device for a water treatment device in which an anaerobic reactor is provided for each of a plurality of inflow pipes branched from a wastewater inflow pipe.
A flow meter is provided to measure the flow rate of wastewater flowing into the wastewater inflow pipe, and a PH meter is provided for each of the anaerobic reactors to measure the PH distribution in the height direction inside the reactor. In addition, each of these
A means for inputting the measured value of the PH meter and determining the height at which the PH value starts to decrease as the processing capacity for each anaerobic reactor, and a means for determining the height at which the PH value starts to decrease as the processing capacity of each anaerobic reactor, and the wastewater inflow pipe according to the processing capacity determined for each anaerobic reactor. A device having means for determining the amount of inflow wastewater flowing into the anaerobic reactor to be distributed to each anaerobic reactor is used.
(作用)
本発明では、各嫌気性リアクタ内に設置された
PH計によつて、リアクタ高さ方向のPH分布を測定
しこれによつて各嫌気性リアクタの処理能力を演
算する。すなわち、廃水中の有機物はまず酸生成
菌の作用によつて揮発性有機酸に分解される。こ
のため嫌気性リアクタの廃水流入口近傍ではPHが
小さく、処理水出口に向つて揮発性有機酸がメタ
ン、炭酸ガスに分解されるため徐々にPHが高くな
る。この場合PHが小さい領域が広いと揮発性有機
酸が充分にガス化されないまま嫌気性リアクタか
ら流出することがある。このようにリアクタ高さ
方向のPH分布によつて嫌気性リアクタの処理能力
を演算し、次いで処理能力に応じて各嫌気性リア
クタに対する流入廃水を分配する。(Function) In the present invention, the
The PH distribution in the height direction of the reactor is measured using a PH meter, and the processing capacity of each anaerobic reactor is calculated from this. That is, organic matter in wastewater is first decomposed into volatile organic acids by the action of acid-producing bacteria. Therefore, the PH is low near the wastewater inlet of the anaerobic reactor, and gradually increases toward the treated water outlet as volatile organic acids are decomposed into methane and carbon dioxide gas. In this case, if the region with low pH is wide, volatile organic acids may flow out of the anaerobic reactor without being sufficiently gasified. In this way, the processing capacity of the anaerobic reactor is calculated based on the PH distribution in the height direction of the reactor, and then the inflow wastewater to each anaerobic reactor is distributed according to the processing capacity.
(実施例)
第1図は本発明の一実施例を示すもので、n個
の嫌気性リアクタ6a,6b,…,6nからなる
水処理施設の概略ブロツク図である。(Embodiment) FIG. 1 shows an embodiment of the present invention, and is a schematic block diagram of a water treatment facility consisting of n anaerobic reactors 6a, 6b, . . . , 6n.
図において、廃水流入管路1にはポンプ2およ
び流量計3が設置されており、この流量計3によ
つて流入廃水の流量が測定される。また分岐され
た各廃水流入管路1a,1b,…,1nには流量
計5a,5b,…,5nが設置されており、これ
らによつて各嫌気性リアクタ6a,6b,…,6
nに流入される廃水量がそれぞれ測定される。さ
らに各廃水流入管路1a,1b,…,1nには、
それぞれ調節バルブ4a,4b,…,4nが設け
られ、対応するリアクタ6a,6b,…,6nへ
の流入廃水量を所望の値に調節する。これら各リ
アクタ6a,6b,…,6nの流出側には処理水
管路10a,10b,…,10nが連結されてお
り、図示しない後圧のプロセスに連結される。ま
た、各リアクタ6a,6b,…,6n内にはPH計
7a,7b,…,7nをそれぞれ設け対応するリ
アクタ6a,6b,…,6n内のたて方向のPH分
布を測定する。各リアクタ6a,6b,…,6n
からは発酵ガスが生じるが、これらはガス管路に
よつて図示しないガスタンクに導びかれ、熱源用
の燃料等に用いられる。9は演算装置で、前述し
た流量計3および各PH計7a,7b,…,7nに
よる各測定信号を入力し、後述する演算手法によ
り、分岐された各廃水流入管路1a,1b,…,
1nの流入廃水量を決定する。8a,8b,…,
8nは流量調節装置で、各廃水流入管路1a,1
b,…,1n毎に設けられ、前記演算装置9にて
求められた流入廃水量を得るべく、対応する流量
計5a,5b,…,5nの値を入力しながら、対
応する調節バルブ4a,4b,…,4nの開度調
節を行なう。 In the figure, a pump 2 and a flowmeter 3 are installed in a wastewater inflow pipe 1, and the flowmeter 3 measures the flow rate of inflowing wastewater. In addition, flow meters 5a, 5b,..., 5n are installed in each of the branched wastewater inflow pipes 1a, 1b,..., 1n, and these flow meters 5a, 5b,..., 6n to each anaerobic reactor 6a, 6b,..., 6.
The amount of wastewater flowing into each of the n is measured. Furthermore, in each wastewater inflow pipe 1a, 1b,..., 1n,
Control valves 4a, 4b, . . . , 4n are provided, respectively, to adjust the amount of wastewater flowing into the corresponding reactors 6a, 6b, . . . , 6n to a desired value. Treated water pipes 10a, 10b, . . . , 10n are connected to the outflow side of each of these reactors 6a, 6b, . Further, PH meters 7a, 7b, . . . , 7n are provided in each of the reactors 6a, 6b, . Each reactor 6a, 6b,..., 6n
Fermentation gas is generated from the tank, which is led to a gas tank (not shown) through a gas pipe and is used as fuel for a heat source. Reference numeral 9 denotes a calculation device which inputs each measurement signal from the flow meter 3 and each PH meter 7a, 7b, .
Determine the amount of influent wastewater of 1n. 8a, 8b,...,
8n is a flow rate adjustment device, and each wastewater inflow pipe 1a, 1
b, ..., 1n, and in order to obtain the amount of inflow wastewater determined by the arithmetic unit 9, while inputting the values of the corresponding flowmeters 5a, 5b, ..., 5n, the corresponding control valves 4a, 5n are operated. Adjust the opening of 4b,..., 4n.
ここで各嫌気性リアクタ6a,6b,…,6n
内に設置されたPH計7a,7b,…,7nは、前
述のように対応するリアクタ6a,6b,…,6
n内の高さ方向のPH分布を測定する。この場合、
PH計は1つの嫌気性リアクタ内に複数個設置して
もよく、あるいは1つのPH計を上下方向に移動し
て測定してもよい。処理が良好に行われている場
合には第2図aに示すようにリアクタ内のPH分布
はほとんど見られないが、メタン菌の処理能力が
低下したり、流入負荷が大きすぎた場合には、第
2図b,cで示す如く、リアクタ下部からPHが
徐々に低下していく。従つて、PHが低下しはじめ
るリアクタ高さによつて嫌気性リアクタの処理能
力を評価することができる。演算装置9には各PH
計7a,7b,…,7nの信号が入力されてお
り、予め設定したリアクタ内高さ毎の設定値と比
較し、PHが低下しはじめるリアクタ高さをそれぞ
れ求める。このPHが低下し始める高さによつて各
嫌気性リアクタ6a,6b,…,6nの処理能力
が判断される。次にこの結果によつて各嫌気性リ
アクタ6a,6b,…,6nごとに流入廃水量を
分配する分配率w1,w2,…woを演算する。この
分配率を演算する方法の一例として次式を示す。 Here, each anaerobic reactor 6a, 6b,..., 6n
The PH meters 7a, 7b, ..., 7n installed inside the reactors 6a, 6b, ..., 6 correspond to
Measure the PH distribution in the height direction within n. in this case,
A plurality of PH meters may be installed in one anaerobic reactor, or one PH meter may be moved vertically for measurement. When the treatment is carried out well, there is almost no PH distribution within the reactor as shown in Figure 2a, but if the treatment capacity of methane bacteria decreases or the inflow load is too large, , as shown in Figure 2 b and c, the pH gradually decreases from the bottom of the reactor. Therefore, the processing capacity of an anaerobic reactor can be evaluated based on the height of the reactor at which the PH begins to decrease. The calculation unit 9 has each PH
A total of 7a, 7b, . . . , 7n signals are inputted, and are compared with preset values for each height inside the reactor to determine the reactor height at which the PH starts to decrease. The processing capacity of each anaerobic reactor 6a, 6b, . . . , 6n is determined based on the height at which the pH starts to decrease. Next, based on this result, distribution ratios w 1 , w 2 , . The following equation is shown as an example of a method for calculating this distribution ratio.
w1=H1/H1+H2+…+Ho
w2=H2/H1+H2+…+Ho
〓
wo=Ho/H1+H2+…+Ho
ここで
w1〜o:分配率
H1〜o:PHが低下しはじめるリアクタ高さ(リア
クタ頂部からの高さ)
次に上記分配率wと廃水流入管路1に設置され
ている流量計3の出力QTとにより、次式に従つ
て各嫌気性リアクタ流入廃水量の目標値Q1,Q2
…,Qoを演算する。 w 1 =H 1 /H 1 +H 2 +…+H o w 2 =H 2 /H 1 +H 2 +…+H o 〓 w o =H o /H 1 +H 2 +…+H o where w 1~o : Distribution ratio H1 ~o : Reactor height at which PH starts to decrease (height from the top of the reactor) Next, based on the above distribution ratio w and the output Q T of the flow meter 3 installed in the wastewater inflow pipe 1, Target values Q 1 , Q 2 for the amount of wastewater flowing into each anaerobic reactor according to the following formula:
..., calculate Q o .
Q1=w1×QT
Q2=w2×QT
〓 〓
Qo=wo×QT
このようにして求めた流入廃水量の目標値Q1,
Q2…,Qoは各調節装置8a,8b,…,8nに
出力され、目標値になるように廃水流入管路1
a,1b,…,1nに設置されているバルブ4
a,4b,…,4nの開度が調節される。 Q 1 =w 1 ×Q T Q 2 =w 2 ×Q T 〓 〓 Q o =w o × Q TTarget value of inflow wastewater amount obtained in this way Q 1 ,
Q 2 ..., Q o are output to each regulating device 8a, 8b, ..., 8n, and the wastewater inflow pipe 1 is adjusted so that the target value is achieved.
Valve 4 installed at a, 1b, ..., 1n
The opening degrees of a, 4b,..., 4n are adjusted.
なお、上記実施例では上向流型のリアクタにつ
いて説明したが、上向流型に限られるものではな
く、下向流型のリアクタにも同様に適用できる。 In addition, although the above-mentioned example explained an upward flow type reactor, it is not limited to an upward flow type, and can be similarly applied to a downward flow type reactor.
以上述べたように本発明によれば嫌気性リアク
タの処理能力に応じて流入廃水量を制御すること
ができるので、常に良好な処理水を得ることがで
き、水処理施設を安定に運転管理することができ
る。また処理能力を、嫌気性リアクタ内のPHを測
定することによつて判断しているので、嫌気性リ
アクタの処理能力を直接的に把握でき、高精度の
制御を行なうことができる。
As described above, according to the present invention, the amount of inflowing wastewater can be controlled according to the processing capacity of the anaerobic reactor, so that good quality treated water can be obtained at all times, and water treatment facilities can be operated and managed in a stable manner. be able to. Furthermore, since the processing capacity is determined by measuring the pH inside the anaerobic reactor, the processing capacity of the anaerobic reactor can be directly grasped and highly accurate control can be performed.
第1図は本発明による水処理装置の流入負荷分
配制御装置の一実施例を示す概略ブロツク図、第
2図a,b,cは嫌気性リアクタ高さ方向のPH分
布を示す特性図である。
3……流量計、4a,4b,〜,4n……バル
ブ、5a,5b,〜,5n……流量計、6a,6
b,〜,6n……嫌気性リアクタ、7a,7b,
〜,7n……PH計、8a,8b,〜,8n……調
節装置、9……演算装置。
Fig. 1 is a schematic block diagram showing an embodiment of the inflow load distribution control device for a water treatment equipment according to the present invention, and Fig. 2 a, b, and c are characteristic diagrams showing the PH distribution in the height direction of the anaerobic reactor. . 3...Flowmeter, 4a, 4b, ~, 4n...Valve, 5a, 5b, ~, 5n...Flowmeter, 6a, 6
b, ~, 6n...anaerobic reactor, 7a, 7b,
~, 7n... PH meter, 8a, 8b, ~, 8n... Adjustment device, 9... Arithmetic device.
Claims (1)
毎にそれぞれ嫌気性リアクタを設けた水処理装置
の流入負荷分配制御装置において、 前記廃水流入管路に流れる廃水の流量を測定す
る流量計と、 前記各嫌気性リアクタ毎に設けられその内部の
高さ方向のPH分布をそれぞれ測定するPH計とを備
え、 これら各PH計の測定値を入力し各嫌気性リアク
タ毎にその処理能力としてPH値が低下し始める高
さをそれぞれ求める手段と、 各嫌気性リアクタ毎に求められた処理能力に応
じて前記廃水流入管路に流れる流入廃水の、各嫌
気性リアクタに対する分配量を決定する手段とを
有する演算装置、 を設けたことを特徴とする水処理装置の流入負荷
分配制御装置。[Scope of Claims] 1. In an inflow load distribution control device for a water treatment device in which each of a plurality of inflow pipes branched from a wastewater inflow pipe is provided with an anaerobic reactor, the flow rate of wastewater flowing into the wastewater inflow pipe is The system is equipped with a flow meter that measures the pH distribution of each anaerobic reactor, and a PH meter that is installed in each of the anaerobic reactors and measures the PH distribution in the height direction inside each anaerobic reactor. means for determining the height at which the PH value begins to decrease as a treatment capacity, and distribution of inflow wastewater flowing into the wastewater inflow pipe to each anaerobic reactor according to the treatment capacity determined for each anaerobic reactor. An inflow load distribution control device for a water treatment device, comprising: a calculation device having means for determining an amount.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61127349A JPS62286592A (en) | 1986-06-03 | 1986-06-03 | Apparatus for distribution control of inflow load of water treatment plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61127349A JPS62286592A (en) | 1986-06-03 | 1986-06-03 | Apparatus for distribution control of inflow load of water treatment plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62286592A JPS62286592A (en) | 1987-12-12 |
| JPH0347158B2 true JPH0347158B2 (en) | 1991-07-18 |
Family
ID=14957728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61127349A Granted JPS62286592A (en) | 1986-06-03 | 1986-06-03 | Apparatus for distribution control of inflow load of water treatment plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62286592A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NO307823B1 (en) * | 1998-12-23 | 2000-06-05 | Norsk Hydro As | Process for the treatment of organic matter |
-
1986
- 1986-06-03 JP JP61127349A patent/JPS62286592A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62286592A (en) | 1987-12-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |