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JP4354468B2 - Water splitting method and water splitting device - Google Patents
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JP4354468B2 - Water splitting method and water splitting device - Google Patents

Water splitting method and water splitting device Download PDF

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JP4354468B2
JP4354468B2 JP2006184575A JP2006184575A JP4354468B2 JP 4354468 B2 JP4354468 B2 JP 4354468B2 JP 2006184575 A JP2006184575 A JP 2006184575A JP 2006184575 A JP2006184575 A JP 2006184575A JP 4354468 B2 JP4354468 B2 JP 4354468B2
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water splitting
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孝雄 村上
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この発明は主として汚水処理、特にステップ流入多段硝化脱窒プロセスに付加して実施される分水方法とその方法において使用される分水装置に関するものである。   The present invention mainly relates to a sewage treatment, in particular, a water splitting method implemented in addition to a step inflow multistage nitrification denitrification process and a water splitting device used in the method.

下水処理においては高度処理の必要性がますます高くなってきている。このため、本件出願人においても、「ステップ流入多段硝化脱窒プロセス」をはじめ、様々な高度処理プロセスを開発してきた。   In sewage treatment, the need for advanced treatment is increasing. For this reason, the present applicant has also developed various advanced treatment processes including the “step inflow multi-stage nitrification denitrification process”.

「ステップ流入多段硝化脱窒プロセス」は多数の導入実績がある高性能な高度処理プロセスであるが、流入水を通常、均等に三分割して一段目から三段目までステップ流入させることを前提とした処理プロセスである。   The "step inflow multi-stage nitrification denitrification process" is a high-performance advanced treatment process that has been introduced in many cases. However, it is assumed that the inflow water is usually divided into three equal parts and step-in from the first stage to the third stage. It is a processing process.

特許第3718180号公報Japanese Patent No. 3718180

前記発明の実施において、実際の運転においては、分水槽において流量を堰高調整により二等分することはさほど難しくないが、これを均等に三分割することは容易でなく、また、仮に三等分されるように堰高を調整しても、流量の変動によって水位が変化すると、分割された流量にかなりの差が生じることが知られている。   In the practice of the invention, in actual operation, it is not so difficult to divide the flow rate into two equal parts by adjusting the weir height in the diversion tank, but it is not easy to divide the flow equally into three parts. Even if the weir height is adjusted so as to be divided, it is known that if the water level changes due to the fluctuation of the flow rate, there is a considerable difference in the divided flow rates.

ステップ流入多段硝化脱窒プロセスにおいては、流入水は均等に分割供給されるという前提の下に施設設計を行っているため、流入水が均等に分配されず、格段の無酸素槽や硝化槽のMLSS濃度や滞留時間が設定と異なる運転となった場合、窒素やりん除去に好ましくない影響が生じることが指摘されている。   In the step inflow multi-stage nitrification denitrification process, the facility design is based on the premise that the inflow water is divided and supplied evenly, so the inflow water is not evenly distributed. It has been pointed out that when the MLSS concentration and the residence time are different from the set operation, an undesirable effect on nitrogen and phosphorus removal occurs.

流入水量の均等分割については、センサによる計測と電動堰等による制御を行えば可能であるが、これは設置費とメンテナンス費が高くつくという問題がある。このため、流量変動にかかわらず、安定した三分割が可能な分水方法、装置の開発が望まれていた。   The equal division of the inflowing water amount can be performed by measuring with a sensor and controlling with an electric weir, but this has the problem of high installation costs and maintenance costs. For this reason, it has been desired to develop a water splitting method and apparatus capable of stable three divisions regardless of flow rate fluctuations.

この発明は、堰等により一旦、分割した流入水を更に等分割し、それを再度、合流させる方法によって、分割時における流量差を均等化する機能を有する分水およびその装置である。   The present invention is a water distribution and a device therefor having a function of equalizing a flow rate difference at the time of division by a method of further dividing the inflow water once divided by a weir or the like and then joining the divided water again.

図1にその原理を示す。図1において、まず、流入水は堰等により三分割される。(A部)その後、三分割された流入水は、更に堰等により各々二等分される。更に、二等分された各流入水を、再度、合流させる。合流後の3つの流れが最終的に三分割された流れである。   FIG. 1 shows the principle. In FIG. 1, first, inflow water is divided into three parts by a weir or the like. (Part A) Thereafter, the inflow water divided into three parts is further divided into two equal parts by a weir or the like. Further, the influent water divided into two equal parts is joined again. The three flows after the merge are finally divided into three.

すなわちこの発明の要旨は次の通りである。
流入水を堰類によって三分割し、次いでその三分割した流入水を更に二分割し、次いでその二分割した流入水をそれぞれ合流させ、合流後の3つの流れをそれぞれ水路に流入させる分水方法および水路の3ヵ所の越流堰類を通して3分割槽に流入水を三分割し、次いで各3分割槽の2ヶ所の越流堰類を通して各合流槽に流入水をそれぞれ合流させ、合流槽の越流堰類を通して各水路に流入させる分水装置である。
That is, the gist of the present invention is as follows.
Dividing the inflow water into three parts by the weirs, then dividing the three inflows into two parts, then joining the two parts of the inflowing water, respectively, and flowing the three flows after joining into the water channel respectively The influent water is divided into three divided tanks through three overflow dams in the water channel, and then the influent water is merged into each merging tank through two overflow dams in each three divided tank. It is a diversion device that flows into each water channel through overflow weirs.

この発明により、流入水量の三等分において、計測・制御装置や動力を用いず、水位変動に伴う流量の相互差を低減することが可能である。   According to the present invention, it is possible to reduce the mutual difference in flow rate due to the fluctuation of the water level without using a measurement / control device or power in the three equal parts of the inflowing water amount.

例として、合計30の流量を、10ずつに三分割するように堰高が調整されている場合を考える。しかしながら、水位の変動等の要因で実際の分割水量には大幅に差が生じ、a=13、b=11、c=6となったものとする。   As an example, let us consider a case where the weir height is adjusted so that a total of 30 flow rates are divided into three parts of 10. However, it is assumed that there is a large difference in the actual amount of split water due to factors such as fluctuations in the water level, and a = 13, b = 11, and c = 6.

これを各流量を二等分して、再度、合流させると、装置からの流出量は、表1に示す数値となる。表1に示されるように、この発明の装置による流量((1),(2),(3))は、流入時よりも相互の差が低減されていることがわかる。また、さらに誤差を低減するために、直列二段としたこの分水装置に前述の水量(a=13)を流入させた場合の流出量も併せて表1に示した。直列二段とした場合には、更に相互の差が低減され、均等分割に近い流量となっていることがわかる。   When this is divided into two equal parts and merged again, the outflow amount from the apparatus becomes the numerical value shown in Table 1. As shown in Table 1, it can be seen that the difference between the flow rates ((1), (2), (3)) by the apparatus of the present invention is smaller than that at the time of inflow. In addition, in order to further reduce the error, Table 1 also shows the outflow amount when the above-described water amount (a = 13) was introduced into this water splitting device in two stages in series. When two stages are connected in series, it is understood that the mutual difference is further reduced, and the flow rate is close to equal division.

Figure 0004354468
Figure 0004354468

以上の効果により、ステップ流入多段硝化・脱窒プロセス設計における前提条件において運転することが可能となり、安定かつ良好な窒素・りん除去が可能となる。   With the above effects, it is possible to operate under the preconditions in the step inflow multi-stage nitrification / denitrification process design, and stable and good nitrogen / phosphorus removal is possible.

この発明による分水装置の用途は下水処理分野に限定されるものでなく、流量分配の目的に広く利用可能である。さらにこの発明は、四分割以上の分割への適用も可能である。
さらに、この発明の原理の数学的根拠について以下に説明する。
The use of the water separator according to the present invention is not limited to the field of sewage treatment, and can be widely used for the purpose of flow distribution. Furthermore, the present invention can be applied to four or more divisions.
Further, the mathematical basis of the principle of the present invention will be described below.

三つの数値があり、その値はいづれもxである。これが、それぞれa,b,cは正または負の値をとり、変化量の合計はゼロとする。(a+b+c=0)
変化後の値は、それぞれ、x+a,x+b,x+cである。
この三つの数値を、二等分すると;
There are three numbers, all of which are x. In this case, a, b, and c each take a positive or negative value, and the total amount of change is zero. (a + b + c = 0)
The changed values are x + a, x + b, and x + c, respectively.
Dividing these three numbers into two equal parts;

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

(1),(2),(3)を2項ずつ組み合わせると   Combining (1), (2), and (3) by two terms

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

ここで、仮定からa+b+c=0であるから、   Here, since a + b + c = 0 from the assumption,

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

(7),(8),(9)をそれぞれ(4),(5),(6)に代入すると   Substituting (7), (8), and (9) into (4), (5), and (6), respectively

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

Figure 0004354468
Figure 0004354468

ここで、   here,

Figure 0004354468
Figure 0004354468

よって、(10),(11),(12)の変化量は、x+a,x+b,x+cの変化量a,b,cよりも小さい。   Therefore, the change amounts of (10), (11), and (12) are smaller than the change amounts a, b, and c of x + a, x + b, and x + c.

以下、この発明を開示した実施形態に基づいて説明する。図2〜4に示す分水用装置は矩形をなし、水路1は開水路、管路からなり、その水路1に所要間隔をもって第一越流堰類2が第一貯槽3に向かって開口している。   Hereinafter, the present invention will be described based on disclosed embodiments. The water diversion device shown in FIGS. 2 to 4 has a rectangular shape, the water channel 1 is composed of an open channel and a pipe, and the first overflow weirs 2 open toward the first storage tank 3 with a required interval in the water channel 1. ing.

この第一越流堰類2は固定堰、可動堰、オリフィス等で形成することができる。
各第一貯槽3には第二貯槽4に向かって開口している一対の第二越流堰類2が開口している。また第二貯槽4には所要の各水路、例えば汚水処理槽へのステップに第三越流堰類2が開口している。
The first overflow weir 2 can be formed of a fixed weir, a movable weir, an orifice, or the like.
Each first storage tank 3 has a pair of second overflow weirs 2 that open toward the second storage tank 4. In the second storage tank 4, third overflow weirs 2 are opened at required water channels, for example, steps to a sewage treatment tank.

図5に示す分水装置は円形を成し、中央部に水路2があり、その周辺に第一貯槽3が配置され、その外側に第二貯槽4が配置され、水路2と第一貯槽3および第一貯槽3と第二貯槽と第二貯槽3との間に越流堰類2が開口している。   The water diverter shown in FIG. 5 has a circular shape, and has a water channel 2 at the center, a first storage tank 3 is disposed in the periphery thereof, a second storage tank 4 is disposed on the outside thereof, and the water channel 2 and the first storage tank 3. The overflow weirs 2 are opened between the first storage tank 3, the second storage tank, and the second storage tank 3.

図6はこの発明の方法、装置を実施するステップ流入多段硝化脱窒プロセスの方法とその配置状態を示したもので、複数段の脱窒タンクB、硝化タンクCを直列に配置し原水をこの発明の分水装置Aを通して各脱窒タンクBへ等配分し、各段の固形物量が等しくなるようにタンク容量を設け、エアリフトによる混合液の内部循環Dがなされる最終沈殿池Eから返送汚泥が返送される。   FIG. 6 shows the method and arrangement of the step inflow multi-stage nitrification denitrification process in which the method and apparatus of the present invention are implemented. A plurality of stages of denitrification tank B and nitrification tank C are arranged in series, and the raw water is supplied to this stage. Equally distributed to each denitrification tank B through the water diverter A of the invention, provided with tank capacity so that the amount of solids at each stage is equal, and returned sludge from the final sedimentation basin E where the internal circulation D of the liquid mixture by air lift is made Will be returned.

分水装置Aの第二貯槽4の越流堰類2を通った水流は流水路5を通じて各脱窒タンクBに排水される。そしてステップ流入多段硝化脱窒法では流入水量が均等に分割されないと各段の汚泥濃度が変化するため、各段の固形物量が等しいという設計上の前提通りの運転ができなくなる問題をこの発明は解消できる。   The water flow that has passed through the overflow weirs 2 of the second storage tank 4 of the water diverter A is drained into the denitrification tanks B through the flow channels 5. And, in the step inflow multi-stage nitrification denitrification method, if the inflow water amount is not divided equally, the sludge concentration in each stage will change, so this invention solves the problem that the solid amount of each stage is not equal to the design assumption it can.

この発明の概要を図解したものである。The outline of the present invention is illustrated. この発明の装置の配置状態を示した平面図である。It is the top view which showed the arrangement | positioning state of the apparatus of this invention. 図2のI−I断面図である。It is II sectional drawing of FIG. 図2のII−II断面図である。It is II-II sectional drawing of FIG. この発明の他の実施例の概要を示した平面図である。It is the top view which showed the outline | summary of the other Example of this invention. この発明の装置を使用した下水処理状態の概要図である。It is a schematic diagram of the state of a sewage treatment using the apparatus of this invention.

符号の説明Explanation of symbols

1…水路 A…分水装置
2…越流堰類 B…脱窒タンク
3…第一貯槽 C…硝化タンク
4…第二貯槽 D…内部循環
5…水路 E…最終沈殿池
F…返送汚泥


DESCRIPTION OF SYMBOLS 1 ... Water channel A ... Divider 2 ... Overflow weir B ... Denitrification tank 3 ... First storage tank C ... Nitrification tank 4 ... Second storage tank D ... Internal circulation 5 ... Water channel E ... Final sedimentation tank
F ... Return sludge


Claims (2)

流入水を堰類によって三分割し、次いでその三分割した流入水を二分割し、次いでその二分割した流入水をそれぞれ合流させ、合流後の3つの流れをそれぞれ各水路に流入させることを特徴とする分水方法。   The inflowing water is divided into three parts by weirs, then the three parts of the inflowing water are divided into two parts, then the two divided inflowing waters are joined together, and the three flows after joining are each flowed into each water channel Water splitting method. 水路の3ヶ所の越流堰類を通して3分割槽に流入水を三分割し、次いで各3分割槽の2ヶ所の越流堰類を通して各合流槽に流入水をそれぞれ合流させ、合流槽の越流堰類を通して各水路に流入させることを特徴とする分水装置。


























The influent water is divided into three division tanks through the three overflow weirs in the waterway, and then the inflow water is merged into each merge tank through the two overflow weirs in each three division tank. A water diverter characterized by flowing into each water channel through flow weirs.


























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