KR101031191B1 - Sludge cohesion apparatus - Google Patents

Sludge cohesion apparatus Download PDF

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KR101031191B1
KR101031191B1 KR1020100073734A KR20100073734A KR101031191B1 KR 101031191 B1 KR101031191 B1 KR 101031191B1 KR 1020100073734 A KR1020100073734 A KR 1020100073734A KR 20100073734 A KR20100073734 A KR 20100073734A KR 101031191 B1 KR101031191 B1 KR 101031191B1
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South Korea
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clock
sludge
venturi tube
polymer coagulant
tube
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KR1020100073734A
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Korean (ko)
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조영호
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조영호
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3123—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20—Measuring; Control or regulation
    • B01F35/22—Control or regulation
    • B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
    • B01F35/2211—Amount of delivered fluid during a period
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56—Macromolecular compounds

Abstract

PURPOSE: A sludge cohesion apparatus is provided to improve the sludge treatment amount since polymer coagulants are not injected. CONSTITUTION: A sludge cohesion apparatus comprises a first venturi tube(210), a mixing tube(212), a second venturi tube(220) and a stirring tank(231). The first venturi tube receives polymer coagulants and sludge and increase a flow rate. The mixing tube is installed at an outlet of the first venturi tube and mixes polymer coagulants and sludge by generating cavitation. The second venturi tube is installed at an outlet of the mixing tube. The stirring tank occurs cavitation by receiving the mixed solution flowing out from the second venturi tube and discharges the polymer coagulants and sludge.

Description

소화슬러지 응집장치{Sludge cohesion apparatus}Sludge cohesion apparatus

본 발명은 소화슬러지 응집장치에 관한 것으로, 보다 상세하게는 소화 슬러지(Digested Sludge)와 고분자 응집제를 함께 슬러지 혼합장치에 투입한 후 혼합 및 교반하여 플록(floc)으로 만들 때에 상기 혼합과정에서 배관 내의 속도를 높여 난류와 캐비테이션을 유발시킴으로써 고분자 응집제와 소화슬러지를 골고루 혼합시켜 플록을 형성하는 한편, 고분자 응집제의 투입량을 대폭 절감할 수 있는 소화슬러지 응집장치에 관한 것이다.
The present invention relates to a digested sludge flocculating apparatus, and more particularly, to digested sludge and a polymer flocculant together into a sludge mixing apparatus, followed by mixing and stirring to form flocs in the pipe during the mixing process. By increasing the speed and causing turbulence and cavitation, the present invention relates to a fired sludge flocculation device that can form a floc by mixing the polymer flocculant and the digested sludge evenly, while significantly reducing the amount of the polymer flocculant.

생활수준이 향상됨에 따라 생활하수의 배출도 급증하고 있어 이를 효율적으로 처리하는 것이 환경정책의 주요 과제로 대두되고 있다. 한편, 하수슬러지 처리방법은 전처리단계, 중간처리단계 및 최종처리단계로 구분할 수 있는 바, 이 중 전처리단계는 하수슬러지를 농축, 소화 및 탈수하는 단계로서 하수슬러지의 처리효율을 향상시키고 감량시키는 것이다. As the standard of living improves, the discharge of domestic sewage is also rapidly increasing, and the efficient treatment of this is becoming a major task of environmental policy. Meanwhile, the sewage sludge treatment method can be divided into pretreatment stage, intermediate treatment stage and final treatment stage, among which pretreatment stage is to concentrate, digest and dehydrate sewage sludge to improve and reduce the treatment efficiency of sewage sludge. .

현재 하수슬러지의 전처리방법은 혐기성 중온에서 고온 소화(50∼55℃)로 전환되고 있는 바, 그 과정에서 소화슬러지의 ph는 8.5∼8.9까지 치솟아 강산성이므로 탈수와 더불어 산가를 낮출 필요가 있고 따라서 탈수약품의 사용량이 급증하고 있다. At present, the pretreatment method of sewage sludge is converted to anaerobic high temperature digestion (50 ~ 55 ℃). In the process, the pH of digested sludge is soaring up to 8.5 ~ 8.9, so it is necessary to lower acid value along with dehydration. The use of dehydrating drugs is skyrocketing.

상기 탈수약품은 분말 약품을 물에 용해시킨 농도 0.2%의 고분자응집제로서 소화슬러지를 플럭으로 전환시키기 위하여 관련업계에서 흔히 사용되고 있다. The dehydrating agent is a polymer coagulant having a concentration of 0.2% in which a powdered drug is dissolved in water, and is commonly used in the related art to convert digested sludge into floc.

고분자응집제가 탈수 및 응집하는 원리는 아래와 같다. 즉, 도 1에서 보는 바와 같이 고분자응집제가 용해되어 생긴 실타래와 같은 고분자속(高分子束)의 접착력에 의해 고분자속으로 현탁입자를 응집시킨다. The principle of dehydration and aggregation of the polymer coagulant is as follows. That is, as shown in Fig. 1, the suspended particles are agglomerated into the polymer bundle by the adhesive force of the polymer bundle such as the thread formed by dissolving the polymer coagulant.

그러나 기존의 하수슬러지 응집장치는 도 2에서 보는 바와 같이 고분자응집제가 유입되는 고분자응집제 유입관(20), 소화슬러지가 유입되는 소화슬러지 유입관(30)과 상기 고분자응집제 유입관(20) 및 소화슬러지 유입관(30)을 통해 유입되어 혼합된 고분자 응집제와 소화슬러지의 혼합액을 혼합하여 플럭을 만드는 혼합탱크(10) 및 탈수기(50)로 구성되며, 상기 혼합탱크(10)에는 교반날개(11)를 회전시키는 모터(40)가 설치되어 있다. However, the existing sewage sludge flocculating device is a polymer coagulant inlet tube 20 into which the polymer coagulant is introduced, a digested sludge inlet tube 30 into which the digested sludge is introduced, and the polymer coagulant inlet tube 20 and the digestion as shown in FIG. It consists of a mixing tank (10) and a dehydrator (50) to make a floc by mixing the mixed solution of the polymer flocculant and the digested sludge introduced through the sludge inlet pipe 30, the mixing tank 10, the stirring blade (11) The motor 40 which rotates) is provided.

따라서 하수슬러지 응집장치를 가동하면 하수슬러지와 고분자응집제가 각각 고분자응집제 유입관(20)과 소화슬러지 유입관(30)을 통해 혼합탱크(10)로 유입된 후 교반날개(11)가 회전함에 따라 혼합되면서 응집된다. Therefore, when the sewage sludge flocculating device is operated, the sewage sludge and the polymer coagulant are introduced into the mixing tank 10 through the polymer coagulant inlet tube 20 and the digested sludge inlet tube 30, respectively, and then the stirring blade 11 rotates. Agglomerates while mixing.

이때 교반날개(11)의 회전을 800rpm 이상으로 빠르게 하면 고분자응집제의 고분자속이 잘리게 되어 현탁입자를 응집하는 힘이 저하되고 교반날개(11)의 회전을 600rpm 이하로 느리게 하면 고분자응집제와 소화슬러지의 혼합이 잘 이루어지지 않아 고분자응집제를 과다하게 투입하지 않을 수 없다. At this time, if the rotation of the stirring blade 11 is faster than 800rpm, the polymer flux of the polymer coagulant is cut, and the force to aggregate the suspended particles is reduced, and if the rotation of the stirring blade 11 is lower than 600rpm, the polymer coagulant and the digested sludge Inadequately mixed, the coagulant must be excessively added.

그러나 고분자응집제를 과다 투입하면 약품비용이 증가함은 물론 잔류약품의 분말이 탈수기(50)에 설치되어 있는 여과포(51) 공극을 막게 되어 탈수 효율이 떨어지며, 이에 따라 케이크 함수율이 나빠져 케이크 발생량이 증가하게 되므로 처리경비의 증가를 가져온다.
However, when the polymer coagulant is excessively added, the drug cost increases, and the powder of the residual drug blocks the pores of the filter cloth 51 installed in the dehydrator 50, so that the dehydration efficiency is lowered. This increases the processing cost.

따라서 고분자응집제의 고분자속이 교반날개에 의하여 잘리지 않으면서도 고분자응집제와 소화슬러지의 혼합이 잘 이루어지는 소화슬러지 응집장치의 개발이 요구되고 있다.
Therefore, it is required to develop a fired sludge flocculating device in which the polymer coagulant of the polymer coagulant is well mixed with the polymer coagulant and the fired sludge without being cut by the stirring blade.

본 발명은 상기와 같은 과제를 해결하기 위하여 고안된 것으로서 소화슬러지와 고분자응집제를 각각 고분자응집제 유입관과 소화슬러지 유입관을 통해 관로상에 설치된 혼합관으로 유입시킬 때 상기 고분자응집제 유입관 및 소화슬러지 유입관과 혼합관 사이에 벤츄리관을 추가로 설치함으로써 해결할 수 있다.
The present invention is designed to solve the above problems, when the digested sludge and polymer coagulant are introduced into the mixing tube installed on the pipeline through the polymer coagulant inlet pipe and the digested sludge inlet pipe, respectively, the polymer coagulant inlet pipe and the digested sludge inflow This can be solved by providing an additional venturi tube between the tube and the mixing tube.

본 발명의 장치에 의하면 소화슬러지와 고분자응집제의 혼합액이 교반탱크로 유입되는 과정에서 2차 이상 난류와 캐비테이션 현상을 일으킴으로써 벤츄리 작용을 하여 고분자응집제와 소화슬러지가 잘 혼합되고 따라서 교반탱크에서는 교반날개를 중간속도인 600∼800rpm으로 회전시켜도 고분자응집제의 응집작용을 최대화시켜 줌으로써 적정한 크기의 플록을 형성시켜줄 수 있다. 이에 따라 고분자응집제를 과다하게 투입하지 않아도 되므로 잔존 약품에 의한 여과포의 공극 막힘을 예방하여 슬러지 처리량을 향상시킬 수 있음은 물론 약품 비용을 절약할 수 있다.
According to the apparatus of the present invention, the mixture mixture of the digested sludge and the polymer coagulant is introduced into the stirring tank to cause the secondary turbulence and cavitation phenomenon to act as a venturi, so that the polymer coagulant and the digested sludge are mixed well. Rotation at a medium speed of 600 to 800rpm can maximize flocculation of the polymer coagulant to form flocs of appropriate size. Accordingly, the polymer coagulant does not need to be excessively added, thereby preventing the clogging of the filter cloth due to the remaining chemicals, thereby improving the sludge throughput, as well as reducing the drug cost.

제1도 : 고분자응집제가 탈수 및 응집하는 원리를 보여주는 도
제2도 : 기존의 소화슬러지 응집장치를 보여주는 도
제3도 : 본 발명의 소화슬러지 응집장치를 보여주는 도Fig. 1: A diagram showing the principle of dehydration and aggregation of the polymer coagulant
2 is a diagram showing a conventional digested sludge flocculation device
3 is a view showing the digested sludge flocculating device of the present invention

본 발명은 소화 슬러지와 고분자 응집제를 함께 슬러지 혼합장치에 투입한 후 혼합 및 교반하여 플록으로 만들 때에 고분자응집제 유입관 및 소화슬러지 유입관과 혼합관 사이에 난류와 캐비테이션을 일으켜 벤츄리 작용을 하는 연결관을 추가로 설치함으로써 적정한 크기의 플록을 형성시키는 한편, 약품의 투입량을 대폭 절감할 수 있는 소화슬러지 응집장치에 관한 것이다.
In the present invention, when the digested sludge and the polymer flocculant are added together into the sludge mixing apparatus, the mixture is mixed and stirred to form a floc. The present invention relates to a fire extinguishing sludge agglomeration apparatus which can additionally form flocs of an appropriate size and significantly reduce the dosage of chemicals.

이하, 도면을 참조하여 설명한다. A description with reference to the drawings is as follows.

도 3은 본 발명의 소화슬러지 응집장치를 보여주는 도면이다.3 is a view showing the digested sludge flocculation apparatus of the present invention.

본 발명의 소화슬러지 응집장치는 고분자응집제 유입관(100), 소화슬러지 유입관(110), 혼합관(212) 및 탈수기(300)로 구성된 소화슬러지 응집장치에 있어서, 상기 고분자응집제 유입관(100) 및 소화슬러지 유입관(110)과 교반탱크(231) 사이에 도 3에서 보는 바와 같이 하나 이상의 벤츄리 구조를 갖춘 벤츄리관(210,220)을 설치한 소화슬러지 응집장치이다. Fire extinguishing sludge agglomeration apparatus of the present invention is a polymer coagulant inlet tube 100, digestive sludge inlet tube 110, mixing pipe 212 and the dehydrator 300 in the digester sludge agglomeration apparatus consisting of, the polymer coagulant inlet tube 100 And the digestion sludge inlet pipe 110 and the agitation tank 231 as shown in Figure 3 is a digestion sludge agglomeration apparatus having a venturi pipe (210,220) having one or more venturi structure.

벤츄리관(210,220)은 1∼2개를 형성하는 것이 적합하다. 그 이유는 벤츄리 구조에 의하여 고분자응집제와 소화슬러지 혼합제는 1～2회 난류와 캐비테이션을 유발하여 벤츄리 작용을 함으로써 고분자응집제와 소화슬러지를 고르게 혼합시켜 주기 때문이다. It is preferable to form one or two venturi tubes 210 and 220. The reason for this is that the polymer coagulant and the digested sludge admixture are mixed with the polymer coagulant and the digested sludge evenly by the venturi action by causing turbulence and cavitation once or twice by the venturi structure.

또 본 발명의 소화슬러지 응집장치에 투입되는 고분자 응집제는 파우더 형태의 약품을 물에 용해시킨 농도 0.2%의 고분자 응집제로서 통상 업계에서 사용되는 제품이다. In addition, the polymer flocculant introduced into the digestive sludge flocculating apparatus of the present invention is a product used in the industry as a polymer flocculant having a concentration of 0.2% dissolved in water in powder form.

한편, 제1벤츄리관(210) 앞쪽에는 압력계(213)가 설치되어 있고, 또 상기 제1벤츄리관(210)에는 유량조절밸브(211)가 설치되어 있다. On the other hand, the pressure gauge 213 is provided in front of the first venturi pipe 210, and the flow control valve 211 is provided in the first venturi pipe 210.

이러한 구조를 다시 정리하면, 고분자응집제 유입관(100)과 소화슬러지 유입관(110)은 제1벤츄리관(210)의 입구부와 연결되고, 상기 제1벤츄리관(210)의 출구부에는 혼합관(212)의 입구부가 연결되어 있으며, 상기 혼합관(212)의 출구부에는 제2벤츄리관(220)의 입구부가 연결되어 있다.To reorganize this structure, the polymer coagulant inlet pipe 100 and the digested sludge inlet pipe 110 is connected to the inlet of the first venturi tube 210, the mixing in the outlet of the first venturi tube 210 The inlet of the pipe 212 is connected, the inlet of the second venturi tube 220 is connected to the outlet of the mixing pipe 212.

상기 제2벤츄리관(220)의 출구부에는 교반탱크(231)가 연결되어 있으며, 상기 교반탱크(231)에는 모터(232)에 의해 회전하는 교반날개(233)를 가진 교반부(230)가 설치되어 있다.The stirring tank 231 is connected to the outlet of the second venturi tube 220, and the stirring tank 231 has a stirring blade 233 rotating by the motor 232. It is installed.

상기 교반탱크(231)의 출구부는 배출관(240)과 연결되어 있어서, 상기 배출관(240)을 통해 배출되는 응집된 소화슬러지가 탈수기(300)로 배출되는 구조를 가진다.The outlet portion of the stirring tank 231 is connected to the discharge pipe 240, has a structure in which the aggregated digested sludge discharged through the discharge pipe 240 is discharged to the dehydrator (300).

이러한 제1벤츄리관(210), 혼합관(212), 제2벤츄리관(220), 교반탱크(231)는 지면과 수평인 상태로 설치되는 것이 좋으며, 이는 큰 동력을 필요로 하지 않으면서도 캐비테이션 현상을 발생할 수 있는 것이다.
The first venturi tube 210, the mixing tube 212, the second venturi tube 220, the stirring tank 231 is preferably installed in a horizontal state with the ground, which does not require a large power cavitation It can happen.

이하, 본 발명을 실시예를 중심으로 하여 설명한다.EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated centering on an Example.

우선 고분자응집제와 소화슬러지를 각각 고분자응집제 유입관(100)과 소화슬러지 유입관(110)을 통해 제1벤츄리관(210)으로 유입시킨다. First, the polymer coagulant and the digested sludge are introduced into the first venturi tube 210 through the polymer coagulant inlet tube 100 and the digested sludge inlet tube 110, respectively.

이울러 소화슬러지의 PH가를 낮추기 위하여 고분자응집제 및/또는 소화슬러지와 함께 세정수를 유입시키지만 필요하면 미리 제1벤츄리관(210) 내에 세정수를 투입할 수 있다. 이 때 유입되는 세정수의 양은 고분자응집제와 소화슬러지 혼합액 대비 30 중량부 이하로 한다.In order to lower the pH value of the digested sludge, the washing water is introduced together with the polymer coagulant and / or the digested sludge, but if necessary, the washing water may be introduced into the first venturi tube 210 in advance. At this time, the amount of washing water flowing in is less than 30 parts by weight relative to the polymer coagulant and the digested sludge mixture.

제1벤츄리관(210)에 설치되는 유량조절밸브(211)는 제1벤츄리관(210) 전단의 관로압력에 따라 유량을 조절하는 것으로서, 압력계(213)에 의해 관로상의 압력을 확인할 수 있다.The flow control valve 211 installed in the first venturi pipe 210 adjusts the flow rate according to the pipe pressure of the front end of the first venturi pipe 210, and the pressure on the pipe can be confirmed by the pressure gauge 213.

그러므로, 압력이 낮은 경우 유량조절밸브(211)에 의해 제1벤츄리관(210)을 많이 닫아 제1벤츄리관(210)을 통과하는 유량의 압력을 크게 하며, 반대로 압력이 높은 경우 유량조절밸브(211)를 크게 열어 많은 유량이 통과되도록 하는 것이다.Therefore, when the pressure is low, the first venturi tube 210 is closed by the flow regulating valve 211 to increase the pressure of the flow rate passing through the first venturi tube 210, and conversely, when the pressure is high, the flow regulating valve ( Open 211) largely to allow a lot of flow.

제1벤츄리관(210)내로 유입된 고분자응집제와 소화슬러지 혼합액은 병목현상에 의해 유속과 압력이 증가한 상태로 구경이 넓은 혼합관(212)으로 유입되는데, 혼합관(212)으로 유입된 혼합액은 급속히 압력이 떨어지므로 캐비테이션(Cavitation, 空洞現像)을 일으키면서 난류가 발생하게 된다.The polymer coagulant and the digested sludge mixed liquid introduced into the first venturi tube 210 are introduced into the mixing tube 212 having a wide diameter while the flow rate and pressure are increased by the bottleneck, and the mixed liquid introduced into the mixing tube 212 is As the pressure drops rapidly, turbulence occurs while cavitation (cavitation) occurs.

이러한 난류에 의해 고분자 응집제와 소화슬러지가 고르고 빠르게 혼합된다.This turbulence allows the polymer coagulant and the digested sludge to be evenly and quickly mixed.

상기 혼합관(212)에 의해 혼합된 혼합액은 제2벤츄리관(220)으로 유입되어 통과되면서 제1벤츄리관(210)과 동일한 현상을 가지면서 처리되어 교반탱크(231)로 유입되는데, 이때도 캐비테이션을 일으키면서 혼합됨과 동시에 교반부(230)의 교반날개(233)에 의해 연속적인 혼합이 이루어지게 되며, 굳이 교반날개(233)를 고속으로 회전시키지 않아도 된다.The mixed solution mixed by the mixing tube 212 is introduced into the second venturi tube 220 while being processed while having the same phenomenon as the first venturi tube 210 and introduced into the stirring tank 231, even at this time. While mixing while causing cavitation, continuous mixing is achieved by the stirring blade 233 of the stirring unit 230, and it is not necessary to rotate the stirring blade 233 at high speed.

즉, 교반탱크(231)로 유입된 고분자응집제와 소화슬러지 혼합액은 상술한 바와 같이 미리 고르게 잘 섞여져 있으므로 굳이 교반날개(233)를 빠른 속도로 구동할 필요가 없다. 따라서 모터(232)의 속도를 조절하여 교반날개(233)를 빠르지도(800rpm 이상) 느리지도(600rpm 이하) 않은 중간속도(600∼800rpm)로 회전시키므로 고분자응집제의 고분자속을 절단할 염려가 없으면서도 고분자응집제와 소화슬러지 혼합액을 교반하여 적당한 크기의 플록을 형성하게 된다. That is, since the polymer coagulant and the digested sludge mixed liquid introduced into the stirring tank 231 are mixed well in advance as described above, it is not necessary to drive the stirring blade 233 at high speed. Therefore, by adjusting the speed of the motor 232, the stirring blade 233 is rotated at a medium speed (600 to 800 rpm) that is neither fast (800 rpm or more) or slow (600 rpm or less), without fear of cutting the polymer flux of the polymer coagulant. Also, the flocculant and the digested sludge mixture are stirred to form flocs of a suitable size.

이와 같이 고분자응집제와 소화슬러지 혼합액이 고르게 잘 섞여졌으므로 고분자응집제의 사용량을 대폭 줄임은 물론 상기와 같이 고분자응집제를 과다 사용하지 않으므로 사용하고 남는 양이 없으므로 잔존 약품에 의하여 배출관(240)의 관로상에 설치된 여과포의 공극을 막는 현상이 발생하지 않아 경비를 대폭 절감할 수 있다. In this way, since the polymer coagulant and the digested sludge mixture are mixed well, the amount of the polymer coagulant is greatly reduced, and the polymer coagulant is not excessively used as described above. As the phenomenon of blocking the air gap of the installed filter cloth does not occur, the cost can be greatly reduced.

이렇게 응집된 소화슬러지는 배출관(240)을 통해 탈수기(300)로 유입되어 탈수되는 것이다.The aggregated digested sludge is introduced into the dehydrator 300 through the discharge pipe 240 to be dehydrated.

아래 표는 2010년 6월 10일부터 6월 16일까지 본 발명의 소화슬러지 응집장치를 시험 가동한 실험예로서 소화슬러지의 처리 양과 고분자 응집제의 사용량을 보여주고 있다. 표 중 10호가 본 발명 장치에 유입된 소화슬러지의 양과 약품사용량을 보여주고 있고 기타 자료는 기존의 장치에 유입된 소화슬러지의 양과 약품사용량을 보여주고 있다. The following table shows the amount of the treated sludge treated and the amount of the polymer flocculant used as the experimental example in which the digested sludge flocculating device of the present invention was tested from June 10 to June 16, 2010. Table 10 shows the amount and digestion of digested sludge introduced into the device of the present invention, and other data shows the amount and digestion of digested sludge introduced into the existing apparatus.

1. 2010년 6월 10일 1. June 10, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월10일June 10 슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 17.017.0 13.013.0 12.012.0 159.0159.0 2시2'o clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 17.017.0 13.013.0 12.012.0 159.0159.0 3시3 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 16.016.0 12.012.0 12.012.0 157.0157.0 4시4 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 16.016.0 12.012.0 11.011.0 155.0155.0 5시5 O'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 16.016.0 12.012.0 11.011.0 155.0155.0 6시6 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 16.016.0 12.012.0 12.012.0 156.0156.0 7시7 o'clock 13.013.0 13.013.0 7.07.0 0.00.0 12.012.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 16.016.0 12.012.0 13.013.0 156.0156.0 8시8 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 15.015.0 12.012.0 12.012.0 156.0156.0 9시9 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 14.014.0 12.012.0 12.012.0 156.0156.0 10시10 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 12.012.0 13.013.0 13.013.0 13.013.0 19.019.0 15.015.0 12.012.0 12.012.0 157.0157.0 11시11 o'clock 13.013.0 12.012.0 9.09.0 0.00.0 13.013.0 10.010.0 14.014.0 12.012.0 13.013.0 19.019.0 14.014.0 12.012.0 12.012.0 153.0153.0 12시12 o'clock 13.013.0 12.012.0 9.09.0 0.00.0 13.013.0 9.09.0 16.016.0 10.010.0 13.013.0 19.019.0 14.014.0 12.012.0 13.013.0 153.0153.0 13시13 o'clock 13.013.0 12.012.0 9.09.0 0.00.0 13.013.0 9.09.0 16.016.0 11.011.0 13.013.0 19.019.0 14.014.0 12.012.0 13.013.0 154.0154.0 14시14 o'clock 13.013.0 12.012.0 9.09.0 0.00.0 13.013.0 9.09.0 11.011.0 8.08.0 13.013.0 19.019.0 14.014.0 12.012.0 14.014.0 147.0147.0 15시15 o'clock 13.013.0 12.012.0 9.09.0 0.00.0 13.013.0 9.09.0 14.014.0 3.03.0 15.015.0 19.019.0 15.015.0 16.016.0 14.014.0 152.0152.0 16시16:00 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 16.016.0 0.00.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 155.0155.0 17시17:00 13.013.0 13.013.0 9.09.0 0.00.0 14.014.0 9.09.0 16.016.0 7.07.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 163.0163.0 18시18 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 14.014.0 9.09.0 17.017.0 12.012.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 169.0169.0 19시19 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 14.014.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 170.0170.0 20시20 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 13.013.0 168.0168.0 21시21 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 13.013.0 168.0168.0 22시22:00 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 12.012.0 167.0167.0 23시23 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 169.0169.0 24시24 hours 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 169.0169.0

나. 고분자 응집제의 사용량 I. Usage of Polymer Flocculant 6월10일June 10
약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.31.3 0.90.9 1.01.0 0.90.9 0.90.9 1.01.0 1.11.1 0.90.9 13.313.3 2시2'o clock 1.51.5 1.51.5 1.11.1 0.00.0 1.31.3 1.41.4 1.01.0 1.11.1 1.01.0 0.90.9 1.01.0 1.21.2 1.01.0 14.014.0 3시3 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.51.5 1.41.4 1.31.3 1.41.4 1.21.2 1.31.3 1.71.7 1.31.3 16.716.7 4시4 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.51.5 1.61.6 1.61.6 1.71.7 1.31.3 1.51.5 1.71.7 1.61.6 18.118.1 5시5 O'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.51.5 1.51.5 1.71.7 1.61.6 1.71.7 1.41.4 1.51.5 1.71.7 1.61.6 18.218.2 6시6 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.41.4 1.41.4 1.71.7 1.61.6 1.71.7 1.21.2 1.31.3 1.41.4 1.51.5 17.317.3 7시7 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.71.7 1.51.5 1.71.7 1.11.1 1.01.0 1.11.1 1.51.5 16.016.0 8시8 o'clock 1.31.3 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.71.7 1.51.5 1.61.6 1.11.1 1.01.0 1.41.4 1.41.4 15.915.9 9시9 o'clock 1.31.3 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.71.7 1.51.5 1.61.6 1.01.0 1.01.0 1.51.5 1.31.3 15.815.8 10시10 o'clock 1.31.3 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.71.7 1.51.5 1.61.6 1.11.1 1.01.0 1.51.5 1.31.3 16.016.0 11시11 o'clock 1.31.3 1.41.4 1.11.1 0.00.0 1.41.4 1.21.2 1.31.3 1.31.3 1.61.6 1.11.1 1.01.0 1.51.5 1.21.2 15.415.4 12시12 o'clock 1.41.4 1.41.4 1.11.1 0.00.0 1.51.5 1.21.2 1.51.5 1.41.4 1.61.6 1.11.1 1.11.1 1.41.4 1.01.0 15.715.7 13시13 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.51.5 1.41.4 1.61.6 1.21.2 1.11.1 1.41.4 1.01.0 15.915.9 14시14 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.11.1 1.01.0 1.41.4 1.11.1 1.01.0 1.31.3 1.01.0 14.614.6 15시15 o'clock 1.41.4 1.41.4 1.11.1 0.00.0 1.51.5 1.21.2 1.21.2 0.20.2 1.21.2 0.90.9 1.01.0 1.31.3 1.01.0 13.413.4 16시16:00 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.41.4 0.00.0 1.21.2 1.01.0 1.01.0 1.51.5 1.01.0 13.913.9 17시17:00 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.41.4 0.60.6 1.21.2 1.01.0 0.90.9 1.41.4 1.01.0 14.314.3 18시18 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.41.4 1.01.0 14.514.5 19시19 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.41.4 1.01.0 1.21.2 1.01.0 1.01.0 1.51.5 1.01.0 14.914.9 20시20 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.21.2 1.41.4 1.01.0 1.21.2 1.01.0 1.01.0 1.51.5 1.01.0 15.015.0 21시21 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 1.01.0 1.21.2 1.01.0 0.90.9 1.41.4 0.90.9 14.614.6 22시22:00 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.41.4 0.90.9 14.514.5 23시23 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.41.4 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.514.5 24시24 hours 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.614.6

2. 2010년 6월 11일2. June 11, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월11일June 11
슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 169.0169.0 2시2'o clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 12.012.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 168.0168.0 3시3 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 16.016.0 12.012.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 167.0167.0 4시4 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 13.013.0 168.0168.0 5시5 O'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 13.013.0 168.0168.0 6시6 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 17.017.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 13.013.0 167.0167.0 7시7 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 16.016.0 12.012.0 16.016.0 19.019.0 15.015.0 18.018.0 12.012.0 164.0164.0 8시8 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 16.016.0 12.012.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 166.0166.0 9시9 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 16.016.0 13.013.0 16.016.0 19.019.0 15.015.0 18.018.0 14.014.0 167.0167.0 10시10 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 16.016.0 13.013.0 16.016.0 18.018.0 15.015.0 18.018.0 13.013.0 165.0165.0 11시11 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 6.06.0 9.09.0 16.016.0 13.013.0 16.016.0 18.018.0 15.015.0 18.018.0 13.013.0 158.0158.0 12시12 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 9.09.0 9.09.0 16.016.0 13.013.0 16.016.0 18.018.0 15.015.0 18.018.0 14.014.0 163.0163.0 13시13 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 11.011.0 10.010.0 16.016.0 13.013.0 16.016.0 18.018.0 15.015.0 18.018.0 14.014.0 166.0166.0 14시14 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 12.012.0 9.09.0 16.016.0 13.013.0 16.016.0 18.018.0 15.015.0 16.016.0 14.014.0 164.0164.0 15시15 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 13.013.0 9.09.0 16.016.0 13.013.0 16.016.0 18.018.0 15.015.0 15.015.0 13.013.0 163.0163.0 16시16:00 13.013.0 13.013.0 9.09.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 19.019.0 15.015.0 15.015.0 13.013.0 162.0162.0 17시17:00 13.013.0 13.013.0 9.09.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 19.019.0 15.015.0 15.015.0 7.07.0 156.0156.0 18시18 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 19.019.0 15.015.0 15.015.0 0.00.0 148.0148.0 19시19 o'clock 13.013.0 13.013.0 9.09.0 0.00.0 12.012.0 9.09.0 16.016.0 13.013.0 16.016.0 19.019.0 15.015.0 15.015.0 0.00.0 150.0150.0 20시20 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 16.016.0 13.013.0 16.016.0 19.019.0 15.015.0 15.015.0 0.00.0 149.0149.0 21시21 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 19.019.0 15.015.0 15.015.0 3.03.0 151.0151.0 22시22:00 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 18.018.0 15.015.0 15.015.0 0.00.0 147.0147.0 23시23 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 18.018.0 15.015.0 14.014.0 1.01.0 147.0147.0 24시24 hours 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 18.018.0 15.015.0 14.014.0 0.00.0 146.0146.0

나. 고분자 응집제의 사용량I. Usage of Polymer Flocculant 6월11일June 11
약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.614.6 2시2'o clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.11.1 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.314.3 3시3 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.514.5 4시4 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.614.6 5시5 O'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.514.5 6시6 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.11.1 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.314.3 7시7 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.11.1 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 0.90.9 14.514.5 8시8 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.51.5 1.11.1 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.41.4 0.90.9 14.414.4 9시9 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.11.1 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 1.01.0 14.414.4 10시10 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.51.5 1.21.2 1.31.3 0.90.9 1.21.2 1.01.0 0.90.9 1.51.5 1.01.0 14.514.5 11시11 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 0.70.7 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.51.5 1.01.0 13.813.8 12시12 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.21.2 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.51.5 1.01.0 14.314.3 13시13 o'clock 1.41.4 1.51.5 1.11.1 0.00.0 1.41.4 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.51.5 1.01.0 14.314.3 14시14 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.31.3 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 1.01.0 14.214.2 15시15 o'clock 1.51.5 1.61.6 1.11.1 0.00.0 1.31.3 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 1.01.0 14.214.2 16시16:00 1.51.5 1.51.5 1.11.1 0.00.0 1.31.3 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 1.11.1 14.214.2 17시17:00 1.41.4 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 1.01.0 13.813.8 18시18 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 1.01.0 1.31.3 1.11.1 14.114.1 19시19 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.21.2 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 1.11.1 13.913.9 20시20 o'clock 1.51.5 1.31.3 1.11.1 0.00.0 1.31.3 1.21.2 1.21.2 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 0.60.6 13.413.4 21시21 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.31.3 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 0.30.3 13.213.2 22시22:00 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.21.2 0.90.9 1.21.2 0.90.9 0.90.9 1.31.3 0.00.0 12.912.9 23시23 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.31.3 1.21.2 1.21.2 0.90.9 1.21.2 0.80.8 0.90.9 1.31.3 0.00.0 12.912.9 24시24 hours 1.51.5 1.51.5 1.11.1 0.00.0 1.31.3 1.21.2 1.21.2 0.90.9 1.21.2 0.80.8 0.90.9 1.31.3 0.00.0 12.912.9

3. 2010년 6월 12일3. June 12, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월12일June 12
슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 18.018.0 15.015.0 14.014.0 0.00.0 146.0146.0 2시2'o clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 18.018.0 15.015.0 14.014.0 0.00.0 146.0146.0 3시3 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 13.013.0 16.016.0 17.017.0 14.014.0 14.014.0 0.00.0 144.0144.0 4시4 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 13.013.0 16.016.0 17.017.0 14.014.0 13.013.0 0.00.0 144.0144.0 5시5 O'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 16.016.0 17.017.0 14.014.0 13.013.0 0.00.0 143.0143.0 6시6 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 16.016.0 17.017.0 14.014.0 13.013.0 0.00.0 143.0143.0 7시7 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 16.016.0 17.017.0 14.014.0 13.013.0 0.00.0 143.0143.0 8시8 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 10.010.0 12.012.0 15.015.0 17.017.0 10.010.0 13.013.0 0.00.0 133.0133.0 9시9 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 9.09.0 12.012.0 15.015.0 18.018.0 10.010.0 13.013.0 0.00.0 133.0133.0 10시10 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 0.00.0 145.0145.0 11시11 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 0.00.0 145.0145.0 12시12 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 0.00.0 144.0144.0 13시13 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 0.00.0 144.0144.0 14시14 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 0.00.0 144.0144.0 15시15 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 4.04.0 148.0148.0 16시16:00 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 15.015.0 19.019.0 14.014.0 14.014.0 13.013.0 158.0158.0 17시17:00 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 6.06.0 19.019.0 14.014.0 6.06.0 11.011.0 139.0139.0 18시18 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 15.015.0 12.012.0 0.00.0 19.019.0 14.014.0 0.00.0 10.010.0 125.0125.0 19시19 o'clock 13.013.0 12.012.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 0.00.0 19.019.0 14.014.0 0.00.0 10.010.0 125.0125.0 20시20 o'clock 13.013.0 12.012.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 0.00.0 19.019.0 14.014.0 0.00.0 10.010.0 125.0125.0 21시21 o'clock 13.013.0 12.012.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 0.00.0 19.019.0 14.014.0 0.00.0 9.09.0 124.0124.0 22시22:00 13.013.0 13.013.0 8.08.0 0.00.0 13.013.0 9.09.0 15.015.0 12.012.0 0.00.0 19.019.0 14.014.0 0.00.0 10.010.0 126.0126.0 23시23 o'clock 13.013.0 12.012.0 8.08.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 0.00.0 19.019.0 14.014.0 0.00.0 11.011.0 124.0124.0 24시24 hours 13.013.0 12.012.0 8.08.0 0.00.0 13.013.0 9.09.0 14.014.0 12.012.0 0.00.0 18.018.0 14.014.0 0.00.0 11.011.0 124.0124.0

나. 고분자 응집제의 사용량I. Usage of Polymer Flocculant 6월12일June 12 약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.21.2 0.90.9 1.21.2 0.80.8 0.90.9 1.31.3 0.00.0 12.712.7 2시2'o clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.21.2 0.90.9 1.21.2 0.80.8 0.90.9 1.31.3 0.00.0 12.812.8 3시3 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.31.3 1.21.2 1.41.4 1.11.1 1.21.2 1.01.0 0.90.9 1.31.3 0.00.0 13.513.5 4시4 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.51.5 1.11.1 1.21.2 1.11.1 0.90.9 1.31.3 0.00.0 13.513.5 5시5 O'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.51.5 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.00.0 13.513.5 6시6 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.51.5 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.00.0 13.613.6 7시7 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.51.5 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.00.0 13.513.5 8시8 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.01.0 1.11.1 1.21.2 1.01.0 0.70.7 1.31.3 0.00.0 12.712.7 9시9 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 0.70.7 1.11.1 1.21.2 1.01.0 0.80.8 1.31.3 0.00.0 12.612.6 10시10 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 1.01.0 1.01.0 1.21.2 0.00.0 13.013.0 11시11 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.00.0 13.013.0 12시12 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.00.0 13.013.0 13시13 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.00.0 13.213.2 14시14 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 1.01.0 1.01.0 1.21.2 0.00.0 13.113.1 15시15 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 1.01.0 1.01.0 1.31.3 0.30.3 13.313.3 16시16:00 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 1.21.2 0.90.9 1.01.0 1.31.3 0.80.8 13.713.7 17시17:00 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 0.50.5 0.90.9 1.01.0 0.50.5 0.80.8 12.312.3 18시18 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.01.0 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.311.3 19시19 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.21.2 1.01.0 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.211.2 20시20 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.11.1 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.411.4 21시21 o'clock 1.51.5 1.51.5 1.11.1 0.00.0 1.21.2 1.21.2 1.01.0 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.411.4 22시22:00 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.01.0 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.311.3 23시23 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.21.2 1.01.0 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.311.3 24시24 hours 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 0.00.0 0.90.9 1.01.0 0.00.0 0.90.9 11.211.2

4. 2010년 6월 13일4. June 13, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월13일June 13
슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 137.0137.0 2시2'o clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 10.010.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 138.0138.0 3시3 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 10.010.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 138.0138.0 4시4 o'clock 13.013.0 13.013.0 8.08.0 0.00.0 12.012.0 10.010.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 138.0138.0 5시5 O'clock 13.013.0 12.012.0 8.08.0 0.00.0 12.012.0 10.010.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 137.0137.0 6시6 o'clock 13.013.0 12.012.0 8.08.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 137.0137.0 7시7 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 136.0136.0 8시8 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 136.0136.0 9시9 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 136.0136.0 10시10 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 14.014.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 136.0136.0 11시11 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 135.0135.0 12시12 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 12.012.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 135.0135.0 13시13 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 12.012.0 15.015.0 19.019.0 14.014.0 0.00.0 10.010.0 136.0136.0 14시14 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 7.07.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 130.0130.0 15시15 o'clock 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 15.015.0 18.018.0 14.014.0 0.00.0 10.010.0 123.0123.0 16시16:00 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 122.0122.0 17시17:00 13.013.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 15.015.0 18.018.0 14.014.0 0.00.0 9.09.0 122.0122.0 18시18 o'clock 4.04.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 14.014.0 18.018.0 14.014.0 0.00.0 10.010.0 113.0113.0 19시19 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 20시20 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 21시21 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 22시22:00 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 23시23 o'clock 0.00.0 13.013.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 109.0109.0 24시24 hours 0.00.0 12.012.0 7.07.0 0.00.0 13.013.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 109.0109.0

나. 고분자 응집제의 사용량I. Usage of Polymer Flocculant 6월13일June 13
약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h]
1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 1.51.5 1.41.4 1.11.1 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 1.01.0 0.00.0 0.70.7 12.112.1 2시2'o clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 3시3 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 4시4 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 5시5 O'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 6시6 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 7시7 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 8시8 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 9시9 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 10시10 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.212.2 11시11 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.112.1 12시12 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.112.1 13시13 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 1.11.1 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 12.112.1 14시14 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.70.7 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 11.711.7 15시15 o'clock 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 11.011.0 16시16:00 1.51.5 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 11.111.1 17시17:00 1.51.5 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.21.2 0.90.9 1.01.0 0.00.0 0.80.8 11.011.0 18시18 o'clock 0.40.4 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.89.8 19시19 o'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.49.4 20시20 o'clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.59.5 21시21 o'clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.59.5 22시22:00 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.49.4 23시23 o'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.49.4 24시24 hours 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 0.90.9 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.49.4

5. 2010년 6월 14일 5. June 14, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월14일June 14
슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 13.013.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 109.0109.0 2시2'o clock 0.00.0 12.012.0 7.07.0 0.00.0 13.013.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 109.0109.0 3시3 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 4시4 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 5시5 O'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 6시6 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 7시7 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 8시8 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 9시9 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 13.013.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 108.0108.0 10시10 o'clock 0.00.0 12.012.0 7.07.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 107.0107.0 11시11 o'clock 12.012.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 114.0114.0 12시12 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 13시13 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 14시14 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 15시15 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 16시16:00 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 13.013.0 116.0116.0 17시17:00 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 10.010.0 113.0113.0 18시18 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 19시19 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 20시20 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 21시21 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 22시22:00 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 23시23 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 24시24 hours 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0

나. 고분자 응집제의 사용량I. Usage of Polymer Flocculant 6월14일June 14
약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.69.6 2시2'o clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.69.6 3시3 o'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.59.5 4시4 o'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 0.90.9 1.01.0 0.00.0 0.80.8 9.59.5 5시5 O'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.80.8 9.69.6 6시6 o'clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.80.8 9.79.7 7시7 o'clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.80.8 9.79.7 8시8 o'clock 0.00.0 1.51.5 1.01.0 0.00.0 1.21.2 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.80.8 9.89.8 9시9 o'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.80.8 9.69.6 10시10 o'clock 0.00.0 1.41.4 1.01.0 0.00.0 1.21.2 1.11.1 1.01.0 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.80.8 9.69.6 11시11 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.21.2 1.21.2 1.11.1 0.00.0 1.11.1 1.01.0 1.11.1 0.00.0 1.01.0 10.610.6 12시12 o'clock 1.61.6 1.51.5 0.00.0 0.00.0 1.21.2 1.21.2 1.11.1 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 1.01.0 10.710.7 13시13 o'clock 1.61.6 1.51.5 0.00.0 0.00.0 1.21.2 1.21.2 1.11.1 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 1.01.0 10.710.7 14시14 o'clock 1.61.6 1.41.4 0.00.0 0.00.0 1.21.2 1.21.2 1.11.1 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 1.01.0 10.610.6 15시15 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.21.2 1.21.2 0.90.9 0.00.0 1.11.1 1.01.0 1.11.1 0.00.0 1.01.0 10.410.4 16시16:00 1.61.6 1.51.5 0.00.0 0.00.0 1.21.2 1.21.2 0.90.9 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 1.01.0 10.510.5 17시17:00 1.51.5 1.51.5 0.00.0 0.00.0 1.21.2 1.21.2 0.90.9 0.00.0 1.11.1 1.01.0 1.01.0 0.00.0 0.40.4 9.89.8 18시18 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 0.90.9 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.310.3 19시19 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.310.3 20시20 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.410.4 21시21 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 0.90.9 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.310.3 22시22:00 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.410.4 23시23 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 0.90.9 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.210.2 24시24 hours 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.310.3

6. 2010년 6월 15일6. June 15, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월15일June 15
슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 2시2'o clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 3시3 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 4시4 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 5시5 O'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 6시6 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 7시7 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 8시8 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 13.013.0 0.00.0 12.012.0 114.0114.0 9시9 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 10시10 o'clock 13.013.0 12.012.0 0.00.0 0.00.0 12.012.0 9.09.0 12.012.0 0.00.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 115.0115.0 11시11 o'clock 14.014.0 13.013.0 0.00.0 0.00.0 13.013.0 11.011.0 12.012.0 5.05.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 125.0125.0 12시12 o'clock 14.014.0 13.013.0 0.00.0 0.00.0 13.013.0 11.011.0 12.012.0 12.012.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 132.0132.0 13시13 o'clock 14.014.0 13.013.0 0.00.0 0.00.0 13.013.0 11.011.0 13.013.0 12.012.0 13.013.0 18.018.0 14.014.0 0.00.0 12.012.0 133.0133.0 14시14 o'clock 14.014.0 13.013.0 0.00.0 0.00.0 14.014.0 11.011.0 13.013.0 12.012.0 13.013.0 18.018.0 14.014.0 2.02.0 12.012.0 136.0136.0 15시15 o'clock 14.014.0 13.013.0 0.00.0 0.00.0 14.014.0 11.011.0 12.012.0 12.012.0 14.014.0 18.018.0 14.014.0 12.012.0 12.012.0 146.0146.0 16시16:00 14.014.0 13.013.0 13.013.0 0.00.0 14.014.0 11.011.0 12.012.0 12.012.0 14.014.0 18.018.0 13.013.0 13.013.0 12.012.0 159.0159.0 17시17:00 14.014.0 13.013.0 13.013.0 0.00.0 14.014.0 11.011.0 13.013.0 12.012.0 14.014.0 18.018.0 13.013.0 13.013.0 12.012.0 160.0160.0 18시18 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 14.014.0 11.011.0 13.013.0 13.013.0 14.014.0 18.018.0 13.013.0 12.012.0 12.012.0 160.0160.0 19시19 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 14.014.0 11.011.0 12.012.0 13.013.0 14.014.0 18.018.0 13.013.0 13.013.0 12.012.0 160.0160.0 20시20 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 14.014.0 11.011.0 12.012.0 13.013.0 13.013.0 18.018.0 13.013.0 13.013.0 12.012.0 159.0159.0 21시21 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 14.014.0 11.011.0 13.013.0 13.013.0 13.013.0 18.018.0 13.013.0 13.013.0 12.012.0 160.0160.0 22시22:00 14.014.0 13.013.0 13.013.0 0.00.0 13.013.0 11.011.0 12.012.0 13.013.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 158.0158.0 23시23 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 13.013.0 11.011.0 13.013.0 13.013.0 13.013.0 18.018.0 14.014.0 13.013.0 12.012.0 160.0160.0 24시24 hours 14.014.0 13.013.0 13.013.0 0.00.0 12.012.0 11.011.0 12.012.0 13.013.0 13.013.0 18.018.0 14.014.0 13.013.0 12.012.0 158.0158.0

나. 고분자 응집제의 사용량I. Usage of Polymer Flocculant 6월15일June 15 약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.11.1 10.410.4 2시2'o clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.310.3 3시3 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 0.90.9 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.210.2 4시4 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 0.90.9 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.110.1 5시5 O'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.310.3 6시6 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.310.3 7시7 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.310.3 8시8 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 0.90.9 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.11.1 10.110.1 9시9 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 0.90.9 0.90.9 0.00.0 1.01.0 10.110.1 10시10 o'clock 1.51.5 1.51.5 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.00.0 1.11.1 1.01.0 0.90.9 0.00.0 1.01.0 10.310.3 11시11 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 0.40.4 1.11.1 1.01.0 0.90.9 0.00.0 1.01.0 10.610.6 12시12 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 1.11.1 1.11.1 0.90.9 0.90.9 0.00.0 1.01.0 11.211.2 13시13 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 1.11.1 1.11.1 0.90.9 0.90.9 0.00.0 1.01.0 11.211.2 14시14 o'clock 1.51.5 1.41.4 0.00.0 0.00.0 1.11.1 1.21.2 1.11.1 1.11.1 1.11.1 0.90.9 0.90.9 0.10.1 1.01.0 11.411.4 15시15 o'clock 1.31.3 1.31.3 0.00.0 0.00.0 1.11.1 1.21.2 1.01.0 1.11.1 1.11.1 0.90.9 0.90.9 1.11.1 1.01.0 12.012.0 16시16:00 1.21.2 1.31.3 1.01.0 0.00.0 1.01.0 1.21.2 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 1.11.1 1.01.0 12.712.7 17시17:00 1.21.2 1.31.3 1.01.0 0.00.0 0.90.9 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 1.11.1 1.01.0 12.512.5 18시18 o'clock 1.21.2 1.21.2 1.11.1 0.00.0 0.90.9 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.90.9 1.21.2 1.01.0 12.812.8 19시19 o'clock 1.31.3 1.31.3 1.11.1 0.00.0 0.90.9 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 1.21.2 1.01.0 12.812.8 20시20 o'clock 1.31.3 1.31.3 1.11.1 0.00.0 1.01.0 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 1.11.1 1.01.0 12.812.8 21시21 o'clock 1.21.2 1.31.3 1.11.1 0.00.0 1.01.0 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.90.9 1.11.1 1.01.0 12.912.9 22시22:00 1.21.2 1.21.2 1.11.1 0.00.0 0.90.9 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 12.412.4 23시23 o'clock 1.21.2 1.31.3 1.11.1 0.00.0 0.90.9 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 12.512.5 24시24 hours 1.31.3 1.31.3 1.11.1 0.00.0 1.01.0 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 12.612.6

7. 2010년 6월 16일 7. June 16, 2010

가. 소화슬러지의 처리 양end. Treatment volume of digested sludge 6월16일June 16
슬 러Slurry 지 공 급 유 량[㎥/h]  Supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 12.012.0 11.011.0 12.012.0 13.013.0 13.013.0 18.018.0 14.014.0 13.013.0 12.012.0 158.0158.0 2시2'o clock 14.014.0 13.013.0 13.013.0 0.00.0 9.09.0 11.011.0 12.012.0 13.013.0 13.013.0 18.018.0 14.014.0 13.013.0 12.012.0 155.0155.0 3시3 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 0.00.0 11.011.0 12.012.0 13.013.0 13.013.0 18.018.0 14.014.0 13.013.0 12.012.0 146.0146.0 4시4 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 0.00.0 11.011.0 12.012.0 12.012.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 144.0144.0 5시5 O'clock 14.014.0 13.013.0 12.012.0 0.00.0 0.00.0 11.011.0 12.012.0 12.012.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 143.0143.0 6시6 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 0.00.0 9.09.0 12.012.0 13.013.0 13.013.0 18.018.0 14.014.0 13.013.0 12.012.0 144.0144.0 7시7 o'clock 14.014.0 13.013.0 12.012.0 0.00.0 6.06.0 5.05.0 12.012.0 12.012.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 143.0143.0 8시8 o'clock 14.014.0 13.013.0 12.012.0 0.00.0 12.012.0 12.012.0 13.013.0 12.012.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 157.0157.0 9시9 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 12.012.0 12.012.0 13.013.0 12.012.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 158.0158.0 10시10 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 12.012.0 12.012.0 13.013.0 12.012.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 158.0158.0 11시11 o'clock 14.014.0 13.013.0 13.013.0 0.00.0 13.013.0 12.012.0 13.013.0 10.010.0 13.013.0 18.018.0 14.014.0 12.012.0 12.012.0 157.0157.0 12시12 o'clock 14.014.0 11.011.0 11.011.0 0.00.0 14.014.0 12.012.0 10.010.0 0.00.0 13.013.0 18.018.0 14.014.0 10.010.0 10.010.0 137.0137.0 13시13 o'clock 14.014.0 10.010.0 10.010.0 0.00.0 14.014.0 12.012.0 10.010.0 0.00.0 13.013.0 18.018.0 14.014.0 10.010.0 10.010.0 135.0135.0 14시14 o'clock 14.014.0 10.010.0 10.010.0 0.00.0 14.014.0 12.012.0 10.010.0 5.05.0 13.013.0 18.018.0 14.014.0 10.010.0 10.010.0 140.0140.0 15시15 o'clock 10.010.0 10.010.0 10.010.0 0.00.0 3.03.0 12.012.0 11.011.0 11.011.0 13.013.0 18.018.0 14.014.0 10.010.0 10.010.0 132.0132.0 16시16:00 11.011.0 10.010.0 10.010.0 0.00.0 9.09.0 11.011.0 11.011.0 11.011.0 13.013.0 18.018.0 14.014.0 10.010.0 10.010.0 138.0138.0 17시17:00 11.011.0 10.010.0 6.06.0 0.00.0 8.08.0 7.07.0 7.07.0 11.011.0 8.08.0 18.018.0 9.09.0 10.010.0 10.010.0 115.0115.0 18시18 o'clock 11.011.0 10.010.0 0.00.0 0.00.0 12.012.0 0.00.0 0.00.0 11.011.0 0.00.0 18.018.0 0.00.0 10.010.0 10.010.0 82.082.0 19시19 o'clock 11.011.0 10.010.0 0.00.0 0.00.0 13.013.0 0.00.0 0.00.0 11.011.0 0.00.0 18.018.0 0.00.0 10.010.0 11.011.0 84.084.0 20시20 o'clock 11.011.0 10.010.0 0.00.0 0.00.0 13.013.0 0.00.0 0.00.0 11.011.0 0.00.0 18.018.0 0.00.0 10.010.0 10.010.0 83.083.0 21시21 o'clock 11.011.0 10.010.0 0.00.0 0.00.0 13.013.0 0.00.0 0.00.0 11.011.0 0.00.0 18.018.0 0.00.0 10.010.0 10.010.0 83.083.0 22시22:00 11.011.0 10.010.0 0.00.0 0.00.0 13.013.0 0.00.0 0.00.0 11.011.0 0.00.0 18.018.0 0.00.0 10.010.0 10.010.0 83.083.0 23시23 o'clock 11.011.0 10.010.0 0.00.0 0.00.0 13.013.0 0.00.0 0.00.0 11.011.0 0.00.0 18.018.0 0.00.0 10.010.0 11.011.0 84.084.0 24시24 hours 11.011.0 10.010.0 9.09.0 0.00.0 8.08.0 10.010.0 11.011.0 11.011.0 11.011.0 15.015.0 13.013.0 10.010.0 10.010.0 129.0129.0

나. 고분자 응집제의 사용량I. Usage of Polymer Flocculant 6월16일June 16
약 품 공 급 유 량[㎥/h]   Chemical supply flow rate [㎥ / h] 1호No. 1 2호No. 2 3호No. 3 4호No. 4 5호No. 5 6호No. 6 7호No. 7 8호No. 8 9호No. 9 10호No. 10 11호No. 11 12호No. 12 13호No. 13 합 계Sum 1시1 o'clock 1.21.2 1.31.3 1.11.1 0.00.0 1.01.0 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 12.612.6 2시2'o clock 1.21.2 1.21.2 1.11.1 0.00.0 0.70.7 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 12.112.1 3시3 o'clock 1.21.2 1.21.2 1.11.1 0.00.0 0.00.0 1.11.1 1.01.0 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 11.411.4 4시4 o'clock 1.31.3 1.31.3 1.21.2 0.00.0 0.00.0 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 11.811.8 5시5 O'clock 1.31.3 1.31.3 1.21.2 0.00.0 0.00.0 1.11.1 1.11.1 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 11.811.8 6시6 o'clock 1.21.2 1.21.2 1.21.2 0.00.0 0.00.0 1.01.0 1.11.1 1.11.1 1.11.1 0.90.9 0.80.8 0.90.9 1.01.0 11.511.5 7시7 o'clock 1.21.2 1.21.2 1.11.1 0.00.0 0.50.5 0.50.5 1.01.0 1.11.1 1.01.0 0.90.9 0.80.8 0.90.9 1.01.0 11.211.2 8시8 o'clock 1.21.2 1.21.2 1.11.1 0.00.0 1.01.0 1.11.1 1.01.0 1.11.1 0.90.9 0.90.9 0.80.8 0.90.9 1.01.0 12.212.2 9시9 o'clock 1.31.3 1.31.3 1.21.2 0.00.0 1.11.1 1.11.1 1.01.0 1.11.1 0.90.9 0.90.9 0.80.8 0.90.9 1.01.0 12.612.6 10시10 o'clock 1.21.2 1.31.3 1.11.1 0.00.0 1.11.1 1.11.1 1.01.0 1.11.1 0.90.9 0.90.9 0.80.8 0.90.9 1.01.0 12.412.4 11시11 o'clock 1.21.2 1.21.2 1.11.1 0.00.0 1.01.0 1.11.1 1.01.0 0.90.9 0.90.9 0.90.9 0.80.8 0.90.9 1.01.0 12.012.0 12시12 o'clock 1.21.2 1.01.0 1.01.0 0.00.0 1.01.0 1.11.1 0.80.8 0.00.0 0.90.9 0.80.8 0.80.8 0.70.7 0.80.8 10.110.1 13시13 o'clock 1.31.3 1.01.0 1.01.0 0.00.0 1.01.0 1.11.1 0.80.8 0.00.0 0.90.9 0.80.8 0.80.8 0.70.7 0.80.8 10.210.2 14시14 o'clock 1.21.2 1.01.0 1.01.0 0.00.0 1.01.0 1.11.1 0.80.8 0.30.3 0.90.9 0.80.8 0.80.8 0.70.7 0.80.8 10.410.4 15시15 o'clock 0.80.8 1.01.0 1.01.0 0.00.0 0.30.3 1.11.1 0.80.8 0.80.8 0.90.9 0.80.8 0.80.8 0.70.7 0.70.7 9.79.7 16시16:00 0.80.8 1.01.0 0.90.9 0.00.0 0.70.7 1.01.0 0.80.8 0.80.8 0.90.9 0.80.8 0.80.8 0.70.7 0.70.7 9.99.9 17시17:00 0.80.8 1.01.0 0.60.6 0.00.0 0.60.6 0.70.7 0.50.5 0.80.8 0.60.6 0.80.8 0.50.5 0.70.7 0.80.8 8.48.4 18시18 o'clock 0.80.8 1.01.0 0.00.0 0.00.0 0.90.9 0.00.0 0.00.0 0.80.8 0.00.0 0.80.8 0.00.0 0.70.7 0.80.8 5.85.8 19시19 o'clock 0.90.9 1.01.0 0.00.0 0.00.0 0.90.9 0.00.0 0.00.0 0.80.8 0.00.0 0.80.8 0.00.0 0.70.7 0.80.8 5.95.9 20시20 o'clock 0.90.9 1.01.0 0.00.0 0.00.0 0.90.9 0.00.0 0.00.0 0.80.8 0.00.0 0.80.8 0.00.0 0.70.7 0.80.8 5.95.9 21시21 o'clock 0.80.8 1.01.0 0.00.0 0.00.0 0.90.9 0.00.0 0.00.0 0.80.8 0.00.0 0.80.8 0.00.0 0.70.7 0.70.7 5.75.7 22시22:00 0.80.8 1.01.0 0.00.0 0.00.0 0.90.9 0.00.0 0.00.0 0.80.8 0.00.0 0.80.8 0.00.0 0.70.7 0.70.7 5.75.7 23시23 o'clock 0.80.8 1.01.0 0.00.0 0.00.0 0.80.8 0.00.0 0.00.0 0.80.8 0.00.0 0.80.8 0.00.0 0.70.7 0.70.7 5.65.6 24시24 hours 0.80.8 0.90.9 0.90.9 0.00.0 0.80.8 0.90.9 0.70.7 0.80.8 0.80.8 0.60.6 0.70.7 0.80.8 0.80.8 9.59.5

위 표에서 보는 바와 같이 본 발명 소화슬러지 응집장치의 소화슬러지 처리 양은 기존 장치에 비하여 월등하게 증가하였으나 고분자 응집제의 사용량은 기존 장치의 약품 사용량과 큰 차이가 없음을 알 수 있다.
As shown in the above table, the digested sludge treatment amount of the present invention digested sludge flocculant is significantly increased compared to the existing apparatus, but the amount of polymer flocculant is not significantly different from the amount of chemicals used in the existing apparatus.

100 : 고분자응집제 유입관
110 : 소화슬러지 유입관
210 : 제1벤츄리관 211 : 밸브
212 : 혼합관 213 : 압력계
220 : 제2벤츄리관 230 : 교반부
231 : 교반탱크 232 : 모터
233 : 교반날개 240 : 배출관
300 : 탈수기100: polymer coagulant inlet tube
110: digested sludge inflow pipe
210: first venturi tube 211: valve
212 mixing tube 213 pressure gauge
220: second venturi 230: stirring section
231: stirring tank 232: motor
233: stirring blade 240: discharge pipe
300: dehydrator

Claims (3)

삭제delete 고분자응집제와 소화슬러지를 유입받아 유속을 증가시키는 제1벤츄리관;
상기 제1벤츄리관의 출구부에 설치되어 증가된 유속을 유입받아 캐비테이션을 발생시켜 고분자응집제와 소화슬러지를 혼합하는 혼합관;
상기 혼합관의 출구부에 설치된 제2벤츄리관;
상기 제2벤츄리관으로부터 유출되는 혼합액을 유입받아 캐비테이션을 발생시켜 고분자응집제와 소화슬러지를 연속 혼합하여 배출하며, 내측으로 교반날개가 인입되어 혼합액을 재차 교반하는 교반부를 갖는 교반탱크;로 구성된 것을 특징으로 하는 소화슬러지 응집장치
A first venturi tube for increasing the flow rate by introducing a polymer coagulant and a digested sludge;
A mixing tube installed at an outlet of the first venturi tube to generate an increased flow rate to generate cavitation to mix the polymer coagulant and the digested sludge;
A second venturi tube installed at an outlet of the mixing tube;
Receiving a mixed solution flowing out of the second venturi tube to generate a cavitation by continuously mixing and discharging the polymer coagulant and the digestive sludge, the stirring tank having an agitating portion to stir the mixed solution again by entering the stirring blade inside; Fire extinguishing sludge flocculator
제2항에 있어서, 상기 제1벤츄리관에는 유량조절밸브가 설치되어 있는 것을 특징으로 하는 소화슬러지 응집장치3. The fire extinguishing sludge flocculating apparatus according to claim 2, wherein the first venturi tube is provided with a flow control valve.
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KR200352785Y1 (en) 2004-03-20 2004-06-22 삼양정수공업 주식회사 Instantaneous intermixture apparatus with high efficiency
KR100791939B1 (en) 2006-12-26 2008-01-04 이양화학주식회사 Flocculation apparatus comprisimg horizontal agitating inverter pelletizing flocculation reactor
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FR3036698A1 (en) * 2015-05-29 2016-12-02 Orege METHOD AND DEVICE FOR PURIFYING DOMESTIC OR INDUSTRIAL WATER.
WO2016193600A1 (en) * 2015-05-29 2016-12-08 Orege Method and device for purifying domestic or industrial water
CN107667073A (en) * 2015-05-29 2018-02-06 奥里格公司 Family or industrial water purification method and equipment
US10442716B2 (en) 2015-05-29 2019-10-15 Orege Method and device for purifying domestic or industrial water
WO2017211542A1 (en) * 2016-06-08 2017-12-14 Veolia Water Solutions & Technologies Support Improved sludge dewatering process assisted by flocculating reactant and plant for the implementation of such a process
FR3052450A1 (en) * 2016-06-08 2017-12-15 Veolia Water Solutions & Tech IMPROVED FLOCULATING REAGENT ASSISTED SLUDGE DEHYDRATION PROCESS AND INSTALLATION FOR IMPLEMENTING SUCH METHOD.
KR20220007235A (en) * 2020-07-10 2022-01-18 이진필 Non-Screw Non-Propeller type High Speed In-line Mixer
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