WO2013047993A1 - Mixing apparatus for a water treatment facility - Google Patents

Mixing apparatus for a water treatment facility Download PDF

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Publication number
WO2013047993A1
WO2013047993A1 PCT/KR2012/006171 KR2012006171W WO2013047993A1 WO 2013047993 A1 WO2013047993 A1 WO 2013047993A1 KR 2012006171 W KR2012006171 W KR 2012006171W WO 2013047993 A1 WO2013047993 A1 WO 2013047993A1
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WO
WIPO (PCT)
Prior art keywords
mixing tank
inlet
raw water
impeller
mixing
Prior art date
Application number
PCT/KR2012/006171
Other languages
French (fr)
Korean (ko)
Inventor
허종형
임정호
Original Assignee
Hur Jong Hyung
Lim Jung Ho
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hur Jong Hyung, Lim Jung Ho filed Critical Hur Jong Hyung
Priority to CN201280041279.7A priority Critical patent/CN103826733B/en
Publication of WO2013047993A1 publication Critical patent/WO2013047993A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/86Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle
    • B01F27/861Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle the baffles being of cylindrical shape, e.g. a mixing chamber surrounding the stirrer, the baffle being displaced axially to form an interior mixing chamber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities

Definitions

  • the present invention relates to a water treatment plant admixture, and more particularly, to a water treatment plant admixture for injecting a flocculant into the raw water so as to aggregate various impurities and foreign substances contained in the raw water.
  • the mixing site of the water and sewage treatment plant undergoes a water treatment process in which chemicals are mixed into the raw water in order to aggregate various impurities or foreign substances contained in the incoming raw water.
  • the mixed area of the water and sewage treatment plant is a mixed water tank having an inlet and an outlet through the raw water, a coagulant injector installed to inject a coagulant into the raw water via the mixed water tank, and the coagulant and the raw water are mixed in the mixed water tank.
  • It is composed of a mixer having an impeller to rotate as possible. That is, the mixed place of the water and sewage treatment plant is introduced into the raw water introduced into the mixing tank through the inlet, the coagulant is introduced into the coagulant injector, and the coagulant and the raw water are mixed by rotating the impeller of the mixer, and then flowed out to the coagulant through the outlet.
  • the relatively simple structure makes it possible to mix the flocculant in the raw water.
  • the conventional mixing site of the water and sewage treatment plant physically mixes the flocculant and the raw water in the mixed water tank depending on the mixer having the impeller rotating in response to the external power supply.
  • the mixer is forcibly operated, which causes problems such as easy failure and increased electricity usage.
  • An object of the present invention is to provide a mixing apparatus for a water treatment plant that can increase the mixing efficiency of raw water and a flocculant.
  • the present invention is a cylindrical mixing tank provided with an inlet and an outlet through the raw water, a coagulant input line for introducing a coagulant into the inlet of the mixing tank, an impeller installed in the mixing tank so as to be axially rotatable, and the impeller is rotated.
  • a drive motor connected to the impeller to be driven, and installed at an inlet of the mixing tank, allowing the raw water to flow into the turbulent turbulent state while passing through the inlet, and the raw water and the inside of the mixing tank through the impeller rotation.
  • a blending apparatus for a water treatment plant including a rotary turbulence generating unit for increasing a blending ratio of a flocculant.
  • the rotary turbulence generating unit the fixed support disposed in the inner center of the mixing tank inlet, one end is coupled to the fixed support, the other end is coupled to each other along the circumferential direction of the mixing tank in the state coupled to the inside of the mixing tank It may be provided with a plurality of spaced apart, it may include an induction wing to be introduced into the rotary turbulent state into the mixing tank while inducing the raw water passing through the inlet to form a rotary water flow.
  • the fixing support may have a conical shape having a recess.
  • a rotary turbulence generating unit is installed at an inlet side in a state where an impeller is disposed inside the mixing tank, so that raw water flowing into the mixing tank is in a rotating turbulent state. Therefore, when the coagulant is introduced into the adjoining inlet of the mixing tank through the coagulant input line, the raw water in which the rotary turbulence is formed by the rotary turbulence generator meets the coagulant and is secondly rotated again by the impeller that is first mixed in the state of mixing. As it is mixed, the mixing efficiency is increased.
  • FIG. 1 is a cross-sectional view of an installation state of a water treatment plant according to an embodiment of the present invention.
  • FIG. 2 is a perspective view of the admixture for water treatment facilities shown in FIG. 1.
  • FIG. 2 is a perspective view of the admixture for water treatment facilities shown in FIG. 1.
  • FIG. 1 is a cross-sectional view of an installation state of a water treatment plant admixture according to an embodiment of the present invention
  • FIG. 2 is a perspective view of the water treatment plant admixture shown in FIG. 1.
  • the admixture device 100 for the water treatment facility includes a mixing tank 110, a coagulant input line 120, an impeller 130, a driving motor 140, and a rotary turbulence generating unit 150. Equipped with.
  • the mixing tank 110 is a cylindrical structure in which water treatment is performed while the raw water to be treated (hereinafter referred to as raw water) by the impeller 130 and the rotary turbulence generating unit 150 to be described later.
  • the mixing tank 110 may be installed on the water tank 10 into which the raw water flows. In this case, the raw water is introduced into the mixing tank 110, and then the inlet 111 to discharge the raw water mixed with the coagulant introduced from the coagulant input line 120 to be described later. And an outlet 112 is formed.
  • the inlet 111 side of the mixing tank 110 is connected to one end in the longitudinal direction of the coagulant input line 120 to be described later, the coagulant supplied from the coagulant input line 120 to the mixing tank 110.
  • Input hole 113 may be formed to be supplied into the inside.
  • the coagulant input line 120 is of a tubular shape into which the coagulant, which is mixed with the raw water in the mixing tank 110 and aggregates the impurities, fine particles and foreign matter contained in the raw water into the mixing tank 110. It is a connecting member. This, one end in the longitudinal direction of the flocculant input line 120 is connected to one side adjacent to the inlet 111 of the mixing tank 110, that is, connected to the input hole 113 of the mixing tank 110, the other end is It is connected to the storage tank (not shown) storing the flocculant.
  • the coagulant movement input into the mixing tank 110 in the storage tank through the coagulant input line 120 is connected to the coagulant input line 120 or the storage tank (not shown) )
  • the impeller 130 is rotated by the drive motor 140 to be described later in a state in which the axial rotation is installed inside the mixing tank 110.
  • the impeller 130 generates a suction discharge force so that the raw water is introduced through the inlet 111 of the mixing tank 110 and then discharged through the outlet 112.
  • the impeller 130 performs a function of rapidly mixing the flocculant and the raw water introduced from the flocculant input line 120.
  • the impeller 130 is connected to the drive motor 140 to be described later, the end of the drive shaft 131 in a state that is rotatably installed in the mixing tank 110 by the drive shaft 131, It is driven to rotate in accordance with the operation of the drive motor 140.
  • the impeller 130 may be configured to control the required number of revolutions in consideration of mixing conditions.
  • the drive motor 140 generates a rotational driving force to allow the impeller 130 to rotate inside the mixing tank 110.
  • the rotation shaft (not shown) of the driving motor 140 is connected to the driving shaft 131 of the impeller 130 to transmit the rotational force of the rotating shaft according to the operation to the driving shaft 131.
  • the drive motor 140 is configured to control the rotational speed of the impeller 130 as described above. As such, while the impeller 130 rotates inside the mixing tank 110 by the driving motor 140, the raw water and the flocculant are introduced into the mixing tank 110 through the inlet 111 of the mixing tank 110. After that, the discharge is made through the outlet 112 in a mixed state.
  • the rotary turbulence generating unit 150 allows the raw water introduced into the mixing tank 110 through the inlet 111 to enter the rotary turbulent state. That is, the rotary turbulence generating unit 150 is to rotate the raw water flowing into the mixing tank 110 into a turbulent turbulent state, and the flocculant in the mixing tank 110 by the impeller 130 and The miscibility increases.
  • the rotary turbulence generating unit 150 is installed in the inlet 111 of the mixing tank 110, and includes a fixed support 151 and the guide vane 153.
  • the fixed support 151 is a part supporting one end of the guide vane 153 to be described later.
  • the fixed support 151 is coupled to one end of the guide blade 153 in a state disposed in the inner center of the mixing tank 110, the inlet 111.
  • the fixed support 151 is coupled to the inside of the mixing tank 110 to maintain a stable support state that one end position of the induction blade 153 is not deformed according to the flow rate of the raw water flows in.
  • a support leg (not shown) may be provided. That is, one end in the longitudinal direction of the support leg is coupled to the mixing tank 110, the other end may be coupled to the fixed support 151.
  • the fixing support 151 may be formed in a conical shape having a concave portion 152.
  • the raw water is introduced through the inlet 111 of the mixing pipe 110, the raw water is introduced into the inlet 152 of the fixed support 151 after moving the raw water is lost due to the flow rate due to the collision It is suppressed that the rotation turbulence formation of the raw water by the guide blade 153 to be described later can be made efficiently.
  • the guide vane 153 forms a rotational speed while the raw water flowing in through the inlet 111 of the mixing tank 110 forms a rotational speed, and thus becomes a rotating turbulent state when introduced into the mixing tank 110.
  • the guide blades 153 are installed in plural to be spaced apart from each other along the circumferential direction of the mixing tank 110.
  • one end of each of the guide vanes 153 is fixedly coupled to the inside of the mixing tank 110 in the other end in a state that is fixedly coupled to the outside of the fixed support (151).
  • one end of the guide blade 153 may be hinged rotatably to adjust the tilt in a state connected to the outside of the fixed support (151).
  • the fixing means (not shown) for fixing in a state in which the inclination of the guide blade 153 is adjusted Of course it is equipped.
  • the guide vane 153 is disposed inclined at a predetermined angle with respect to the inflow direction of the raw water so as to collide with the incoming raw water.
  • the degree of inclination of the guide vane 153 is an angle capable of forming a large rotary turbulence while minimizing a decrease in flow rate of the raw water.
  • the installation angle of the guide vane 153 may be obtained through repeated experiments depending on the diameter of the mixing tank 110, the inlet 111, the size of the guide vane 153, and the number of installations.
  • the mixing device 110 is installed on the water tank 10 in which the raw water is stored. Subsequently, the impeller 130 is axially rotated inside the mixing tank 110 while operating by supplying power to the driving motor 140. At the same time, the flocculant is introduced into the mixing tank 110 through the flocculant input line 120.
  • the raw water in the mixing tank 110 is discharged through the outlet 112 by the impeller 130 is axially rotated in addition to the water level difference between the inflow water level and the outflow water level in the mixing tank 110.
  • the internal pressure of the mixing tank 110 is lowered to generate suction movement force so that the raw water can be continuously introduced through the inlet 111.
  • the mixing tank 110 is discharged through the outlet 112 in a state in which the raw water is mixed with the flocculant introduced from the flocculant input line 120 by the impeller 130.
  • the inlet 111 of the mixing tank 110 when the raw water is introduced through the inlet 111 of the mixing tank 110, while passing through the rotary turbulence generating unit 150 before mixing with the flocculant by the impeller 130, the inlet 111 Immediately after passing through), miscibility with the flocculant is achieved.
  • the raw water when the raw water is introduced through the inlet 111 of the mixing tank 110, the raw water is in a rotary turbulent state due to collision with the guide vanes 153 of the rotary turbulence generating unit 150, the flocculant Will be mixed with.
  • the raw water firstly mixed with the flocculant through the rotary turbulence generating unit 150 is mixed again while passing through the impeller 130, while the mixing efficiency of the raw water and the flocculant is increased. Discharge is made through the outlet 112.
  • the mixing apparatus 100 for the water treatment facility includes the rotary turbulence generating unit 150 at the inlet 111 in a state in which the impeller 130 is disposed inside the mixing tank 110.
  • the raw water flowing into the mixing tank 110 to be in a rotary turbulent state. Therefore, when the coagulant is introduced into the adjoining port 111 of the mixing tank 110 through the coagulant input line 120, the raw water in which the rotary turbulence is formed by the rotary turbulence generating unit 150 is The mixing efficiency is increased by the second mixing by the impeller 130 is rotated again in the state of mixing is first made while meeting the flocculant.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The present invention relates to a mixing apparatus for a water treatment facility, comprising: a cylindrical mixing tank having an inlet and an outlet such that raw water can pass therethrough; a condensate feeding line for feeding a condensate to the inlet of the mixing tank; an impeller installed inside the mixing tank to be capable of rotating on an axis; a driving motor connected to the impeller to drive and rotate the impeller; and a rotating turbulence generator installed at the inlet of the mixing tank, for inducing raw water to pass through the inlet and enter in the form of a rotating current, and improving the mixed ratio of raw water and condensate within the mixing tank through the rotation of the impeller. In this mixing apparatus for a water treatment facility, the rotating turbulence generator is installed at a side of the inlet in a state where the impeller is disposed within the mixing tank, and raw water entering the mixing tank is made to turbulently rotate. Accordingly, when condensate is fed through the condensate feeding line inside adjacent to the inlet of the mixing tank, raw water that is formed into a rotating current by the rotating turbulence generator meets the condensate so that a first mixing occurs, and then a second mixing occurs by rotating the mixture again by means of the impeller, to thereby increase mixing efficiency.

Description

수처리시설용 혼화장치Admixture for Water Treatment Facilities
본 발명은 수처리시설용 혼화장치에 관한 것으로서, 보다 상세하게는 원수에 포함된 각종 불순물이나 이물질을 응집되도록 원수에 응집제를 투입하는 수처리시설용 혼화장치에 관한 것이다.The present invention relates to a water treatment plant admixture, and more particularly, to a water treatment plant admixture for injecting a flocculant into the raw water so as to aggregate various impurities and foreign substances contained in the raw water.
상,하수처리장의 혼화지는 유입되는 원수에 포함하고 있는 각종의 불순물이나 이물질이 응집되도록 하기 위해서 그 원수에 약품을 혼화하여 주는 수처리 공정을 감당하게 된다.The mixing site of the water and sewage treatment plant undergoes a water treatment process in which chemicals are mixed into the raw water in order to aggregate various impurities or foreign substances contained in the incoming raw water.
이러한, 상,하수처리장의 혼화지는 원수가 경유하도록 유입구 및 유출구를 가지는 혼화수조와, 상기 혼화수조를 경유하는 원수에 응집제를 투입하도록 설치되는 응집제주입기와, 상기 혼화수조 내에서 응집제와 원수가 혼화되도록 회전동작하는 임펠러를 갖는 혼합기로 구성된다. 즉, 상기 상,하수처리장의 혼화지는 유입구를 통하여 혼화수조 내에 유입된 원수에 응집제주입기로 응집제를 투입하고, 응집제와 원수를 혼합기의 임펠러를 회전동작시켜서 혼화시킨 후 유출구를 통하여 응집지로 유출시키게 되므로, 비교적 간단한 구조로서 원수에 응집제를 혼화할 수 있게 한다.The mixed area of the water and sewage treatment plant is a mixed water tank having an inlet and an outlet through the raw water, a coagulant injector installed to inject a coagulant into the raw water via the mixed water tank, and the coagulant and the raw water are mixed in the mixed water tank. It is composed of a mixer having an impeller to rotate as possible. That is, the mixed place of the water and sewage treatment plant is introduced into the raw water introduced into the mixing tank through the inlet, the coagulant is introduced into the coagulant injector, and the coagulant and the raw water are mixed by rotating the impeller of the mixer, and then flowed out to the coagulant through the outlet. The relatively simple structure makes it possible to mix the flocculant in the raw water.
그러나, 종래의 상,하수처리장의 혼화지는 외부전원을 공급받아서 회전동작하는 임펠러를 갖는 혼합기에 의존하여 혼화수조 내의 응집제와 원수를 물리적으로 혼화시키는 바, 응집제와 원수의 혼화시간이 길어지고 응집제의 투입량이 증가될 뿐만 아니라, 혼합기를 무리하게 운용하게 되어서 쉽게 고장이 발생되고 전기사용량이 증가되는 등의 문제점이 발생된다.However, the conventional mixing site of the water and sewage treatment plant physically mixes the flocculant and the raw water in the mixed water tank depending on the mixer having the impeller rotating in response to the external power supply. In addition to the increased input amount, the mixer is forcibly operated, which causes problems such as easy failure and increased electricity usage.
더불어, 응집제의 투입지점을 임펠러에 떨어진 유입구에 설치하므로 반응시간이 극히 짧은 응집제의 특성상 신속하게 확산되어 반응하지 못하여 효율적인 응집 반응을 이루기가 어려워서 응집제의 투입량이 많아지고, 또한 교반기의 임펠라에 의하여 교반되는 원수의 량의 부피가 커서 효율적인 교반이 어려운 문제점이 있다.In addition, since the input point of the flocculant is installed at the inlet away from the impeller, it is difficult to achieve an efficient flocculation reaction due to the nature of the flocculant having a short reaction time, which is difficult to diffuse and react, resulting in a large amount of flocculant and agitation by the impeller of the stirrer. There is a problem that the efficient agitation is difficult because the volume of the amount of raw water is large.
본 발명은, 원수와 응집제의 혼화 효율을 높일 수 있는 수처리시설용 혼화장치를 제공하는데 목적이 있다.An object of the present invention is to provide a mixing apparatus for a water treatment plant that can increase the mixing efficiency of raw water and a flocculant.
본 발명은, 원수가 경유하도록 유입구 및 배출구가 마련된 원통형상의 혼화조와, 상기 혼화조의 유입구로 응집제를 투입하는 응집제투입라인과, 상기 혼화조 내부에 축회전 가능하게 설치되는 임펠러와, 상기 임펠러가 회전 구동되도록 상기 임펠러와 연결되는 구동모터 및, 상기 혼화조의 유입구에 설치되며, 상기 원수가 상기 유입구를 통과하면서 회전 난류상태로 유입되게 하면서, 상기 임펠러 회전을 통한 상기 혼화조 내부에서의 상기 원수 및 상기 응집제의 혼화율을 증대시키는 회전난류발생부를 포함하는 수처리시설용 혼화장치를 제공한다.The present invention is a cylindrical mixing tank provided with an inlet and an outlet through the raw water, a coagulant input line for introducing a coagulant into the inlet of the mixing tank, an impeller installed in the mixing tank so as to be axially rotatable, and the impeller is rotated. A drive motor connected to the impeller to be driven, and installed at an inlet of the mixing tank, allowing the raw water to flow into the turbulent turbulent state while passing through the inlet, and the raw water and the inside of the mixing tank through the impeller rotation. Provided is a blending apparatus for a water treatment plant including a rotary turbulence generating unit for increasing a blending ratio of a flocculant.
또한, 상기 회전난류발생부는, 상기 혼화조 유입구의 내부 중앙에 배치되는 고정지지대와, 일단은 상기 고정지지대에 결합되며, 타단은 상기 혼화조 내측에 결합된 상태로 상기 혼화조의 원주방향을 따라 상호 이격되게 복수 설치되어, 상기유입구를 통과하는 상기 원수가 회전수류를 형성하도록 유도하면서 상기 혼화조 내부로 회전 난류상태로 유입되게 하는 유도날개를 포함할 수 있다.In addition, the rotary turbulence generating unit, the fixed support disposed in the inner center of the mixing tank inlet, one end is coupled to the fixed support, the other end is coupled to each other along the circumferential direction of the mixing tank in the state coupled to the inside of the mixing tank It may be provided with a plurality of spaced apart, it may include an induction wing to be introduced into the rotary turbulent state into the mixing tank while inducing the raw water passing through the inlet to form a rotary water flow.
또한, 상기 고정지지대는 요입부를 가지는 원뿔형상일 수 있다.In addition, the fixing support may have a conical shape having a recess.
본 발명에 따른 수처리시설용 혼화장치는, 혼화조 내부에 임펠러를 배치한 상태에서 유입구 측에 회전난류발생부를 설치하여, 혼화조 내부로 유입되는 원수를 회전 난류상태가 되게 한다. 따라서, 응집제투입라인을 통해 혼화조의 유입구에 인접한 내부로 응집제를 투입시, 회전난류발생부에 의해 회전난류가 형성된 원수가 응집제와 만나면서 1차적으로 혼화가 이루어진 상태에서 다시 회전하는 임펠러에 의해 2차 혼화되는 바 혼화효율이 증대된다.In the mixing apparatus for water treatment facilities according to the present invention, a rotary turbulence generating unit is installed at an inlet side in a state where an impeller is disposed inside the mixing tank, so that raw water flowing into the mixing tank is in a rotating turbulent state. Therefore, when the coagulant is introduced into the adjoining inlet of the mixing tank through the coagulant input line, the raw water in which the rotary turbulence is formed by the rotary turbulence generator meets the coagulant and is secondly rotated again by the impeller that is first mixed in the state of mixing. As it is mixed, the mixing efficiency is increased.
도 1은 본 발명의 일실시예에 따른 수처리시설용 혼화장치의 설치상태 단면도이다.1 is a cross-sectional view of an installation state of a water treatment plant according to an embodiment of the present invention.
도 2는 도 1에 나타낸 수처리시설용 혼화장치의 사시도이다.FIG. 2 is a perspective view of the admixture for water treatment facilities shown in FIG. 1. FIG.
이하 첨부된 도면을 참조로 본 발명의 바람직한 실시예들을 상세히 설명하기로 한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명의 일실시예에 따른 수처리시설용 혼화장치의 설치상태 단면도이며, 도 2는 도 1에 나타낸 수처리시설용 혼화장치의 사시도이다. 도 1 및 도 2를 참조하면, 상기 수처리시설용 혼화장치(100)는, 혼화조(110), 응집제투입라인(120), 임펠러(130), 구동모터(140), 회전난류발생부(150)를 구비하고 있다.1 is a cross-sectional view of an installation state of a water treatment plant admixture according to an embodiment of the present invention, and FIG. 2 is a perspective view of the water treatment plant admixture shown in FIG. 1. 1 and 2, the admixture device 100 for the water treatment facility includes a mixing tank 110, a coagulant input line 120, an impeller 130, a driving motor 140, and a rotary turbulence generating unit 150. Equipped with.
상기 혼화조(110)는 이후 설명될 상기 임펠러(130) 및 상기 회전난류발생부(150)에 의해 수처리대상 원수(이하 원수로 기재)가 경유하면서 수처리가 이루어지는 원통형상의 구조물이다. 이러한, 상기 혼화조(110)는 상기 원수가 유입되는 수조(10) 상에 설치될 수 있다. 여기서, 상기 혼화조(110)에는 상기 수조(10)에서 상기 원수를 유입시킨 후, 이후 설명될 상기 응집제투입라인(120)으로부터 투입되는 응집제와 혼화된 상기 원수를 배출시킬 수 있도록 유입구(111) 및 배출구(112)가 형성된다. 또한, 상기 혼화조(110)의 유입구(111) 측에는 이후 설명될 상기 응집제투입라인(120)의 길이방향 일단이 연결되어, 상기 응집제투입라인(120)으로부터 공급되는 상기 응집제를 상기 혼화조(110) 내부로 공급할 수 있도록 투입공(113)이 형성될 수 있다.The mixing tank 110 is a cylindrical structure in which water treatment is performed while the raw water to be treated (hereinafter referred to as raw water) by the impeller 130 and the rotary turbulence generating unit 150 to be described later. The mixing tank 110 may be installed on the water tank 10 into which the raw water flows. In this case, the raw water is introduced into the mixing tank 110, and then the inlet 111 to discharge the raw water mixed with the coagulant introduced from the coagulant input line 120 to be described later. And an outlet 112 is formed. In addition, the inlet 111 side of the mixing tank 110 is connected to one end in the longitudinal direction of the coagulant input line 120 to be described later, the coagulant supplied from the coagulant input line 120 to the mixing tank 110. Input hole 113 may be formed to be supplied into the inside.
상기 응집제투입라인(120)은 상기 혼화조(110) 내부에서 상기 원수와 혼화되면서 상기 원수에 포함된 불순물, 미세입자 및 이물질을 응집시키는 응집제를 상기 혼화조(110) 내부로 투입하는 관 형상의 연결부재이다. 이러한, 상기 응집제투입라인(120)의 길이방향 일단은 상기 혼화조(110)의 유입구(111)에 인접한 일측, 즉 상기 혼화조(110)의 투입공(113)에 연결 결합되며, 타단은 상기 응집제를 저장한 저장탱크(도면미도시)에 연결 설치된다. 여기서, 상기 응집제투입라인(120)을 통한 상기 저장탱크에서 상기 혼화조(110) 내부로의 상기 응집제 이동 투입은, 상기 응집제투입라인(120) 또는 상기 저장탱크에 연결 설치되는 펌프(도면미도시)를 통해 이루어지게 된다.The coagulant input line 120 is of a tubular shape into which the coagulant, which is mixed with the raw water in the mixing tank 110 and aggregates the impurities, fine particles and foreign matter contained in the raw water into the mixing tank 110. It is a connecting member. This, one end in the longitudinal direction of the flocculant input line 120 is connected to one side adjacent to the inlet 111 of the mixing tank 110, that is, connected to the input hole 113 of the mixing tank 110, the other end is It is connected to the storage tank (not shown) storing the flocculant. Here, the coagulant movement input into the mixing tank 110 in the storage tank through the coagulant input line 120 is connected to the coagulant input line 120 or the storage tank (not shown) )
상기 임펠러(130)는 상기 혼화조(110) 내부에 축회전 가능하게 설치된 상태로 이후 설명될 상기 구동모터(140)에 의해 회전하게 된다. 이러한, 상기 임펠러(130)는 상기 혼화조(110)의 유입구(111)를 통해 상기 원수가 유입된 후 상기 배출구(112)를 통해 배출 이동될 수 있도록 흡입 배출력을 발생시킨다. 더불어, 상기 임펠러(130)는 상기 응집제투입라인(120)으로부터 투입되는 상기 응집제와 상기 원수를 급속 혼화시키는 기능을 수행하게 된다. 여기서, 상기 임펠러(130)는 구동축(131)에 의해 상기 혼화조(110) 내부에 축회전 가능하게 설치된 상태로 상기 구동축(131)의 단부가 이후 설명될 상기 구동모터(140)에 연결되어, 상기 구동모터(140)에 작동에 따라 회전 구동하게 된다. 이러한, 상기 임펠러(130)는 혼화조건을 고려하여 필요한 회전수를 제어할 수 있도록 구성될 수 있다.The impeller 130 is rotated by the drive motor 140 to be described later in a state in which the axial rotation is installed inside the mixing tank 110. The impeller 130 generates a suction discharge force so that the raw water is introduced through the inlet 111 of the mixing tank 110 and then discharged through the outlet 112. In addition, the impeller 130 performs a function of rapidly mixing the flocculant and the raw water introduced from the flocculant input line 120. Here, the impeller 130 is connected to the drive motor 140 to be described later, the end of the drive shaft 131 in a state that is rotatably installed in the mixing tank 110 by the drive shaft 131, It is driven to rotate in accordance with the operation of the drive motor 140. Such, the impeller 130 may be configured to control the required number of revolutions in consideration of mixing conditions.
상기 구동모터(140)는 상기 혼화조(110) 내부에서 상기 임펠러(130)가 회전할 수 있도록 회전 구동력을 발생시킨다. 이러한, 상기 구동모터(140)의 회전축(도면미도시)은 상기 임펠러(130)의 구동축(131)에 연결되어, 작동에 따른 상기 회전축의 회전력을 상기 구동축(131)으로 전달하게 된다. 여기서, 상기 구동모터(140)는 앞서 설명한 바와 같이 상기 임펠러(130)의 회전수를 제어할 수 있도록 구성된다. 이같이, 상기 구동모터(140)에 의해 상기 임펠러(130)가 상기 혼화조(110) 내부에서 회전하면서, 상기 원수 및 상기 응집제가 상기 혼화조(110)의 유입구(111)를 통해 내부로 유입된 후, 혼화상태로 상기 배출구(112)를 통해 배출이 이루어지게 된다.The drive motor 140 generates a rotational driving force to allow the impeller 130 to rotate inside the mixing tank 110. The rotation shaft (not shown) of the driving motor 140 is connected to the driving shaft 131 of the impeller 130 to transmit the rotational force of the rotating shaft according to the operation to the driving shaft 131. Here, the drive motor 140 is configured to control the rotational speed of the impeller 130 as described above. As such, while the impeller 130 rotates inside the mixing tank 110 by the driving motor 140, the raw water and the flocculant are introduced into the mixing tank 110 through the inlet 111 of the mixing tank 110. After that, the discharge is made through the outlet 112 in a mixed state.
상기 회전난류발생부(150)는 상기 유입구(111)를 통해 상기 혼화조(110) 내부로 유입되는 상기 원수가 회전 난류상태로 유입되게 한다. 즉, 상기 회전난류발생부(150)는 상기 혼화조(110) 내부로 유입되는 상기 원수를 회전 난류상태가 되도록 하여, 상기 임펠러(130)에 의한 상기 혼화조(110) 내부에서의 상기 응집제와 혼화효율이 증대되게 한다. 이러한, 상기 회전난류발생부(150)는 상기 혼화조(110)의 유입구(111)에 설치되는데, 고정지지대(151) 및 유도날개(153)를 포함한다.The rotary turbulence generating unit 150 allows the raw water introduced into the mixing tank 110 through the inlet 111 to enter the rotary turbulent state. That is, the rotary turbulence generating unit 150 is to rotate the raw water flowing into the mixing tank 110 into a turbulent turbulent state, and the flocculant in the mixing tank 110 by the impeller 130 and The miscibility increases. This, the rotary turbulence generating unit 150 is installed in the inlet 111 of the mixing tank 110, and includes a fixed support 151 and the guide vane 153.
상기 고정지지대(151)는 이후 설명될 상기 유도날개(153)의 일단을 지지하는 부분이다. 이러한, 상기 고정지지대(151)는 상기 혼화조(110) 유입구(111)의 내부 중앙에 배치된 상태로 상기 유도날개(153)의 일단이 결합된다. 여기서, 상기 고정지지대(151)는 유입되는 상기 원수의 유량에 따라 상기 유도날개(153)의 일단 위치가 변형되지 않는 안정적인 지지상태를 유지할 수 있도록 상기 혼화조(110)의 내측에 결합되는 복수의 지지다리(도면미도시)를 구비할 수도 있다. 즉, 상기 지지다리의 길이방향 일단은 상기 혼화조(110) 내측에 결합되며, 타단은 상기 고정지지대(151)에 결합될 수 있다.The fixed support 151 is a part supporting one end of the guide vane 153 to be described later. The fixed support 151 is coupled to one end of the guide blade 153 in a state disposed in the inner center of the mixing tank 110, the inlet 111. Here, the fixed support 151 is coupled to the inside of the mixing tank 110 to maintain a stable support state that one end position of the induction blade 153 is not deformed according to the flow rate of the raw water flows in. A support leg (not shown) may be provided. That is, one end in the longitudinal direction of the support leg is coupled to the mixing tank 110, the other end may be coupled to the fixed support 151.
더불어, 상기 고정지지대(151)는 요입부(152)를 가지는 원뿔형상으로 형성될 수 있다. 여기서, 상기 혼합배관(110)의 유입부(111)를 통해 상기 원수가 유입시, 상기 고정지지대(151)의 요입부(152)로 상기 원수가 인입된 후 이동게 하면서 충돌에 따른 유속이 손실되는 것을 억제시켜, 이후 설명될 상기 유도날개(153)에 의한 상기 원수의 회전난류 형성이 효율적으로 이루어질 수 있게 한다.In addition, the fixing support 151 may be formed in a conical shape having a concave portion 152. Here, when the raw water is introduced through the inlet 111 of the mixing pipe 110, the raw water is introduced into the inlet 152 of the fixed support 151 after moving the raw water is lost due to the flow rate due to the collision It is suppressed that the rotation turbulence formation of the raw water by the guide blade 153 to be described later can be made efficiently.
상기 유도날개(153)는 상기 혼화조(110)의 유입구(111)를 통해 유입되는 상기 원수가 회전수를 형성하면서, 상기 혼화조(110) 내부로 유입시에는 회전 난류상태가 되게 한다. 이러한, 상기 유도날개(153)는 상기 혼화조(110)의 원주방향을 따라 상호 이격되게 복수 설치된다. 여기서, 각각의 상기 유도날개(153) 일단은 상기 고정지지대(151) 외측에 고정 결합된 상태로 타단이 상기 혼화조(110)의 내측에 고정 결합된다. 이때, 상기 유도날개(153)의 일단은 상기 고정지지대(151) 외측에 연결된 상태에서 기울기를 조절할 수 있도록 회동 가능하게 힌지 결합될 수도 있다. 여기서, 상기 유도날개(153)의 일단이 상기 고정지지대(151) 외측에 회동 가능하게 결합될 경우에는, 상기 유도날개(153)의 기울기를 조절한 상태에서 고정시키는 고정수단(도면미도시)이 구비됨은 물론이다.The guide vane 153 forms a rotational speed while the raw water flowing in through the inlet 111 of the mixing tank 110 forms a rotational speed, and thus becomes a rotating turbulent state when introduced into the mixing tank 110. The guide blades 153 are installed in plural to be spaced apart from each other along the circumferential direction of the mixing tank 110. Here, one end of each of the guide vanes 153 is fixedly coupled to the inside of the mixing tank 110 in the other end in a state that is fixedly coupled to the outside of the fixed support (151). At this time, one end of the guide blade 153 may be hinged rotatably to adjust the tilt in a state connected to the outside of the fixed support (151). Here, when one end of the guide blade 153 is rotatably coupled to the outside of the fixed support 151, the fixing means (not shown) for fixing in a state in which the inclination of the guide blade 153 is adjusted Of course it is equipped.
여기서, 상기 유도날개(153)는 유입되는 상기 원수와 충돌되도록 상기 원수의 유입방향에 대해 일정각도로 기울어지게 배치된다. 여기서, 상기 유도날개(153)의 기울임 정도는 상기 원수의 유속감소를 최소화하면서 회전난류를 크게 형성할 수 있는 각도이다. 이러한 상기 유도날개(153)의 설치각도는 상기 혼화조(110) 유입구(111)의 직경 및 상기 유도날개(153)의 크기, 설치갯수에 따른 반복 실험을 통해 얻을 수 있음은 물론이다.Here, the guide vane 153 is disposed inclined at a predetermined angle with respect to the inflow direction of the raw water so as to collide with the incoming raw water. Here, the degree of inclination of the guide vane 153 is an angle capable of forming a large rotary turbulence while minimizing a decrease in flow rate of the raw water. The installation angle of the guide vane 153 may be obtained through repeated experiments depending on the diameter of the mixing tank 110, the inlet 111, the size of the guide vane 153, and the number of installations.
이와 같이 구성되는 일실시예에 따른 상기 수처리시설용 혼화장치(100)의 작동을 도 1 및 도 2를 참조하여 설명하면 다음과 같다.The operation of the admixture 100 for water treatment facilities according to an embodiment configured as described above will be described with reference to FIGS. 1 and 2.
먼저, 상기 혼화장치(110)는 상기 원수가 저장되는 상기 수조(10) 상에 설치된다. 이후, 상기 구동모터(140)에 전원을 공급하여 작동시키면서, 상기 임펠러(130)가 상기 혼화조(110) 내부에서 축회전되게 한다. 이와 동시에, 상기 응집제투입라인(120)을 통해 상기 혼화조(110) 내부로는 상기 응집제를 투입한다.First, the mixing device 110 is installed on the water tank 10 in which the raw water is stored. Subsequently, the impeller 130 is axially rotated inside the mixing tank 110 while operating by supplying power to the driving motor 140. At the same time, the flocculant is introduced into the mixing tank 110 through the flocculant input line 120.
그러면, 상기 혼화조(110)의 내부에서 유입수위와 유출수위의 수위차에 더해 축회전하는 상기 임펠러(130)에 의해 상기 혼화조(110) 내부의 상기 원수가 상기 배출구(112)를 통해 배출되면서, 상기 혼화조(110) 내부 압력이 낮아지며 상기 유입구(111)를 통해 상기 원수가 지속적으로 유입될 수 있게 흡입 이동력을 발생시킨다.Then, the raw water in the mixing tank 110 is discharged through the outlet 112 by the impeller 130 is axially rotated in addition to the water level difference between the inflow water level and the outflow water level in the mixing tank 110. In addition, the internal pressure of the mixing tank 110 is lowered to generate suction movement force so that the raw water can be continuously introduced through the inlet 111.
이때, 상기 혼화조(110) 내부에서는 상기 임펠러(130)에 의해 상기 원수가 상기 응집제투입라인(120)으로부터 투입된 상기 응집제와 혼화된 상태로 상기 배출구(112)를 통해 배출된다.At this time, the mixing tank 110 is discharged through the outlet 112 in a state in which the raw water is mixed with the flocculant introduced from the flocculant input line 120 by the impeller 130.
여기서, 상기 원수는 상기 혼화조(110)의 유입구(111)를 통해 유입시, 상기 회전난류발생부(150)를 통과하면서 상기 임펠러(130)에 의한 상기 응집제와의 혼화이전에 상기 유입구(111)를 지나면서 바로 상기 응집제와의 혼화가 이루어지게 된다. 즉, 상기 원수는 상기 혼화조(110)의 유입구(111)를 통해 유입될 때, 상기 회전난류발생부(150)의 각 유도날개(153)들과 충돌에 따른 회전난류상태가 되면서, 상기 응집제와의 혼화가 이루어지게 된다.Here, when the raw water is introduced through the inlet 111 of the mixing tank 110, while passing through the rotary turbulence generating unit 150 before mixing with the flocculant by the impeller 130, the inlet 111 Immediately after passing through), miscibility with the flocculant is achieved. In other words, when the raw water is introduced through the inlet 111 of the mixing tank 110, the raw water is in a rotary turbulent state due to collision with the guide vanes 153 of the rotary turbulence generating unit 150, the flocculant Will be mixed with.
이렇게, 상기 회전난류발생부(150)를 통과하여 상기 응집제와 1차적으로 혼화된 상기 원수는 다시 상기 임펠러(130)를 통과하면서 재차 혼화되면서, 상기 원수와 상기 응집제의 혼화효율이 증대된 상태로 상기 배출구(112)를 통해 배출이 이루어지게 된다.As such, the raw water firstly mixed with the flocculant through the rotary turbulence generating unit 150 is mixed again while passing through the impeller 130, while the mixing efficiency of the raw water and the flocculant is increased. Discharge is made through the outlet 112.
이와 같이, 일실시예의 상기 수처리시설용 혼화장치(100)는, 상기 혼화조(110) 내부에 상기 임펠러(130)를 배치한 상태에서 상기 유입구(111) 측에 상기 회전난류발생부(150)를 설치하여, 상기 혼화조(110) 내부로 유입되는 상기 원수를 회전 난류상태가 되게 한다. 따라서, 상기 응집제투입라인(120)을 통해 상기 혼화조(110)의 유입구(111)에 인접한 내부로 상기 응집제를 투입시, 상기 회전난류발생부(150)에 의해 회전난류가 형성된 상기 원수가 상기 응집제와 만나면서 1차적으로 혼화가 이루어진 상태에서 다시 회전하는 상기 임펠러(130)에 의해 2차 혼화되는 바 혼화효율이 증대된다.As described above, the mixing apparatus 100 for the water treatment facility according to the embodiment includes the rotary turbulence generating unit 150 at the inlet 111 in a state in which the impeller 130 is disposed inside the mixing tank 110. By installing, the raw water flowing into the mixing tank 110 to be in a rotary turbulent state. Therefore, when the coagulant is introduced into the adjoining port 111 of the mixing tank 110 through the coagulant input line 120, the raw water in which the rotary turbulence is formed by the rotary turbulence generating unit 150 is The mixing efficiency is increased by the second mixing by the impeller 130 is rotated again in the state of mixing is first made while meeting the flocculant.
본 발명은 도면에 도시된 실시예를 참고로 설명되었으나 이는 예시적인 것에 불과하며, 본 기술 분야의 통상의 지식을 가진 자라면 이로부터 다양한 변형 및 균등한 다른 실시예가 가능하다는 점을 이해할 것이다. 따라서, 본 발명의 진정한 기술적 보호 범위는 첨부된 특허청구범위의 기술적 사상에 의하여 정해져야 할 것이다.Although the present invention has been described with reference to the embodiments shown in the drawings, this is merely exemplary, and it will be understood by those skilled in the art that various modifications and equivalent other embodiments are possible. Therefore, the true technical protection scope of the present invention will be defined by the technical spirit of the appended claims.

Claims (3)

  1. 원수가 경유하도록 유입구 및 배출구가 마련된 원통형의 혼화조와;A cylindrical mixing tank provided with an inlet and an outlet through the raw water;
    상기 혼화조의 유입구로 응집제를 투입하는 응집제투입라인과;A coagulant input line for injecting a coagulant into the inlet of the mixing tank;
    상기 혼화조 내부에 축회전 가능하게 설치되는 임펠러와;An impeller rotatably installed in the mixing tank;
    상기 임펠러가 회전 구동되도록 상기 임펠러와 연결되는 구동모터; 및,A drive motor connected to the impeller so that the impeller is driven to rotate; And,
    상기 혼화조의 유입구에 설치되며, 상기 원수가 상기 유입구를 통과하면서 회전 난류상태로 유입되게 하면서, 상기 임펠러 회전을 통한 상기 혼화조 내부에서의 상기 원수 및 상기 응집제의 혼화율을 증대시키는 회전난류발생부를 포함하는 수처리시설용 혼화장치.Is installed in the inlet of the mixing tank, the rotary turbulence generating unit for increasing the mixing rate of the raw water and the flocculant in the mixing tank through the impeller rotation while allowing the raw water to flow into the rotating turbulent state while passing through the inlet Admixture for water treatment facility comprising.
  2. 청구항 1에 있어서,The method according to claim 1,
    상기 회전난류발생부는,The rotary turbulence generating unit,
    상기 혼화조 유입구의 내부 중앙에 배치되는 고정지지대와,A fixed support disposed in the inner center of the mixing tank inlet,
    일단은 상기 고정지지대에 결합되며, 타단은 상기 혼화조 내측에 결합된 상태로 상기 혼화조의 원주방향을 따라 상호 이격되게 복수 설치되어, 상기 유입구를 통과하는 상기 원수가 회전수류를 형성하도록 유도하면서 상기 혼화조 내부로 회전 난류상태로 유입되게 하는 유도날개를 포함하는 수처리시설용 혼화장치.One end is coupled to the fixed support, the other end is coupled to the mixing tank in a state in which a plurality of spaced apart from each other along the circumferential direction of the mixing tank, the raw water passing through the inlet to form a rotating water flow Mixing device for a water treatment plant comprising an induction blade to be introduced into the turbulent turbulent state into the mixing tank.
  3. 청구항 1에 있어서,The method according to claim 1,
    상기 고정지지대는 요입부를 가지는 원뿔형상인 수처리시설용 혼화장치.The fixed support is a conical device for water treatment facilities of the conical shape having a recess.
PCT/KR2012/006171 2011-09-30 2012-08-02 Mixing apparatus for a water treatment facility WO2013047993A1 (en)

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