KR100688036B1 - The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted - Google Patents

The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted Download PDF

Info

Publication number
KR100688036B1
KR100688036B1 KR1020060077348A KR20060077348A KR100688036B1 KR 100688036 B1 KR100688036 B1 KR 100688036B1 KR 1020060077348 A KR1020060077348 A KR 1020060077348A KR 20060077348 A KR20060077348 A KR 20060077348A KR 100688036 B1 KR100688036 B1 KR 100688036B1
Authority
KR
South Korea
Prior art keywords
coupled
bowl
sludge
rotor shaft
shaft
Prior art date
Application number
KR1020060077348A
Other languages
Korean (ko)
Inventor
김재선
Original Assignee
화양중공업 주식회사
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 화양중공업 주식회사 filed Critical 화양중공업 주식회사
Priority to KR1020060077348A priority Critical patent/KR100688036B1/en
Application granted granted Critical
Publication of KR100688036B1 publication Critical patent/KR100688036B1/en
Priority to PCT/KR2007/002075 priority patent/WO2008020674A1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/127Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B1/2016Driving control or mechanisms; Arrangement of transmission gearing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B2001/205Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl with special construction of screw thread, e.g. segments, height
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B2001/2083Configuration of liquid outlets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/20Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
    • B04B2001/2091Configuration of solids outlets
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/26Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Centrifugal Separators (AREA)

Abstract

A centrifugal dehydrator for extracting sludge without using a coagulant is provided to separate and extract principal components of the sludge such as celluloid, minerals and oil and fat constituents through a plurality of diaphragm parts by using a specific gravity difference of the principal components of the sludge. A centrifugal dehydrator for extracting sludge without using a coagulant comprises: a bowl(1) which is formed as a cylindrical cross-sectional shaped member and has four crushing projections(14) longitudinally projected to four directions from an inner circumference thereof, and into which the screw conveyor is connected; a rotary vane(20) formed on an outer side of the screw conveyor such that the rotary vane has 1 mm or less of a tolerance with the crushing projections and 1 to 3 mm of a tolerance with the inner circumference of the bowl; a first rotor shaft(11) connected to one side of the bowl; a first screw shaft(12) connected into the first rotor shaft; a second rotor shaft(21) connected to the other side of the bowl; a second screw shaft(22) connected into the second rotor shaft; a screw conveyor(2) in which a centrifugal rod connecting hole(23) is formed, and which is connected into the first screw shaft and the second screw shaft; a centrifugal rod(3) slid into the centrifugal rod connecting hole from an outer side of the first rotor shaft; and a first pulley(41) and a second pulley(42) respectively connected onto the first rotor shaft and the second rotor shaft.

Description

응집제를 사용하지 않고 슬러지가 추출되는 원심탈수기{THE CENTRIFUGAL DEHYDRATOR WHICH DOES NOT USE A COAGULANT AND IN WHICH THE SLUDGE IS EXTRACTED}CENTRIFUGAL DEHYDRATOR WHICH DOES NOT USE A COAGULANT AND IN WHICH THE SLUDGE IS EXTRACTED}

도 1은 본 발명의 결합상태 정단면도1 is a cross-sectional view of the coupling state of the present invention

도 2는 도 1의 분리상태도Figure 2 is an isolated state of Figure 1

도 3a은 제 1로터샤프트 측면도3A is a side view of the first rotor shaft

도 3b는 제 1로터샤프트의 사시도3b is a perspective view of the first rotor shaft;

도 4a는 제 2로터샤프트의 측면도4A is a side view of the second rotor shaft

도 4b는 제 2로터샤프트의 사시도4b is a perspective view of the second rotor shaft;

도 5는 종래의 원심분리기 작동상태도5 is a conventional centrifuge operating state diagram

<도면의 주요 부분에 대한 부호의 설명><Explanation of symbols for the main parts of the drawings>

1-보올 2-스크류컨베이어1-Ball 2-Screw Conveyor

3-원심봉 11-제 1로터샤프트3-centrifugal rod 11-first rotor shaft

12-제 1스크류샤프트 14-분쇄턱12-first screw shaft 14-crushing jaw

20-회전날개 21-제 2로터샤프트 20-swing vanes 21-second rotor shaft

22-제 2스크류샤프트 23-원심봉결합공22-second screw shaft 23-centrifugal rod coupling hole

24-판막 25-볼턱24-valve 25-ball jaw

26a,26b-격막부 27a,27b,27c-추출공26a, 26b-diaphragm 27a, 27b, 27c-hole

31-토출구 41-제 1풀리31-discharge outlet 41-first pulley

42-제 2풀리 43-제 3풀리42-second pulley 43-second pulley

44-제 4풀리 411,421-V밸트44-Fourth Pulley 411,421-V Belt

M1-제 1모터 M2-제 2모터M1-first motor M2-second motor

본 발명은 응집제를 필요로 하지 않는 슬러지 추출용 원심탈수기에 관한 것으로서 보다 상세하게는 원심봉의 토출구를 통하여 토출되어지는 슬러지가 스크류컨베이어의 내부 중앙에 형성된 판막의 볼턱으로 안내된 후 상기 스크류컨베이어와 상기 스크류컨베이어를 감싸는 보올이 각각 2500RPM으로 역회전되어 상기 슬러지가 비중차에 의하여 원심분리되는 것이며 상기와 같이 원심분리작업시 슬러지에 포함된 각 분자 중 비중이 경량인 셀룰로이드로부터 광섬유와 유지성분인 피지나 지방유등으로 각각 분리되어 서로 다른 격막부에 안내되고 상기와 같이 안내된 각 성분들은 상기 격막부의 외측으로 형성된 다수의 추출공을 통하여 스크류컨베이어의 외측으로 안내되어 상기 스크류컨베이어의 회전날개와 상기 스크류컨베이어를 감싸고 있는 보올의 내주연 및 상기 내주연으로부터 사방향에 돌출되어진 분쇄턱과의 공차에 의하여 상기 슬러지가 1㎜이하의 공차에 의하여 원심회전하면서 미세하게 분쇄되어지는 것으로서 상기와 같이 분쇄됨으로서 별도의 약품처리가 불필요하여 응집제가 원심탈수과정에서 전혀 투입되지 않아 유기질비료 등으로 사용이 가능한 매우 우수한 발명이다.The present invention relates to a sludge extraction centrifugal dehydrator that does not require a flocculant. More specifically, the screw conveyor and the sludge discharged through the discharge port of the centrifugal rod are guided to the sill of the valve formed in the inner center of the screw conveyor. As the bowl surrounding the screw conveyor is reversely rotated at 2500RPM, the sludge is centrifuged by the specific gravity difference. Separated by fat oil, etc., respectively, guided to different diaphragm parts, and each of the guided components as described above is guided to the outside of the screw conveyor through a plurality of extraction holes formed outside the diaphragm portion, the rotary blades of the screw conveyor and the screw conveyor Of the bowl which surrounds Due to the tolerance between the inner periphery and the grinding jaw protruding in the four directions from the inner periphery, the sludge is finely ground while being centrifugally rotated by a tolerance of 1 mm or less. Since the flocculant is not introduced at all in the centrifugal dehydration process, it is a very excellent invention that can be used as an organic fertilizer.

주지되는 바와 같이 종래에 사용되어 오던 대부분의 슬러지 추출방식은 주로 상,하수 수처리공정이나 축산폐수등을 처리하는 공정에서 발생하는 슬러지를 물리적인 원심력에 의하여 농축탈수 가능하도록 원심분리기에 주입하여 사용하는 것으로서 상기와 같이 제공되는 원심분리기는 주로 한국 특허등록 제 407896호에 기재된 것과 같이 스크류컨베이어의 구동에 따라 주입된 슬러지가 추출되어지는 것으로서 상기 원심분리기의 경우 슬러지에 함유되어 있는 물과 고형물을 회전하는 외동보올에 주입하여 적은 동력으로 원심력을 가함으로서 물과 고형물이 분리되는 것이며 상기와 같이 분리되는 상태에서 별도의 응집제가 투입되어 상당의 슬러지가 토출되어지는 것이다. As is well known, most of the sludge extraction methods that have been used in the past are mainly used by injecting sludge generated in water, sewage water treatment, livestock wastewater treatment, etc. into a centrifuge in order to concentrate and dehydrate by physical centrifugal force. As described above, the centrifuge provided as described above mainly extracts sludge injected according to the operation of a screw conveyor, as described in Korean Patent Registration No. 407896, wherein the centrifuge rotates water and solids contained in the sludge. Water and solids are separated by applying centrifugal force with little power by injecting into the external copper, and a separate flocculant is put in a state in which the sludge is discharged.

즉 상기한 바를 첨부된 도 5에 의하여 보다 상세히 설명하면 상기 원심분리기는 양측으로 구동모터가 형성되고 상기 구동모터로부터 각각의 풀리가 V밸트 결합되어 구동되어지되, 상기 우측에 도시된 슬러지투입관을 통하여 투입되는 슬러지는 스크류컨베이어의 내측으로 인입된 원심봉을 따라 인입되고 상기와 같이 인입된 슬러지가 스크류컨베이어의 내부막과 마찰되어 상기 슬러지가 스크류컨베이어의 추출공을 통하여 외부로 토출되어지는 것으로서 상기와 같이 토출작업이 진행시 슬러지의 응집력에 대한 문제점으로 인하여 별도의 응집제와 같은 약품이 첨가되어 작업상의 비능률은 물론 유기질비료로 사용하기에 곤란하게 되는 등의 문제점이 제기되는 것이다.That is, the centrifuge will be described in more detail with reference to the accompanying FIG. 5, wherein a driving motor is formed at both sides, and each pulley is driven by a V-belt coupled from the driving motor, and the sludge inlet tube shown on the right side is provided. The sludge introduced through the sludge is introduced along the centrifugal rod drawn into the screw conveyor, and the sludge introduced as described above is rubbed with the inner film of the screw conveyor, and the sludge is discharged to the outside through the extraction hole of the screw conveyor. Due to the problem of the cohesive force of the sludge during the discharge operation as described above, a problem such as the addition of a separate coagulant, such as inefficiency in the operation as well as difficult to use as an organic fertilizer is raised.

따라서 본 발명의 목적은 원통형상의 단면을 갖는 멤버로 형성되어진 보올의 내주연에 길이방향으로 4개의 분쇄턱이 사방향에서 돌설되어 상기 보올의 내측으로 스크류컨베이어가 결합되어지되, 상기 스크류컨베이어의 회전날개는 상기 분쇄턱과 1㎜이하의 공차를 갖도록 형성되고 보올의 내주연과는 1~2㎜이상의 공차를 갖도록 구성된 것을 본 발명의 목적으로 한다.Therefore, an object of the present invention is that four grinding jaws protruding in four directions in the longitudinal direction on the inner circumference of the bowl is formed of a member having a cylindrical cross-section, the screw conveyor is coupled to the inside of the bowl, the rotation of the screw conveyor It is an object of the present invention that the blade is formed to have a tolerance of 1 mm or less with the grinding jaw and configured to have a tolerance of 1 to 2 mm or more with the inner circumference of the bowl.

본 발명의 다른 목적은 슬러지의 입자가 비중차에 의하여 원심분리되어지도록 구성되는 원심분리기를 이용한 슬러지 추출장치로서 상기 슬러지의 주성분인 셀룰로이드와 광물질 및 유지성분 등이 비중차에 의하여 다수의 격막부를 통하여 비중차로 분할추출되어지는 것을 본 발명의 다른 목적으로 한다.Another object of the present invention is a sludge extraction device using a centrifuge which is configured to centrifuge the sludge particles by specific gravity difference, and the celluloid and minerals and oils, which are the main components of the sludge, through a plurality of diaphragms due to the specific gravity difference. It is another object of the present invention to be divided by specific gravity difference.

본 발명의 또 다른 목적은 케이싱의 내측으로 회전구동되어지는 보올과 스크류컨베이어가 각각 2500~3000RPM으로 회전되어지되, 상기 회전방향이 역방향으로 회전되어 그 회전가속도가 증강가능하게 형성되어지는 것을 본 발명의 또 다른 목적으로 한다.Another object of the present invention is that the bowl and the screw conveyor to be rotated to the inside of the casing is rotated at 2500 ~ 3000RPM, respectively, the rotational direction is rotated in the reverse direction is formed so that the rotational acceleration is augmented For another purpose.

이하 본 발명의 구성요소를 설명하면 다음과 같다.Hereinafter, the components of the present invention will be described.

케이싱의 내측으로 보올(1)과 스크류컨베이어(2)가 결합되어진 응집제를 사용하지 않고 0.1㎜ 이하로 슬러지가 추출되는 원심탈수기에 있어서, 상기 보올(1)은 원통형상의 단면을 갖는 멤버로 형성되어 상기 보올(1)의 내주연에 길이방향으로 4개의 분쇄턱(14)이 상,하,좌,우에 각각 돌설되어지며 상기 보올(1)의 내측으로 스크류컨베이어(2)가 결합되어지되, 상기 스크류컨베이어(2)의 회전날개(20)는 상기 분쇄턱(14)과 1㎜이하의 공차를 갖도록 형성되고 보올(1)의 내주연과는 1~3㎜이내의 공차를 갖도록 구성된 것이다.In the centrifugal dehydrator in which sludge is extracted to 0.1 mm or less without using a coagulant having the bowl 1 and the screw conveyor 2 coupled inside the casing, the bowl 1 is formed of a member having a cylindrical cross section. Four grinding jaw 14 in the longitudinal direction on the inner circumference of the bowl (1) is protruded in the upper, lower, left, right, respectively, screw conveyor (2) is coupled to the inside of the bowl (1), The rotary blade 20 of the screw conveyor 2 is formed to have a tolerance of 1 mm or less with the grinding jaw 14 and is configured to have a tolerance within 1 to 3 mm from the inner circumference of the bowl 1.

상기와 같이 구성된 보올(1)의 일측으로 제 1로터샤프트(11)가 결합되고 상기 제 1로터샤프트(11)의 내측으로 제 1스크류샤프트(12)가 결합되며 상기 보올(1)의 타측에는 제 2로터샤프트(21)가 결합되고 상기 제 2로터샤프트(21)의 내측으로 제 2스크류샤프트(22)가 결합되며, 상기 제 1스크류샤프트(12)와 제 2스크류샤프트(22)의 내측에는 길이방향으로 원심봉결합공(23)이 형성되어진 스크류컨베이어(2)가 결합되어지되, 상기 제 1로터샤프트(11)의 외측방향으로부터 원심봉(3)이 원심봉결합공(23)에 슬라이드 결합되어지고 상기 제 1로터샤프트(11)와 제 2로터샤프트(21) 축상에는 제 1풀리(41)와 제 2풀리(42)가 각각 결합되어진 것이며 상기 스크류컨베이어(2)의 원심봉결합공(23) 중앙에는 판막(24)이 형성되어지고 상기 판막(24)의 전면에는 반구형상의 볼턱(25)이 돌설되어 상기 원심봉결합공(23)에 결합되어진 원심봉(3)의 토출구(31)로부터 토출되는 슬러지가 상기 볼턱(25)으로 안내되어지도록 형성된 것이다.The first rotor shaft 11 is coupled to one side of the bowl 1 configured as described above, and the first screw shaft 12 is coupled to the inside of the first rotor shaft 11, and on the other side of the bowl 1. The second rotor shaft 21 is coupled and the second screw shaft 22 is coupled to the inside of the second rotor shaft 21, and the inner side of the first screw shaft 12 and the second screw shaft 22 is coupled. The screw conveyor (2) having the centrifugal rod coupling hole (23) formed in the longitudinal direction is coupled thereto, and the centrifugal rod (3) is inserted into the centrifugal rod coupling hole (23) from the outer direction of the first rotor shaft (11). The first pulley 41 and the second pulley 42 are coupled to each other on the shaft of the first rotor shaft 11 and the second rotor shaft 21, and the centrifugal rod coupling of the screw conveyor 2 is performed. A valve 24 is formed at the center of the ball 23, and a hemispherical ball jaw 25 is protruded on the front surface of the valve 24. The distal bar sludge discharged from the discharge port 31 of the centrifugal pin 3 been coupled to the coupling hole 23 is formed such that it is guided by the bolteok 25.

또한 상기 원심봉결합공(23)의 내측으로 다수의 격막부(26a),(26b)가 형성되고 상기 격막부(26a),(26b)의 외측으로 다수의 추출공(27a),(27b),(27c)이 스크류컨베이어(2)의 날과 날사이로 관통형성되어진 것이며 상기 제 1풀리(41)의 외측으로 제 1모터(M1)의 축상에 결합된 제 3풀리(43)가 V벨트(411)결합되어 보올(1)이 회전되고, 상기 제 2풀리(42)의 외측으로 제 2모터(M2)의 축상에 결합된 제 4풀 리(44)가 V벨트(421)결합되어 스크류컨베이어(2)가 회전되어지되, 상기 제 1모터(M1)와 제 2모터(M2)가 역방향으로 회전되어지는 것이다.In addition, a plurality of diaphragm portions 26a and 26b are formed inside the centrifugal rod coupling hole 23, and a plurality of extraction holes 27a and 27b are disposed outside the diaphragm portions 26a and 26b. (27c) is formed through the blade and the blade of the screw conveyor (2) and the third pulley (43) coupled to the shaft of the first motor (M1) to the outside of the first pulley (41) is a V belt ( 411) the bowl 1 is rotated, the fourth pulley 44 coupled to the shaft of the second motor (M2) to the outside of the second pulley 42 is coupled to the V belt 421 screw conveyor (2) is rotated, but the first motor (M1) and the second motor (M2) is rotated in the reverse direction.

이하 첨부된 도면에 의하여 본 발명의 구성요소를 설명하고자 한다.Hereinafter, the components of the present invention will be described with reference to the accompanying drawings.

도 1은 본 발명의 결합상태 정단면도를 도시한 것으로서 상기 도시된 것과 같이 하우징의 내측으로 보올(1)이 결합되고 상기 보올(1)의 내측으로 스크류컨베이어(2)가 결합되어지되, 상기 보올(1)의 내주연에는 사방향에 길이방향으로 분쇄턱(14)이 돌설되어 상기 분쇄턱(14)이 스크류의 외측에 나사산형상으로 형성되어진 회전날개(20)와 1㎜ 이하의 공차를 갖도록 형성되고 상기 분쇄턱(14)이 돌설되지 않은 내주연은 스크류컨베이어(2)의 회전날개(20)와 1~3㎜이내의 공차를 형성한 것으로서 상기와 같이 형성된 공차에 의하여 상기 원심봉(3)의 토출구를 통하여 토출되는 슬러지가 상기 화살표와 같이 볼턱(25)과 마찰되고 이때 상기 스크류컨베이어(2)와 보올(1)이 역회전하면서 원심분리작용이 발생하여 비중차에 의하여 다수의 격막부(26a),(26b)에 비중이 서로 상이한 분자가 안내되는 것이며 상기 격막부(26a),(26b)의 외측으로 형성된 추출공(27a),(27b),(27c)을 통하여 분자가 추출되어지고 상기 분자는 상기 분쇄턱(14)과 스크류컨베이어(2)의 회전날개(20) 사이의 공차에 의하여 미세하게 분쇄되어 일측에 도시된 추출공(13)을 통하여 추출되어지는 것이다.1 is a cross-sectional view showing a state in which the coupling state of the present invention, as shown above, the bowl 1 is coupled to the inside of the housing and the screw conveyor 2 is coupled to the inside of the bowl 1, but the bowl At the inner circumference of (1), the grinding jaw 14 protrudes in the longitudinal direction in the four directions so that the grinding jaw 14 has a tolerance of 1 mm or less with the rotary blade 20 formed in a thread shape on the outside of the screw. The inner periphery formed and the crushing jaw 14 is not protruding form a tolerance within the range of 1 to 3 mm with the rotary blade 20 of the screw conveyor 2. Sludge discharged through the discharge port of the friction friction with the ball jaw 25 as shown by the arrow at this time, the screw conveyor (2) and the bowl (1) is rotated in reverse centrifugal separation occurs due to the specific gravity difference (26a) and (b) share specific gravity Different molecules are guided and the molecules are extracted through the extraction holes 27a, 27b, and 27c formed outside the diaphragm portions 26a and 26b. It is finely pulverized by the tolerance between the rotary blades 20 of the screw conveyor 2 is to be extracted through the extraction hole 13 shown on one side.

도 2는 도 1의 분리상태도를 도시한 것으로서 제 1모터(M1)와 제 2모터(M2)로부터 동력이 전달되어지면서 상기 모터(M1),(M2)의 축상에 축설된 풀리(41),(42)가 상기 보올(1)과 스크류컨베이어(2)의 축상에 결합되어진 풀리(43),(44)와 V밸 트(411),(421) 결합되어 구동가능한 것이며 상기 보올(1)의 상측에 도시된 확대도는 상기 보올(1)의 내주연에 분쇄턱(14)이 돌설되어진 것을 확대도시한 것이다.FIG. 2 is a diagram illustrating a separated state of FIG. 1, in which power is transmitted from the first motor M1 and the second motor M2, and a pulley 41 formed on an axis of the motors M1 and M2. (42) is coupled to the pulley (43), (44) and V-belt (411, 421) coupled to the shaft of the bowl (1) and screw conveyor (2) and can be driven An enlarged view of the upper side shows an enlarged view of the crushing jaw 14 protruding from the inner circumference of the bowl 1.

도 3a는 제 1로터샤프트(11) 측면도를 도시한 것이고 도 3b는 제 1로터샤프트(11)의 사시도를 도시한 것으로서 상기 도시된 것과 같이 제 1로터샤프트(11)의 일측으로 풀리가 결합되어지고 타측에는 제 1스크류샤프트(12)가 축설결합되어져 풀리로부터 전달되는 동력이 보올(1)을 회전구동하는 것이며 도 4a는 제 2로터샤프트(21)의 측면도를 도시한 것이고 도 4b는 제 2로터샤프트(21)의 사시도를 도시한 것으로서 상기 도시된 것과 같이 상기 제 2로터샤프트(21)의 일측으로 풀리가 결합되어지고 타측에는 제 2스크류샤프트(22)가 축설결합되어져 풀리로부터 전달되는 동력이 스크류컨베이어(2)를 회전구동하는 것이다.FIG. 3a illustrates a side view of the first rotor shaft 11 and FIG. 3b illustrates a perspective view of the first rotor shaft 11, in which a pulley is coupled to one side of the first rotor shaft 11 as shown above. On the other side of the bearing, the first screw shaft 12 is installed in a row, and the power transmitted from the pulley rotates the bowl 1. FIG. 4A shows a side view of the second rotor shaft 21 and FIG. 4B shows a second view. As shown in the perspective view of the rotor shaft 21 as shown in the pulley is coupled to one side of the second rotor shaft 21 and the second screw shaft 22 is coupled to the other side is the power transmitted from the pulley The screw conveyor 2 is driven to rotate.

도 5는 종래의 원심분리기 작동상태도를 도시한 것으로서 상기 도시된 것과 같이 원심분리기는 양측으로 구동모터가 형성되고 상기 구동모터로부터 각각의 풀리가 V밸트 결합되어 구동되어지되, 상기 우측에 도시된 슬러지투입관을 통하여 투입되는 슬러지는 스크류컨베이어의 내측으로 인입된 원심봉을 따라 인입되고 상기와 같이 인입된 슬러지가 스크류컨베이어의 내부막과 마찰되어 상기 슬러지가 스크류컨베이어의 추출공을 통하여 외부로 토출되어지는 것으로서 상기와 같이 토출작업이 진행시 슬러지의 응집력에 대한 문제점으로 인하여 별도의 응집제와 같은 약품이 첨가되어 구성되어지는 것이다.Figure 5 shows a conventional state of the centrifuge as shown in the centrifuge as shown above the drive motor is formed on both sides and each pulley from the drive motor is driven by the V belt coupled, the sludge shown on the right The sludge introduced through the input pipe is introduced along the centrifugal rod drawn into the screw conveyor. The sludge introduced as described above is rubbed with the inner film of the screw conveyor, and the sludge is discharged to the outside through the extraction hole of the screw conveyor. As a result, as described above, due to the problem of the cohesive force of the sludge during the discharging operation as described above, a drug such as a separate coagulant is added.

이하 본 발명의 효과를 설명하고자 한다.Hereinafter will be described the effects of the present invention.

보올의 내주연을 따라 사방향에 분쇄턱을 돌설함으로서 상기 스크류샤프트의 회전날개와 상기 분쇄턱과의 공차 및 상기 회전날개와 보올의 내주연 사이의 공차가 상이하게 형성되어 상기 보올과 스크류컨베이어가 회전시 비중차에 의하여 분할 추출된 슬러지입자가 원심력에 의하여 0.1㎜이하로 분쇄되어지는 것으로서 종래와 같이 별도의 응집제 투입이 필요없어 작업공정의 간소화 및 유기질비료로 활용이 가능한 효과를 제공한다.By protruding the grinding jaw in four directions along the inner circumference of the bowl, the tolerance between the rotary blade of the screw shaft and the crushing jaw and the tolerance between the inner circumference of the rotating blade and the bowl are differently formed. The sludge particles divided and extracted by the specific gravity during rotation are pulverized to 0.1 mm or less by centrifugal force, and thus, a separate flocculant is not required as in the prior art, thereby providing an effect that can be utilized as a simplification of the work process and organic fertilizer.

또한 종전과 같이 응집제를 넣어 사용하게 되는 경우 폐기물이 발생하여 상기 폐기물을 처리하는 과정상 해양투기가 빈번하게 사용되며 환경오염에 저해가 되는 등의 문제점이 해소되어 환경친화적인 효과가 발생하는 것이며 슬러지의 종류에 따라 함수율이 기존 슬러지에 비하여 30%가량 낮게 설정가능한 것이며, 한편 본 발명은 도면에 도시된 예를 참조로 설명되었으나 이는 예시적인 것에 불과하며 본 기술분야에서 통상의 지식을 가진 자라면 이로부터 다양한 변형이 가능한 것은 자명한 사실인 것이라 할 수 있다.In addition, when a flocculant is used as in the past, wastes are generated and marine dumping is frequently used in the process of treating the wastes, and problems such as impediment to environmental pollution are solved and environmentally friendly effects occur. Depending on the type of water content is set to be about 30% lower than the conventional sludge, while the present invention has been described with reference to the example shown in the drawings, but this is merely illustrative and those skilled in the art From the above, it is obvious that various variations are possible.

Claims (5)

케이싱의 내측으로 보올과 스크류컨베이어가 결합되어진 원심탈수기에 있어서,In the centrifugal dehydrator in which a bowl and a screw conveyor are coupled to the inside of the casing, 상기 보올(1)은 원통형상의 단면을 갖는 멤버로 형성되어 상기 보올(1)의 내주연에 길이방향으로 4개의 분쇄턱(14)이 상,하,좌,우 사방향에서 돌설되어지며 상기 보올(1)의 내측으로 스크류컨베이어(2)가 결합되어지되, 상기 스크류컨베이어(2)의 외측으로 형성되어지는 회전날개(20)는 상기 분쇄턱(14)과 1㎜이하의 공차를 갖도록 형성되고 보올(1)의 내주연과는 1~3㎜이내의 공차를 갖도록 구성되어지며, 상기 보올(1)의 일측으로 제 1로터샤프트(11)가 결합되고 상기 제 1로터샤프트(11)의 내측으로 제 1스크류샤프트(12)가 결합되며 상기 보올(1)의 타측에는 제 2로터샤프트(21)가 결합되고 상기 제 2로터샤프트(21)의 내측으로 제 2스크류샤프트(22)가 결합되며, 상기 제 1스크류샤프트(12)와 제 2스크류샤프트(22)의 내측에는 상기 원심봉결합공(23)이 형성되어진 스크류컨베이어(2)가 결합되어지되, 상기 제 1로터샤프트(11)의 외측방향으로부터 원심봉(3)이 원심봉결합공(23)에 슬라이드 결합되어지고 상기 제 1로터샤프트(11)와 제 2로터샤프트(21) 축상에는 제 1풀리(41)와 제 2풀리(42)가 각각 결합되어진 것을 특징으로 하는 응집제를 사용하지 않고 슬러지가 추출되는 원심탈수기.The bowl 1 is formed of a member having a cylindrical cross section so that four grinding jaws 14 in the longitudinal direction are protruded from the upper, lower, left, and right directions on the inner circumference of the bowl 1. Screw conveyor 2 is coupled to the inside of the (1), the rotary blade 20 is formed to the outside of the screw conveyor (2) is formed to have a tolerance of 1 mm or less with the grinding jaw (14) The inner periphery of the bowl 1 is configured to have a tolerance within 1 to 3 mm, the first rotor shaft 11 is coupled to one side of the bowl 1 and the inner side of the first rotor shaft 11. The first screw shaft 12 is coupled to the other side of the bowl (1) is coupled to the second rotor shaft 21 and the second screw shaft 22 is coupled to the inside of the second rotor shaft 21, On the inside of the first screw shaft 12 and the second screw shaft 22, the centrifugal rod coupling hole 23 is formed Conveyor (2) is coupled, the centrifugal rod (3) is slide-bonded to the centrifugal rod coupling hole (23) from the outer direction of the first rotor shaft (11) and the first rotor shaft (11) and the second A centrifugal dehydrator in which sludge is extracted without using a flocculant, characterized in that the first pulley (41) and the second pulley (42) are respectively coupled on the shaft of the rotor shaft (21). 삭제delete 제 1항에 있어서,The method of claim 1, 상기 스크류컨베이어(2)의 원심봉결합공(23) 중앙에는 판막(24)이 형성되어지고 상기 판막(24)의 전면에는 반구형상의 볼턱(25)이 돌설되어 상기 원심봉결합공(23)에 결합되어진 원심봉(3)의 토출구(31)로부터 토출되는 슬러지가 상기 볼턱(25)으로 안내되어지도록 형성된 것을 특징으로 하는 응집제를 사용하지 않고 슬러지가 추출되는 원심탈수기.A valve 24 is formed at the center of the centrifugal rod coupling hole 23 of the screw conveyor 2, and a hemispherical ball jaw 25 is protruded from the front side of the valve 24 to the centrifugal rod coupling 23. Centrifugal dehydrator to extract the sludge without using a flocculant, characterized in that the sludge discharged from the discharge port 31 of the combined centrifugal rod (3) is guided to the chin (25). 제 3항에 있어서,The method of claim 3, 상기 원심봉결합공(23)의 내측으로 다수의 격막부(26a),(26b)가 형성되고 상기 격막부(26a),(26b)의 외측으로 다수의 추출공(27a),(27b),(27c)이 스크류컨베이어(2)의 날과 날사이로 관통형성되어진 것을 특징으로 하는 응집제를 사용하지 않고 슬러지가 추출되는 원심탈수기.A plurality of diaphragm portions 26a and 26b are formed inside the centrifugal rod coupling hole 23, and a plurality of extraction holes 27a and 27b outside the diaphragm portions 26a and 26b are provided. A centrifugal dehydrator in which sludge is extracted without using a flocculant, characterized in that (27c) is penetrated between the blade and the blade of the screw conveyor (2). 제 3항에 있어서,The method of claim 3, 상기 제 1풀리(41)의 외측으로 제 1모터(M1)의 축상에 결합된 제 3풀리(43)가 V벨트(411)결합되어 보올(1)이 회전되고, 상기 제 2풀리(42)의 외측으로 제 2모터(M2)의 축상에 결합된 제 4풀리(44)가 V벨트(421)결합되어 스크류컨베이어(2)가 회전되어지되, 상기 제 1모터(M1)와 제 2모터(M2)가 역방향으로 회전되어지는 것을 특징으로 하는 응집제를 사용하지 않고 슬러지가 추출되는 원심탈수기.The third pulley 43 coupled to the shaft of the first motor M1 to the outside of the first pulley 41 is coupled to the V belt 411 so that the bowl 1 is rotated and the second pulley 42 is rotated. The fourth pulley 44 coupled to the shaft of the second motor M2 to the outside of the V belt 421 is coupled to the screw conveyor 2 is rotated, the first motor (M1) and the second motor ( A centrifugal dehydrator in which sludge is extracted without using a flocculant, wherein M2) is rotated in a reverse direction.
KR1020060077348A 2006-08-16 2006-08-16 The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted KR100688036B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
KR1020060077348A KR100688036B1 (en) 2006-08-16 2006-08-16 The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted
PCT/KR2007/002075 WO2008020674A1 (en) 2006-08-16 2007-04-27 A centrifugal dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020060077348A KR100688036B1 (en) 2006-08-16 2006-08-16 The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted

Publications (1)

Publication Number Publication Date
KR100688036B1 true KR100688036B1 (en) 2007-03-02

Family

ID=38102067

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020060077348A KR100688036B1 (en) 2006-08-16 2006-08-16 The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted

Country Status (2)

Country Link
KR (1) KR100688036B1 (en)
WO (1) WO2008020674A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100740608B1 (en) 2007-03-02 2007-07-18 (주)이화에코시스템 Sludge treatment apparatus with thickener and driersystem
KR100916032B1 (en) * 2007-11-20 2009-09-08 이자빈 Centrifugal hydroextractor for Submerged Sludge of Animal Waste Water
KR101422567B1 (en) 2014-03-12 2014-07-24 (주)이화에코시스템 Centrifugal separator comprising outlet
KR101428762B1 (en) * 2013-02-01 2014-08-12 덕산엔지니어링 주식회사 Centrifugal hydroextractor for sludge

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104556599B (en) * 2014-12-04 2016-05-25 浙江海洋学院 A kind of greasy dirt reclaims separating treatment technology
CN105435533B (en) * 2015-12-14 2017-07-14 无锡市永亿精密铸造有限公司 A kind of centrifugal separator for mud and water

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200316299Y1 (en) * 2003-02-27 2003-06-18 오인숙 screwtype centrifugal machine having dehydration promoting device for disposing of slurry
KR20030067632A (en) * 2003-07-25 2003-08-14 주식회사 무한기술 A centrifugal separator for sludge and oragnic effluents
KR20050017257A (en) * 2003-08-11 2005-02-22 김윤호 Hydroextractor
KR200407420Y1 (en) * 2005-11-15 2006-01-31 이기영 Centrifugal dehydrator
KR200411144Y1 (en) * 2005-12-12 2006-03-10 (주)이화에코시스템 Sludge Removal Centrifuge

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002224891A (en) * 2001-02-01 2002-08-13 Hitachi Zosen Corp Dewatering equipment for waste and method of operating the same
US6589154B2 (en) * 2001-05-30 2003-07-08 Alfa Laval Inc. Decanter centrifuge with a gear box mounted on the bowl

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200316299Y1 (en) * 2003-02-27 2003-06-18 오인숙 screwtype centrifugal machine having dehydration promoting device for disposing of slurry
KR20030067632A (en) * 2003-07-25 2003-08-14 주식회사 무한기술 A centrifugal separator for sludge and oragnic effluents
KR20050017257A (en) * 2003-08-11 2005-02-22 김윤호 Hydroextractor
KR200407420Y1 (en) * 2005-11-15 2006-01-31 이기영 Centrifugal dehydrator
KR200411144Y1 (en) * 2005-12-12 2006-03-10 (주)이화에코시스템 Sludge Removal Centrifuge

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100740608B1 (en) 2007-03-02 2007-07-18 (주)이화에코시스템 Sludge treatment apparatus with thickener and driersystem
KR100916032B1 (en) * 2007-11-20 2009-09-08 이자빈 Centrifugal hydroextractor for Submerged Sludge of Animal Waste Water
KR101428762B1 (en) * 2013-02-01 2014-08-12 덕산엔지니어링 주식회사 Centrifugal hydroextractor for sludge
KR101422567B1 (en) 2014-03-12 2014-07-24 (주)이화에코시스템 Centrifugal separator comprising outlet

Also Published As

Publication number Publication date
WO2008020674A1 (en) 2008-02-21

Similar Documents

Publication Publication Date Title
KR100688036B1 (en) The centrifugal dehydrator which does not use a coagulant and in which the sludge is extracted
KR101428762B1 (en) Centrifugal hydroextractor for sludge
KR101127015B1 (en) Centrifugal separator including agitating blade
US9517959B2 (en) Mixing apparatus for crushing sludge
JP2000509322A (en) Decantation centrifuge
CN111085009A (en) Traditional Chinese medicine extraction device
US2510781A (en) Centrifugal separator
KR100977196B1 (en) The separating screw decanter centrifuges having double acceleration discharging cover installed in screw conveyer
KR101869300B1 (en) Centrifuges with limiting turbulent formation of raw water
KR20170031149A (en) Centrifugal abatement separator
KR200319149Y1 (en) screw conveyor structured cylindrical centrifugal machine capable of separating minutely powdered solid
CN206457471U (en) A kind of extraction separation device of Moringa grease
KR100867762B1 (en) Centrifuge with screw for raising removal efficiency of micro-sludge
KR102188288B1 (en) Decanter type centrifugal dehydrator with increased dehydration efficiency using solid-liquid separator
US4147293A (en) Continuously operating solid-jacket counterflow centrifugal extractor
CN206996877U (en) Crystallization backwash centrifuge
KR20150103817A (en) a driving gear and a driver of a wastewater disposal machine
KR100773493B1 (en) A ball mill using the centrifugal force
CN108906344A (en) A kind of dynamical water-oil separating duplex centrifugal machine
JP4007674B2 (en) Centrifuge with power recovery function
US3658182A (en) Sludge centrifuge
JPS63194759A (en) Centrifugal dehydrator
KR950009309Y1 (en) Self-priming screw turbo pump
CN216191808U (en) Magnetic separation mechanism and recovery device for magnetic recovery
CN220346162U (en) Flotation device convenient to discharge for copper fine powder production

Legal Events

Date Code Title Description
A201 Request for examination
A302 Request for accelerated examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20130220

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20140321

Year of fee payment: 8

FPAY Annual fee payment

Payment date: 20150217

Year of fee payment: 9

FPAY Annual fee payment

Payment date: 20160222

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20170222

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20171220

Year of fee payment: 12

FPAY Annual fee payment

Payment date: 20190131

Year of fee payment: 13