KR20020096769A - Vacuum high pressure dehydrator with improved dewatering efficiency - Google Patents

Vacuum high pressure dehydrator with improved dewatering efficiency Download PDF

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KR20020096769A
KR20020096769A KR1020010035615A KR20010035615A KR20020096769A KR 20020096769 A KR20020096769 A KR 20020096769A KR 1020010035615 A KR1020010035615 A KR 1020010035615A KR 20010035615 A KR20010035615 A KR 20010035615A KR 20020096769 A KR20020096769 A KR 20020096769A
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South Korea
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vacuum
roller
sludge
water
dehydration
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KR1020010035615A
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Korean (ko)
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KR100406191B1 (en
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김용훈
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김용훈
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    • 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
    • C02F11/123Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/044Filters with filtering elements which move during the filtering operation with filtering bands or the like supported on cylinders which are pervious for filtering
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/44Regenerating the filter material in the filter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/24Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band
    • B30B9/241Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band co-operating with a drum or roller
    • 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
    • C02F11/14Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
    • C02F11/147Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents using organic substances
    • 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
    • C02F11/15Treatment of sludge; Devices therefor by de-watering, drying or thickening by treatment with electric, magnetic or electromagnetic fields; by treatment with ultrasonic waves
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • 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

Abstract

PURPOSE: A vacuum dehydrator for sludge dewatering is provided to efficiently remove water from wet sludge by installing a microwave generator for irradiating microwave to wet sludge in conventional vacuum dehydrator. CONSTITUTION: The vacuum dehydrator comprises a gravitational separation part(10) for removing water from the sludge; a first dehydration part(20) composed of a vacuum dewatering roller(24) formed by prominence and groove, and covered with a frame(22) of a microwave generating equipment(21) for irradiating microwave to disturb and decompose the particles of the sludge, to the grooves connecting pipes communicating with vacuum pipe are formed and to the opposite side valves are installed to supply vacuum by the actuation of press button pressed by filtration fabric(2); a second dehydration part(40) for advanced removal of water by discharge roller(42); a third dehydration part(50) composed of high vacuum roller(51), tension roller(52) and press roller, the high vacuum roller(51) formed by prominence and groove, to the grooves connecting pipes communicating with vacuum pipe are formed and to the opposite side press button are installed to supply vacuum by pressing of filtration fabric(2).

Description

탈수 효율을 높인 진공 고압 탈수기{omitted}Vacuum high pressure dehydrator with improved dewatering efficiency

본 발명은 하수처리장 또는 산업 현장 등에서 발생되는 폐수의 정화처리로 발생된 슬러지내의 수분을 제거하는 탈수기에 관한 것으로, 특히 탈수기의 탈수부를 이루는 제1탈수부,제2탈수부,제3탈수부(고압탈수부)를 구성하는 롤러의 구조를 개량함과 동시에 슬러지가 케익크 상태로 배출되는 시점까지 슬러지내의 수분을 진공흡입에 의한 분리 제거함은 물론, 제1탈수부의 진공흡입탈수롤러의 외주면으로 설치된 마이크로파발생장치로 슬러지의 입자를 교란 파괴시켜 슬러지내의 수분 분리가 원활하게 이루어질 수 있게 한 탈수효율을 높인 진공 고압 탈수기에 관한 것이다.The present invention relates to a dehydrator for removing water in the sludge generated by the purification of wastewater generated in sewage treatment plants or industrial sites, and more particularly, the first dehydration unit, the second dehydration unit, the third dehydration unit ( In addition to improving the structure of the roller constituting the high pressure dewatering part, the water in the sludge is separated and removed by vacuum suction until the sludge is discharged in the cake state, and is installed on the outer peripheral surface of the vacuum suction dewatering roller of the first dewatering part. The present invention relates to a vacuum high-pressure dehydrator with a dehydration efficiency that enables the water separation in the sludge to be made smoothly by disturbing and destroying the particles of the sludge with a microwave generator.

일반적으로 하수처리장 및 산업폐수에서 발생된 슬러지에 포함되어 있는 수분을 제거할 때에는 탈수기를 이용하여 수분을 슬러지로부터 분리 탈수시킨다.In general, when removing the water contained in the sludge generated in sewage treatment plants and industrial wastewater, the water is separated and dewatered from the sludge using a dehydrator.

상기 탈수기로 투입되어지는 슬러지에는 탈수조제(고분자 응집제)를 혼합기에서 참가한 다음, 슈트에 의해 슬러지가 여과포위에 균일하게 펼쳐진 상태로 공급되어 이송되어지게 되고, 상기 여과포에 도포 되어진 슬러지내의 수분이 중력에 의해 1차 제거되어지게 된다.The sludge to be introduced into the dehydrator participates in a dehydrating aid (polymer coagulant) in the mixer, and then the sludge is supplied and transported uniformly on the filter cloth by a chute, and the moisture in the sludge applied to the filter cloth is applied to gravity. By primary removal.

상기와 같이 여과포에서 슬러지의 수분이 제거되는 부위를 중력탈수부라 한다.As described above, the area from which the water of the sludge is removed from the filter cloth is called a gravity dehydration part.

상기와 같이 여과포에 실려진 상태에서 중력에 의해 수분이 자연 제거되어진슬러지는 여과포가 제1탈수부의 진공흡입롤러와 진공흡입롤러의 외주면으로 설치된 가압롤러를 지나면서 가압되어 수분이 분리됨과 동시에 슬러지로부터 분리되어진 수분은 진공흡입롤러로 흡입되어 2차 제거되어진다.As the sludge is naturally removed by gravity in the state loaded on the filter cloth as described above, the filter cloth is pressurized by passing through the vacuum suction roller of the first dewatering part and the pressure roller installed on the outer circumferential surface of the vacuum suction roller to separate the water from the sludge. The separated water is sucked into the vacuum suction roller and then removed secondarily.

제1탈수부에서 수분이 2차 제거되어진 슬러지는 제1탈수부와 제3탈수부(고압탈수부)의 사이에 위치하는 제2탈수부의 롤러들을 지나면서 수분이 3차 제거되어진다.The sludge from which the moisture is removed from the first dewatering portion is passed through the rollers of the second dehydration portion positioned between the first dehydration portion and the third dehydration portion (high pressure dewatering portion), and the water is removed three times.

제2탈수부에서 수분이 3차 제거되어진 슬러지는 제3탈수부로 이동하여 드럼롤러와 드럼롤러 외주면으로 가압롤러를 가지고 있고, 장력벨트로 이루어진 제3탈수부(고압탈수부)로 이동하여 마지막으로 수분이 탈수되어진 후 배출 처리하게 된다.The sludge from which moisture is removed from the second dehydration part is moved to the third dehydration part and has a pressure roller to the drum roller and the outer circumferential surface of the drum roller. The sludge is moved to the third dewatering part (high pressure dewatering part) made of a tension belt. After the water is dehydrated, it is discharged.

상기와 같와 같이 슬러지내의 수분을 제거하는 종래의 진공 고압 탈수기는 첫째, 여과포에 도포되어 이송되어지는 슬러지내의 수분을 진공흡입 제거하는 제1 탈수부의 진공흡입롤러가 통상의 관형태이고, 그 외주면에 수분을 진공 흡입할 수 있는 구멍들이 형성되어 있는 것이어서 여과포에 도포되어 이송되는 슬러지내의 수분 분리가 구멍과 일치하는 부위에서만 이루어져 진공흡입에 의한 탈수효율이 높지 못한 단점을 가지고 있고; 둘째, 제1탈수부에서만 슬러지내의 수분을 진공흡입 하고 나머지 제2탈수부와 제3탈수부(고압탈수부)에서는 가압력에 의해서만 수분이 제거되어지기 때문에 최종 슬러지 케익의 함수율이 높은 단점을 가지고 있으며; 셋째, 제1탈수부의 진공흡입롤러가 통상의 관형태이어서 진공이 이루어져야 하는 면적이 너무 커 진공펌프 가동시간이 길어질 뿐만 아니라 그에 따른 전기에너지의 손실이 많아지는 단점을 가지고 있고; 넷째, 최종 슬러지 케익크의 함수율이 높아 슬러지 소각에 따른 에너지 낭비와 매립시 토양 잠식과 침출수의 발생으로 인한 2차 토양 오염 및 수질 오염을 발생시키는 문제점이 있었다.As described above, the conventional vacuum high pressure dehydrator for removing the water in the sludge firstly, the vacuum suction roller of the first dewatering part for vacuum suctioning and removing the water in the sludge that is applied to the filter cloth and transported is in the form of a common tube, Since holes are formed to suck water in vacuum, water separation in the sludge applied and transported to the filter cloth is made only at a portion coinciding with the holes, so that dehydration efficiency by vacuum suction is not high. Second, the moisture content of the final sludge cake is high because vacuum is sucked in the sludge only in the first dewatering part and water is removed only by the pressing force in the remaining second and third dehydrating parts (high pressure dewatering part). ; Third, the vacuum suction roller of the first dewatering part is in the form of a conventional tube, so that the area where the vacuum should be made is too large and the vacuum pump operation time is long, and there is a disadvantage in that the loss of electrical energy increases accordingly; Fourth, the high water content of the final sludge cake has a problem of generating secondary soil pollution and water pollution due to energy waste and land erosion and leachate from landfill due to sludge incineration.

상기와 같은 종래 탈수기의 문제점을 해결하기 위하여 개발된 본 발명은, 자중 중력부와 제1탈수부, 제2탈수부, 제3탈수부(고압탈수부)로 이루어진 통상의 탈수기에 있어서, 제1탈수부의 마이크로파발생장치를 부설함과 동시에 제1,제2,제3 탈수부를 구성하는 롤러(드럼)의 구조를 개량한 것으로서, 첫째, 제1탈수부의 진공흡입탈수롤러의 외주면으로 설치된 마이크로파발생장치로 슬러지의 입자를 교란 및 파괴한 후, 파괴된 슬러지내의 수분을 분리해 냄으로서 탈수효율을 높일 수 있는 장점이 있고; 둘째, 제2탈수부에 흡입롤러 및 토출롤러를 두고 제3탈수부(고압탈수부)에 드럼을 고압진공롤러로 대체하므로서 최종 슬러지 케익크의 함수율을 현저하게 낮출수 있는 장점을 가지고 있으며, 셋째, 각 탈수부를 이루는 롤러의 진공면적이 적어 진공펌프 가동시간을 줄일 수 있을 뿐만 아니라 그에 따른 전기에너지의 손실을 줄일 수 있는 탈수효율을 높인 진공 고압 탈수기를 제공하는데 그 목적이 있다.The present invention developed to solve the problems of the conventional dehydrator as described above, in the conventional dehydrator consisting of a self-gravity portion, the first dehydration portion, the second dehydration portion, the third dehydration portion (high pressure dehydration portion), The structure of the roller (drum) constituting the first, second, and third dehydration parts at the same time as the installation of the microwave generating device of the dehydration part, firstly, the microwave generating device installed on the outer circumferential surface of the vacuum suction dewatering roller of the first dehydration part. After disturbing and destroying the particles of the sludge, there is an advantage that can increase the dehydration efficiency by separating the water in the destroyed sludge; Second, the suction roller and the discharge roller are placed in the second dewatering part, and the drum is replaced with the high pressure vacuum roller in the third dewatering part (high pressure dewatering part), which has the advantage of significantly lowering the water content of the final sludge cake. The purpose of the present invention is to provide a vacuum high pressure dehydrator with a high vacuum dehydration efficiency, which reduces the vacuum pump operation time and reduces the loss of electrical energy.

도1은 본 발명에 따른 탈수효율을 높인 진공 고압 탈수기의 구성도.1 is a block diagram of a vacuum high pressure dehydrator to increase the dehydration efficiency according to the present invention.

도2는 본 발명에 의한 진공 고압 탈수기의 제1탈수부 진공흡입탈수롤러를 발췌한 사시도.Figure 2 is a perspective view of the first dewatering vacuum suction dehydration roller of the high pressure vacuum dehydrator according to the present invention.

도3은 본 발명에 의한 진공 고압 탈수기의 제1탈수부 진공흡입탈수롤러를 측단면도.Figure 3 is a side cross-sectional view of the first dehydration unit vacuum suction dehydration roller of the vacuum high pressure dehydrator according to the present invention.

도4는 본 발명에 따른 진공 고압 탈수기의 제2탈수부 흡입롤러와 토출롤러를 예시한 단면도.4 is a cross-sectional view illustrating a second dewatering part suction roller and a discharge roller of a vacuum high pressure dehydrator according to the present invention;

도5는 본 발명에 따른 진공 고압 탈수기의 제3탈수부 고압진공롤러를 예시한 단면도.Figure 5 is a cross-sectional view illustrating a third dewatering unit high pressure vacuum roller of the vacuum high pressure dehydrator in accordance with the present invention.

※ 도면의 주요 부분에 사용된 부호 설명 ※※ Explanation of symbols used in the main part of the drawing ※

10 : 자중중력부 20 : 제1탈수부10: self-gravity unit 20: first dewatering unit

21 : 마이크로파발생장치 24 : 진공흡입탈수롤러21: microwave generator 24: vacuum suction dehydration roller

26,41a,42a,59 : 밸브 40 : 제2탈수부26, 41a, 42a, 59: valve 40: second dewatering part

41 : 흡입롤러 42 : 토출롤러41: suction roller 42: discharge roller

50 : 제3탈수부 51 : 고압진공롤러50: third dewatering part 51: high pressure vacuum roller

53 : 가압롤러53: pressure roller

상기 목적을 달성하기 위한 본 발명의 구성은, 하수처리장 또는 산업 현장등에서 발생되는 폐수의 정화처리로 발생된 슬러지내의 수분을 자중중력부(10)에서 제거하고, 자중 중력부에서 제거된 슬러지내의 수분을 제1탈수부에서 진공흡입시켜2차 제거하며, 제1탈수부로부터 이송되어지는 슬러지내의 수분을 3차 제거하는 제2탈수부와, 마지막으로 슬러지내의 수분을 제거하는 제3탈수부(고압탈수부)로 구성된 진공 탈수기에 있어서,The configuration of the present invention for achieving the above object is to remove the water in the sludge generated by the purification process of wastewater generated in sewage treatment plants or industrial sites, etc. in the self-gravity portion 10, the water in the sludge removed from the self-gravity gravity portion The second dewatering unit by vacuum suction in the first dewatering unit to remove the water in the sludge conveyed from the first dewatering unit, and the third dewatering unit (high pressure) to finally remove the water in the sludge. In the vacuum dehydrator consisting of a dehydration unit),

상기 자중중력부(10)에서 수분이 1차 제거되어진 슬러지내의 수분을 제거하는 제1탈수부(20)는,슬러지의 입자를 교란 파괴하는 마이크로파가 조사되는 마이크로파발생기(23)가 진공흡입탈수롤러(24)를 감쌀수 있게 형성되어 있는 프레임(22)상에 상하,좌우로 등간격을 이루며 설치되어서 있는 마이크로파발생장치(21)를 포함하고, 여과포가 지나가는 부위의 외주면이 요홈(25)과 돌기(30)가 연속반복되는 요철형상을 이루되, 요홈(25)에는 진공펌프에 의해 진공이 걸리는 진공관(27)에 연결된 연결관(28)이 일측으로 연결되어 있고, 연결관(28)이 연결된 반대쪽이 요홈(25)과 도통되어서 여과포(2)에 눌려지는 눌림버튼(29)의 눌림 작동으로 요홈(25)에 진공이 발생되어지게하여 슬러지내의 수분을 진공흡입 분리시키는 밸브(26)가 설치되어 있으며, 외주면의 돌기(30)는 속이 비워서 여과포(2)에 실려 이송되는 슬러지로부터 분리되어진 수분이 자중에 의하여 자연탈수되어질 수 있도록 표면에 탈수공(31)들이 형성되어 있고, 탈수공(31)을 통해 분리되어진 수분이 배출되어질 수 있도록 양측면에 배출공(32)이 형성되어 있는 것이다.In the first dehydration unit 20 for removing water in the sludge from which the water is first removed from the gravity unit 10, the microwave generator 23, which is irradiated with microwaves to disturb and destroy particles of the sludge, is vacuum suction dewatering roller. It includes a microwave generating device 21 is installed on the frame 22 formed to cover the 24, at equal intervals vertically and horizontally, the outer peripheral surface of the portion through which the filter cloth passes through the groove 25 and the projections. 30 is repeatedly formed in the concave-convex shape, the groove 25 is connected to one side of the connecting pipe 28 is connected to the vacuum tube 27 takes the vacuum by the vacuum pump, the connection pipe 28 is connected A valve 26 is installed on the opposite side to be connected to the groove 25 so that a vacuum is generated in the groove 25 by pressing the push button 29 pressed by the filter cloth 2 so that the water in the sludge is sucked and vacuumed. The projections 30 on the outer circumferential surface are Dehydration holes (31) are formed on the surface so that the water separated from the sludge conveyed in the filter cloth (2) is hollowed out and naturally dehydrated by its own weight, and the water separated through the dehydration holes (31) can be discharged. Discharge hole 32 is formed on both sides so that.

상기 제1탈수부(20)의 마이크로파발생장치(21)와 진공흡입탈수롤러(24)에 의해 수분이 2차 제거된 슬러지내의 수분을 흡입 또는 토출시켜 분리하는 제2탈수부(40)는 흡입롤러(41)와 토출롤러(42)가 교차하는 순서로 배치 설치되고, 외주면이 요홈(41a)(42a)과 돌기(41b)(42b)가 연속반복되는 요철형상으로서요홈(41a)(42a)에는 진공펌프에 의해 진공이 걸리는 진공관(41c)(42c)에 연결된 연결관(41d)(42d)이 일측으로 연결 설치되고, 연결관(41d)(42d)이 연결된 반대쪽이 요홈(41a)(42a)과 도통되어서 여과포(2)에 눌려지는 눌림버튼(41f)(42f)의 눌림 작동으로 개방되어 요홈(41a)(42a)에 진공을 일으켜 슬러지내의 수분을 진공흡입 분리시키거나 또는 공기를 토출시키는 밸브(41e)(42e)가 설치되어 있으며, 외주면의 돌기(41b)(42b)는 속이 비워서 여과포에 도포되어 이송되는 슬러지로부터 분리되어진 수분이 자연탈수되어질 수 있도록 표면에 탈수공(41g)(42g)들이 형성되어 있고, 탈수공을 통해 분리되어진 수분이 배출되어질 수 있도록 양측면에 배출공(41h)(42h)이 형성되어 있는 것이다.The second dewatering part 40 which sucks or discharges water in the sludge from which water is secondarily removed by the microwave generator 21 and the vacuum suction dewatering roller 24 of the first dewatering part 20 is suctioned. The grooves 41a and 42a are arranged in the order in which the roller 41 and the discharge roller 42 intersect, and the outer circumferential surface is a concave-convex shape in which the grooves 41a and 42a and the projections 41b and 42b are repeated repeatedly. ) Is connected to one side of the connecting pipe 41d, 42d connected to the vacuum tube 41c (42c) to be vacuumed by the vacuum pump, the other side is connected to the groove 41a (42d) connected to the connection pipe 41d (42d) ( 42a) is opened and is opened by the pressing operation of the pressing buttons 41f and 42f pressed by the filter cloth 2 to generate a vacuum in the grooves 41a and 42a to vacuum suction and separate the water in the sludge or discharge the air. Valves 41e and 42e are provided, and the projections 41b and 42b on the outer circumferential surface are hollowed out from sludge that is applied to the filter cloth and transported. Dehydration holes (41g) (42g) are formed on the surface so that the separated water can be naturally dehydrated, and discharge holes (41h) (42h) are formed on both sides so that the separated water is discharged through the dehydration hole. will be.

상기 제2탈수부(40)에서 수분이 3차 제거되어진 슬러지내의 수분을 고압 진공 제거하는 제3탈수부(50)는 고압진공롤러(51)의 외주면으로 텐션롤러(52)에 의해 장력이 유지되고, 배출쪽으로가면서 지름이 작은 가압롤러(53)에 의해 고압진공롤러(51)의 외주면으로 밀착되어지는 여러가닥의 고무벨트(54)와 고압진공롤러(51)의 사이를 지나면서 4차제거되어지되, 상기 고압진공롤러(51)는, 여과포(2)가 지나가는 부위의 외주면이 요홈(55)과 돌기(56)가 연속반복되는 요철형상으로, 요홈(55)에는 진공펌프에 의해 진공이 걸리는 진공관(57)에 연결된 연결관(58)이 일측으로 연결 설치되고, 연결관(58)이 연결된 반대쪽이 요홈(55)과 도통되어서 여과포(2)에 눌려지는 눌림버튼(60)의 눌림 작동으로 요홈(55)에 진공을 일으켜 슬러지내의 수분을 진공흡입 분리시키는 밸브(59)가 설치되어 있으며, 외주면의 돌기(56)는 속이 비워서 여과포(2)에 실려 이송되는 슬러지로부터 분리되어진 수분이 자연탈수되어질 수 있도록 표면에 탈수공(61)들이 형성되어 있고, 탈수공을 통해 분리되어진 수분이 배출되어질 수 있도록 양측면에 배출공(62)이 형성되어 있는 것을 특징으로 한다.The third dehydration part 50 for removing the moisture in the sludge from which the water is removed from the second dewatering part 40 under high pressure is maintained by the tension roller 52 at the outer circumferential surface of the high pressure vacuum roller 51. 4th removal while passing between the rubber belt 54 and the high pressure vacuum roller 51 of several strands which are in close contact with the outer circumferential surface of the high pressure vacuum roller 51 by the pressure roller 53 having a small diameter while going toward the discharge side. The high-pressure vacuum roller 51 is a concave-convex shape in which the outer circumferential surface of the portion where the filter cloth 2 passes is concave and convex in the groove 55 and the projection 56, and the groove 55 is vacuumed by a vacuum pump. The connecting tube 58 connected to the vacuum tube 57 is connected to one side, and the opposite side to which the connecting tube 58 is connected is connected to the recess 55 so that the pressing button 60 pressed by the filter cloth 2 is pressed. The valve 59 for causing vacuum in the groove 55 to vacuum suction and separate the water in the sludge is The projections 56 on the outer circumferential surface of the outer circumferential surface are formed with dehydration holes 61 formed on the surface thereof so that the water separated from the sludge carried on the filter cloth 2 can be naturally dehydrated. Characterized in that the discharge hole 62 is formed on both sides so that the water is discharged.

이하 본 발명의 바람직한 실시예를 명세서에 첨부된 도면을 참조하여 보다 상세하게 설명한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도1은 본 발명에 따른 탈수효율을 높인 진공 고압 탈수기의 구성도이고, 도2는 본 발명에 의한 진공 고압 탈수기의 제1탈수부 진공흡입탈수롤러를 발췌한 사시도이며, 도3은 본 발명에 의한 진공 고압 탈수기의 제1탈수부 진공흡입탈수롤러를 측단면도이다.1 is a configuration diagram of a vacuum high pressure dehydrator with a high dehydration efficiency according to the present invention, Figure 2 is a perspective view of the first dewatering unit vacuum suction dehydration roller of the vacuum high pressure dehydrator according to the present invention, Figure 3 is a present invention Is a side cross-sectional view of the first vacuum suction dewatering roller of the vacuum high pressure dehydrator.

도4는 본 발명에 따른 진공 고압 탈수기의 제2탈수부 흡입롤러와 토출롤러를 예시한 단면도이고, 도5는 본 발명에 따른 진공 고압 탈수기의 제3탈수부 고압진공롤러를 예시한 단면도 이다.4 is a cross-sectional view illustrating a second dewatering part suction roller and a discharge roller of the vacuum high pressure dehydrator according to the present invention, and FIG. 5 is a cross-sectional view illustrating the third dewatering part high pressure vacuum roller of the vacuum high pressure dehydrator according to the present invention.

도시된 바와 같이, 본 발명의 고압 탈수기에 폐수로부터 분리된 슬러지가 슈트(1)를 통해 여과포(2)에 도포되어 이송되어지게 된다.As shown, the sludge separated from the waste water in the high pressure dehydrator of the present invention is applied to the filter cloth (2) through the chute (1) to be transported.

상기와 같이 여과포에 도포되어 운반되는 슬러지는 자중중력부(10)를 지나면서 슬러지내에 포함되어 있는 수분이 자중에 의하여 1차 분리되어지게 된다.As described above, the sludge applied and transported to the filter cloth is separated from the water contained in the sludge by the own weight while passing through the self-gravity portion 10.

자중중력부(10)에서 수분이 1차 탈수된 슬러지는 제1탈수부(20)의 진공흡입 탈수롤러(24)와 마이크로파발생장치(21)를 지나면서 2차 탈수되어진다.The sludge from which water is first dehydrated in the gravity unit 10 is secondarily dehydrated while passing through the vacuum suction dehydration roller 24 and the microwave generator 21 of the first dehydration unit 20.

상기와 같이 여과포(2)에 도포된 슬러지가 제1탈수부(20)로 위치하여지면, 마이크로파발생장치(21)의 마이크로파발생기(23)로부터 조사되는 마이크로파에 의하여 슬러지의 입자가 교란 파괴되어 슬러지로부터 수분이 원활하게 분리되어진다.When the sludge coated on the filter cloth 2 is positioned as the first dewatering part 20 as described above, the particles of the sludge are disturbed and destroyed by the microwaves irradiated from the microwave generator 23 of the microwave generator 21. Moisture is separated from it smoothly.

상기와 같이 슬러지로부터 분리되어진 수분은 진공펌프(도시하지 않았음)에 의해 진공이 발생되어지는 진공흡입탈수롤러(24)에서 흡입 제거하게 된다.As described above, the water separated from the sludge is sucked and removed by the vacuum suction dehydration roller 24 in which a vacuum is generated by a vacuum pump (not shown).

상기 진공흡입탈수롤러(24)가 슬러지로부터 분리되어진 수분을 흡수하는 과정을 설명하면 다음과 같다.The vacuum suction dehydration roller 24 will be described as follows to absorb the water separated from the sludge.

상기 진공흡입탈수롤러(24)의 외주면으로 여과포(2)가 지나가면, 진공흡입탈수롤러(24)의 요홈(25)으로 설치된 밸브(26)중 여과포가 접촉되는 밸브(26)의 눌림버튼(29)이 눌려져 개방되어지게 되고, 나머지는 차단된 상태를 이루게 된다.When the filter cloth 2 passes through the outer circumferential surface of the vacuum suction dewatering roller 24, the push button of the valve 26 in which the filter cloth contacts the valve 26 installed as the groove 25 of the vacuum suction dewatering roller 24 ( 29) is pressed to open, the rest is blocked.

상기와 같이 여과포(2)에 의해 눌림버튼(29)이 눌린 밸브(26)는 진공펌프(도시하지 않았음)에 의해 진공상태를 이루는 진공관(27)과 연결관(28)으로 연통되어 있어 요홈(25)부위에 진공이 발생하게 되고, 진공이 발생된 요홈(25)부위에 위치하여진 여과포(2)내의 슬러지에 포함되어 있는 수분이 진공흡입 되어지게 된다.As described above, the valve 26 in which the push button 29 is pressed by the filter cloth 2 is in communication with the vacuum tube 27 and the connecting tube 28 which form a vacuum state by a vacuum pump (not shown). Vacuum is generated at the portion 25, and moisture contained in the sludge in the filter cloth 2 located at the recess 25 in which the vacuum is generated is sucked into the vacuum.

상기와 같이 진공흡입탈수롤러(24)의 외주면을 이루는 요홈(25)들로 설치되어진 밸브(26)들이 여과포(2)에 의해 지속적으로 작동되면서 요홈(25)에 진공이 발생하므로서 여과포(2)에 도포되어진 슬러지내의 수분을 연속하여 흡입 분리하게 된다.As described above, the valves 26 installed as the grooves 25 constituting the outer circumferential surface of the vacuum suction dewatering roller 24 are continuously operated by the filter cloth 2, so that vacuum is generated in the grooves 25 and thus the filter cloth 2. The water in the sludge applied to the suction is continuously separated.

한편, 속이 비워있는 돌기(30)에는 여과포(2)가 접촉되는 표면에 탈수공(31)이 형성되어 있어 여과포(2)가 돌기(30)를 지날때에는 슬러지내의 수분이 탈수공(31)을 통해 자연탈수되어 돌기(30)의 내부로 유입되어지게 되고, 돌기(30)의 내부로 유입된 분리수는 돌기(30)의 양쪽으로 위치하여 형성된 배출공(32)을 통해 배출처리되어 진다.On the other hand, in the hollow projection 30, a dehydration hole 31 is formed on the surface where the filter cloth 2 is in contact, and when the filter cloth 2 passes through the protrusion 30, the moisture in the sludge dehydrates the hole 31. Natural dehydration is introduced through the protrusion 30, and the separated water introduced into the protrusion 30 is discharged through the discharge holes 32 formed at both sides of the protrusion 30.

상기에서와 같이 제1탈수부(20)에서 2차 탈수되어진 여과포(2) 내의 슬러지는 제2탈수부(40)에서 3차 탈수되어진다.As described above, the sludge in the filter cloth 2 which is secondarily dewatered in the first dewatering part 20 is dewatered in the third part in the second dewatering part 40.

슬러지내의 수분을 3차 탈수시키는 제2탈수부(40)는 상기의 진공흡입탈수롤러(24)와 동일한 구성을 가지는 것으로서 압축공기의 흐름이 다른 흡입롤러(41)와 토출롤러(42)가 서로 교차되는 순서로 배치되어 있다.The second dewatering part 40 for dewatering the water in the sludge thirdly has the same configuration as the vacuum suction dewatering roller 24, and the suction roller 41 and the discharge roller 42 having different flows of compressed air are different from each other. It is arranged in the order of crossing.

상기와 같이 이루어진 제2탈수부(40)로 제1탈수부(20)를 빠져나온 여과포(2)가 진입하게 되면, 제2탈수부(40)의 흡입롤러(41)에 슬러지가 도포되어진 여과포(2)가 먼저 위치하게 되어 흡입롤러(41)의 요홈(41a)들로 설치되어진 밸브(41e)들 중 어느 하나의 눌림버튼(41f)를 여과포(2)가 눌러 밸브(41e)를 개방시키게된다.When the filter cloth 2 exiting the first dewatering part 20 enters the second dewatering part 40 made as described above, the sludge is coated on the suction roller 41 of the second dewatering part 40. (2) is positioned first to allow the filter cloth (2) to press the push button (41f) of any one of the valves (41e) installed in the grooves (41a) of the suction roller (41) to open the valve (41e). do.

상기와 같이 흡입롤러(41)의 요홈(41a)으로 설치되어진 밸브(41e)가 개방되어진 밸브(41e)는 진공관(41c)과 연결관(41d)에 의해 연결되어 있어 진공펌프에 의해 진공이 일어나는 진공압력에 의하여 요홈(41a)에 진공이 발생하게 되고, 요홈(41a)이 진공되어짐으로서 요홈(41a)부위에 위치한 여과포(2)에 도포되어진 슬러지내의 수분이 흡입 제거되어지게 되는 것이다.As described above, the valve 41e in which the valve 41e installed in the recess 41a of the suction roller 41 is opened is connected by the vacuum tube 41c and the connecting tube 41d, so that vacuum is generated by the vacuum pump. The vacuum is generated in the groove 41a by the vacuum pressure, and the moisture in the sludge applied to the filter cloth 2 positioned on the groove 41a is sucked out by vacuuming the groove 41a.

상기와 같이 밸브(41e)의 작동으로 슬러지내의 수분이 분리되어질때 돌기(41b)에 위치하는 슬러지내의 수분은 자중에 의하여 돌기(41b)의 표면으로 형성되어 있는 탈수공(41g)으로 중력 분리되어 돌기(41b)의 양측면으로 형성되어 있는 배출공(41h)으로 배출되어진다.As described above, when the water in the sludge is separated by the operation of the valve 41e, the water in the sludge located on the protrusion 41b is gravity-separated by the dehydration hole 41g formed on the surface of the protrusion 41b by its own weight. It is discharged | emitted by the discharge hole 41h formed in the both sides of the projection 41b.

상기와 같이 흡입롤러(41)에 의하여 수분이 흡입 제거되어진 슬러지는 흡입롤러(41)의 다음으로 설치되어진 토출롤러(42)에 이루게 되면 토출롤러(42)의 요홈(42a)으로 설치되어진 밸브(42e)의 눌림버튼(42f)이 여과포(2)에 눌려 개방되어지게 되고, 개방되어진 밸브(42a)로는 진공관(42c)과 연결되어진 연결관(42d)을 통해 진공압축공기가 토출되어져 요홈(42a)에 위치하는 슬러지내의 수분을 불어내어 제거하게 된다.As described above, when the sludge from which water is sucked and removed by the suction roller 41 is formed in the discharge roller 42 installed next to the suction roller 41, the valve installed as the groove 42a of the discharge roller 42 ( The push button 42f of 42e is pressed by the filter cloth 2 to open, and the vacuum valve air is discharged through the connecting pipe 42d connected to the vacuum pipe 42c to the opened valve 42a, and thus the groove 42a. Blow off the water in the sludge located in the).

이때 슬러지가 도포되어 있는 여과포(2)가 토출롤러(42)의 하부로 위치하여 수분의 제거가 가능한 것이다.At this time, the sludge is applied to the filter cloth (2) is located in the lower portion of the discharge roller 42 can remove the water.

상기 제2탈수부(40)는 전술한 바와 같이 작용하는 흡입롤러(41)와 토출롤러(42)가 서로 교차되는 순서로 연속 구성되어 있어 상기한 수분 분리과정이 연속반복되어진다.The second dewatering part 40 is configured in a continuous order in which the suction roller 41 and the discharge roller 42 which function as described above intersect with each other, so that the above-described water separation process is repeated continuously.

이상에서와 같이 제2탈수부(40)에서 수분이 3차 제거되어진 슬러지는 최종단계인 제3탈수부(50)에서 수분이 최종적으로 분리되어지게 된다.As described above, the sludge from which the water is removed from the second dewatering part 40 in the third step is finally separated from the third dewatering part 50 which is the final step.

상기 제3탈수부(50)의 고압진공롤러(51)의 외주면으로 여과포(2)가 지나가면, 고압진공롤러(51)의 요홈(55)으로 설치된 밸브(59)중 여과포가 접촉되는 밸브(59)의 눌림버튼(60)이 눌려져 개방되어지게 되고, 나머지는 차단된 상태를 이루게 된다.When the filter cloth 2 passes through the outer circumferential surface of the high pressure vacuum roller 51 of the third dewatering part 50, the valve that contacts the filter cloth of the valve 59 installed as the groove 55 of the high pressure vacuum roller 51 ( The pressing button 60 of 59 is pressed to open, and the rest is blocked.

상기와 같이 여과포(2)에 의해 눌림버튼(60)이 눌린 밸브(59)는 진공펌프(도시하지 않았음)에 의해 진공상태를 이루는 진공관(57)과 연결관(58)으로 연통되어 있어 요홈(55)부위에 진공이 발생하게 되고, 진공이 발생된 요홈(55)부위에 위치하여진 여과포(2)내의 슬러지에 포함되어 있는 수분이 진공흡입 되어지게 된다.As described above, the valve 59 in which the push button 60 is pressed by the filter cloth 2 is connected to the vacuum tube 57 and the connecting tube 58 which are in a vacuum state by a vacuum pump (not shown). The vacuum is generated at the 55 part, and the moisture contained in the sludge in the filter cloth 2 positioned at the recess 55 formed at the vacuum is sucked into the vacuum.

상기와 같이 고압진공롤러(24)의 외주면을 이루는 요홈(55)들로 설치되어진 밸브(59)들이 여과포(2)에 의해 지속적으로 작동되면서 요홈(55)에 진공이 발생하므로서 여과포(2)에 도포되어진 슬러지내의 수분을 연속하여 흡입 분리하게 된다.As described above, the valves 59 installed as the grooves 55 constituting the outer circumferential surface of the high pressure vacuum roller 24 are continuously operated by the filter cloth 2, so that vacuum is generated in the groove 55 so that the filter cloth 2 is applied to the filter cloth 2. The moisture in the applied sludge is continuously separated by suction.

한편, 속이 비워있는 돌기(56)에는 여과포(2)가 접촉되는 표면에 탈수공(61)이 형성되어 있어 여과포(2)가 돌기(56)를 지날때에는 슬러지내의 수분이 탈수공(61)을 통해 자중에 의하여 중력분리되어 돌기(56)의 내부로 유입되어지게 되고, 돌기(56)의 내부로 유입된 분리수는 돌기(56)의 양쪽으로 위치하여 형성된 배출공(62)을 통해 배출 처리되어 진다.On the other hand, the hollow projection 56 is formed with a dehydration hole 61 on the surface where the filter cloth 2 is in contact, and when the filter cloth 2 passes through the projection 56, the water in the sludge dehydrates the hole 61. Gravity-separated by its own weight is introduced into the projections 56, and the separation water introduced into the projections 56 is discharged through the discharge holes 62 formed at both sides of the projections 56. Lose.

한편, 고압진공롤러(51)의 외주면에 대하여 가압되어질 수 있도록 텐션롤러(52)에 의해 장력이 유지되어진 고무벨트(54)가 상기의 고압진공롤러(51)에 대하여 밀착되어질 수 있도록 설치되어진 가압롤러(53)에 의해 가압되어짐과 동시에 가압롤러(53)가 배출구 쪽으로 가면서 작은 지름를 가지는 것이어서 가압롤러(53)의 표면 압력차이에 의하여 가압력이 증대되는 것이다.On the other hand, the pressure is installed so that the rubber belt 54 is maintained in tension by the tension roller 52 to be pressed against the outer peripheral surface of the high pressure vacuum roller 51 is in close contact with the high pressure vacuum roller 51 At the same time being pressed by the roller 53, the pressing roller 53 has a small diameter as it goes toward the discharge port, so that the pressing force is increased by the surface pressure difference of the pressing roller 53.

상기된 바와 같이 본 발명의 탈수 효율을 높인 진공 고압 탈수기는, 자중 중력부와 제1탈수부, 제2탈수부, 제3탈수부(고압탈수부)로 이루어진 통상의 탈수기에 있어서, 제1탈수부(20)에 마이크로파발생장치(21)를 부설함과 동시에 제1,제2,제3 탈수부를 구성하는 롤러(드럼)의 구조를 개량한 것으로서, 제1탈수부(20)의 진공흡입탈수롤러(24)의 외주면으로 설치된 마이크로파발생장치(21)로 슬러지의 입자를교란 및 파괴한 후, 파괴된 슬러지내의 수분을 분리해 냄으로서 탈수효율을 높일 수 있는 가지고 있는점이고; 제2탈수부(40)에 수분을 흡입 제거하는 흡입롤러(41) 및 수분을 불어내어 제거하는 토출롤러(42)를 교차되는 순서로 배치 하고, 제3탈수부(50)(고압탈수부)에 드럼을 고압진공롤러(51)로 대체하므로서 최종슬러지 케익크의 함수율을 현저하게 낮출수 있는 장점을 가지고 있는 것이며; 각 탈수부를 이루는 롤러의 진공면적이 적어 진공펌프 가동시간을 줄일 수 있을 뿐만 아니라 그에 따른 전기에너지의 손실을 줄일 수 있는 매우 유용한 발명인 것이다.As described above, the vacuum high pressure dehydrator having the improved dehydration efficiency of the present invention is a first dewatering machine in a conventional dehydrator including a gravity unit, a first dehydration unit, a second dehydration unit, and a third dehydration unit (high pressure dehydration unit). The vacuum suction dewatering roller of the first dewatering part 20 is an improvement in the structure of the roller (drum) constituting the first, second, and third dewatering parts while providing the microwave generator 21 in the part 20. A disturbance and destruction of the sludge particles by the microwave generator 21 provided on the outer circumferential surface of (24), thereby separating the water in the destroyed sludge to increase the dehydration efficiency; The suction roller 41 which sucks and removes moisture to the second dehydration part 40 and the discharge roller 42 which blows and removes moisture are arranged in the order of crossing, and the third dehydration part 50 (high pressure dehydration part) By replacing the drum with the high-pressure vacuum roller 51 has the advantage that can significantly lower the water content of the final sludge cake; The vacuum area of the roller forming each dewatering part is not only can reduce the vacuum pump operating time, it is a very useful invention that can reduce the loss of electrical energy accordingly.

Claims (1)

하수처리장 또는 산업 현장 등에서 발생되는 폐수의 정화처리로 발생된 슬러지내의 수분을 제거하는 진공 탈수기에 있어서,In the vacuum dehydrator for removing the water in the sludge generated by the purification of wastewater generated in sewage treatment plants or industrial sites, 고분자 응집제가 혼합기에서 참가되어 슈트(1)에 의해 여과포에 도포된 슬러지의 수분이 자중에 의하여 1차제거되는 자중중력부(10)와;A self-gravity unit 10 in which a polymer coagulant participates in the mixer and the water of the sludge applied to the filter cloth by the chute 1 is first removed by its own weight; 상기 자중중력부(10)에서 수분이 1차 제거된 슬러지의 입자를 잘게 파괴하는 마이크로파가 조사되는 마이크로파발생기(23)가 진공흡입탈수롤러(24)를 감쌀수 있게 형성되어 있는 프레임(22)상에 상하,좌우로 등간격을 이루며 설치되어서 있는 마이크로파발생장치(21)를 포함하고, 여과포가 지나가는 부위의 외주면이 요홈(25)과 돌기(30)가 연속반복되는 요철형상을 이루되, 요홈(25)에는 진공펌프에 의해 진공이 걸리는 진공관(27)에 연결된 연결관(28)이 일측으로 연결되어 있고, 연결관(28)이 연결된 반대쪽이 요홈(25)과 도통되어서 여과포(2)에 눌려지는 눌림버튼(29)의 눌림 작동으로 요홈(25)에 진공이 발생되어지게하여 슬러지내의 수분을 진공흡입 분리시키는 밸브(26)가 설치되어 있으며, 외주면의 돌기(30)는 속이 비워서 여과포(2)에 실려 이송되는 슬러지로부터 분리되어진 수분이 자연탈수되어질 수 있도록 표면에 탈수공(31)들이 형성되어 있고, 탈수공(31)을 통해 분리되어진 수분이 배출되어질 수 있도록 양측면에 배출공(32)이 형성되어 있는 진공흡입탈수롤러(24)로 이루어진 제1탈수부(20)와;On the frame 22 in which the microwave generator 23, which is irradiated with microwaves for finely destroying the particles of sludge from which the moisture is first removed from the self-gravity unit 10, is wrapped around the vacuum suction dehydration roller 24. Including up and down, left and right at equal intervals, including a microwave generating device 21, the outer peripheral surface of the filter cloth passing portion forms a concave-convex shape in which the groove 25 and the projection 30 is repeated repeatedly, groove ( 25 is connected to one side of the connecting pipe 28 connected to the vacuum tube 27 to be vacuumed by the vacuum pump, the opposite side to which the connecting pipe 28 is connected to the groove 25 is pressed by the filter cloth (2) The valve 26 is installed to allow vacuum to be generated in the groove 25 by the depressing operation of the depressing button 29 to separate the vacuum suction and suction of the water in the sludge. Sludge transported in Dewatering holes 31 are formed on the surface so that the water separated from the water can be naturally dehydrated, and the suction hole 32 is formed on both sides so that the separated water is discharged through the dewatering hole 31. A first dewatering part 20 formed of a dehydration roller 24; 상기 제1탈수부의 마이크로파발생장치(21)와 진공흡입탈수롤러(24)에 의해수분이 2차 제거된 슬러지내의 수분을 흡입 토출시켜 분리할 수 있는 흡입롤러(41)와 토출롤러(42)가 교차되는 순서로 배치 설치되되, 상기 흡입롤러(41)와 토출롤러(42)는, 외주면이 요홈(41a)(42a)과 돌기(41b)(42b)가 연속반복되는 요철형상으로서 요홈(41a)(42a)에는 진공펌프에 의해 진공이 걸리는 진공관(41c)(42c)에 연결된 연결관(41d)(42d)이 일측으로 연결 설치되고, 연결관(41d)(42d)이 연결된 반대쪽이 요홈(41a)(42a)과 도통되어서 여과포(2)에 눌려지는 눌림버튼(41f)(42f)의 눌림 작동으로 개방되어 요홈(41a)(42a)에 진공을 일으켜 슬러지내의 수분을 진공흡입 분리시키거나 또는 공기를 토출시키는 밸브(41e)(42e)가 설치되어 있으며, 외주면의 돌기(41b)(42b)는 속이 비워서 여과포에 실려 이송되는 슬러지로부터 분리되어진 수분이 자연탈수되어질 수 있도록 표면에 탈수공(41g)(42g)들이 형성되어 있고, 탈수공을 통해 분리되어진 수분이 배출되어질 수 있도록 양측면에 배출공(41h)(42h)이 형성되어 있는 제2탈수부(40)와;The suction roller 41 and the discharge roller 42 capable of suctioning and separating the water in the sludge from which the moisture is secondarily removed by the microwave generator 21 and the vacuum suction dewatering roller 24 of the first dewatering part are provided. The suction rollers 41 and the discharge rollers 42 are disposed in the order of crossing, and the grooves 41a have an outer circumferential surface as an uneven shape in which the grooves 41a, 42a and the projections 41b, 42b are continuously repeated. In the 42a, connecting pipes 41d and 42d connected to the vacuum tubes 41c and 42c which are vacuumed by the vacuum pump are connected to one side, and the opposite side to which the connecting pipes 41d and 42d are connected is a recess 41a. Is opened by the pressing operation of the pressing buttons 41f and 42f, which are in contact with the 42a and pressed by the filter cloth 2, to create a vacuum in the grooves 41a and 42a to vacuum-induce and separate the water in the sludge or air. Valves 41e and 42e for discharging air are provided, and the protrusions 41b and 42b on the outer circumferential surface are hollowed out and transported on a filter cloth. Dehydration holes (41g) (42g) are formed on the surface so that the water separated from the rug can be naturally dehydrated, and discharge holes (41h) (42h) are formed on both sides so that the water separated through the dehydration holes can be discharged. A second dewatering part 40; 제2탈수부(40)에서 수분이 3차 제거되어진 슬러지내의 수분이 고압진공롤러(51)의 외주면으로 텐션롤러(52)에 의해 장력이 유지되고, 배출쪽으로가면서 지름이 작은 가압롤러(53)에 의해 고압진공롤러(51)의 외주면으로 밀착되어지는 여러가닥의 고무벨트(54)와 고압진공롤러(51)의 사이를 지나면서 4차제거되어지되, 상기 고압진공롤러(51)는, 여과포(2)가 지나가는 부위의 외주면이 요홈(55)과 돌기(56)가 연속반복되는 요철형상으로, 요홈(55)에는 진공펌프에 의해 진공이 걸리는 진공관(57)에 연결된 연결관(58)이 일측으로 연결 설치되고, 연결관(58)이 연결된 반대쪽이 요홈(55)과 도통되어서 여과포(2)에 눌려지는 눌림버튼(60)의 눌림 작동으로 요홈(55)에 진공을 일으켜 슬러지내의 수분을 진공흡입 분리시키는 밸브(59)가 설치되어 있으며, 외주면의 돌기(56)는 속이 비워서 여과포(2)에 실려 이송되는 슬러지로부터 분리되어진 수분이 자연탈수되어질 수 있도록 표면에 탈수공(61)들이 형성되어 있고, 탈수공을 통해 분리되어진 수분이 배출되어질 수 있도록 양측면에 배출공(62)이 형성되어서된 제3탈수부(50)로 구성된 것을 특징으로 하는 탈수 효율을 높인 고압 진공 탈수기.Moisture in the sludge from which the water is removed from the second dewatering part 40 is maintained by the tension roller 52 to the outer circumferential surface of the high pressure vacuum roller 51, and the pressure roller 53 having a small diameter goes toward the discharge side. By the four-way between the rubber belt 54 and the high pressure vacuum roller 51 which is in close contact with the outer circumferential surface of the high pressure vacuum roller 51 by being removed, the high pressure vacuum roller 51, the filter cloth The outer circumferential surface of the part where (2) passes is a concave-convex shape in which the concave groove 55 and the protrusion 56 are repeatedly repeated, and the concave groove 55 has a connecting pipe 58 connected to a vacuum tube 57 that is vacuumed by a vacuum pump. Connected to one side, the opposite side to which the connection pipe 58 is connected is conducted to the groove 55, the pressure of the push button 60 is pressed by the filter cloth (2) to create a vacuum in the groove 55 to draw moisture in the sludge A valve 59 for separating vacuum suction is installed, and the protrusion 56 on the outer circumferential surface is Dehydration holes 61 are formed on the surface so that the water separated from the sludge carried on the filter cloth 2 is emptied to be naturally dehydrated, and the discharge holes on both sides are discharged so that the separated water is discharged through the dewatering hole. High pressure vacuum dehydrator, the dehydration efficiency is improved, characterized in that consisting of a third dehydration unit 50 is formed 62).
KR10-2001-0035615A 2001-06-21 2001-06-21 Vacuum high pressure dehydrator with improved dewatering efficiency KR100406191B1 (en)

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CN103611354A (en) * 2013-11-29 2014-03-05 广西大学 Multistage filtering squeezer for cassava residues
CN107050971A (en) * 2017-03-30 2017-08-18 通山新知力环保设备机械厂(普通合伙) Roller is filtered in a kind of press filtration for belt type sludge filter press
KR101949946B1 (en) * 2018-10-01 2019-02-19 박윤규 Tube press sludge dewatering device
CN110294584A (en) * 2019-07-23 2019-10-01 中交上海航道勘察设计研究院有限公司 A kind of device and method that mud dystopy is reinforced using self weight consolidation
CN111544944A (en) * 2020-05-23 2020-08-18 李玲玲 Rolling belt type dehydrator capable of automatically adjusting tension of filter cloth

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KR20180060002A (en) 2016-11-28 2018-06-07 태인공업(주) Sludge dehydrator having high dehydrating efficiency
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KR100312612B1 (en) * 1998-12-05 2002-02-19 김주식 High pressure dehydrating system of sludge with vacuum roller and compression belt
KR20000041282A (en) * 1998-12-22 2000-07-15 이구택 Methof for dewatering of sludge
KR100330731B1 (en) * 1999-04-12 2002-04-03 한상배 Dewatering apparatus of sludge and dewaterer
KR20020078452A (en) * 2001-04-09 2002-10-18 대정엔바이로(주) Vacuum suction type sludge dewatering device using an electromagnetic heat source device and air pressurization

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CN103611354A (en) * 2013-11-29 2014-03-05 广西大学 Multistage filtering squeezer for cassava residues
CN107050971A (en) * 2017-03-30 2017-08-18 通山新知力环保设备机械厂(普通合伙) Roller is filtered in a kind of press filtration for belt type sludge filter press
KR101949946B1 (en) * 2018-10-01 2019-02-19 박윤규 Tube press sludge dewatering device
CN110294584A (en) * 2019-07-23 2019-10-01 中交上海航道勘察设计研究院有限公司 A kind of device and method that mud dystopy is reinforced using self weight consolidation
CN110294584B (en) * 2019-07-23 2024-02-02 中交上海航道勘察设计研究院有限公司 Device and method for consolidating sludge in different positions by utilizing dead weight
CN111544944A (en) * 2020-05-23 2020-08-18 李玲玲 Rolling belt type dehydrator capable of automatically adjusting tension of filter cloth

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