KR20020081007A - High pressure dehydrator with improved dehydration efficiency - Google Patents
High pressure dehydrator with improved dehydration efficiency Download PDFInfo
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- KR20020081007A KR20020081007A KR1020010020960A KR20010020960A KR20020081007A KR 20020081007 A KR20020081007 A KR 20020081007A KR 1020010020960 A KR1020010020960 A KR 1020010020960A KR 20010020960 A KR20010020960 A KR 20010020960A KR 20020081007 A KR20020081007 A KR 20020081007A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
- B01D33/62—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying
- B01D33/64—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by compression
- B01D33/642—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by compression by pressure belts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
- B01D33/62—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying
- B01D33/64—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by compression
- B01D33/646—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by compression by pressure rollers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
- B01D33/62—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying
- B01D33/66—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by gases or by heating
- B01D33/663—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by gases or by heating by direct contact with a fluid
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/123—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/15—Treatment of sludge; Devices therefor by de-watering, drying or thickening by treatment with electric, magnetic or electromagnetic fields; by treatment with ultrasonic waves
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Mechanical Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
본 발명은 하수처리장 또는 산업 현장 등에서 발생되는 폐수에 포함되어 있는 슬러지를 탈수하는 탈수기에 관한 것으로, 슬러지의 수분을 단계별로 제거하는 탈수기의탈수부중 제2탈수부와 제2탈수부를 개량하여 탈수효율을 높인 탈수기에 관한 것이다.The present invention relates to a dehydrator for dewatering sludge contained in wastewater generated in a sewage treatment plant or industrial site, and improving dewatering efficiency by improving a second dewatering part and a second dehydrating part of a dehydrating part of a dehydrator which removes water of sludge step by step. It is about the dehydrator which raised it.
일반적으로 하수처리장 및 산업폐수에서 발생된 슬러지에 포함되어 있는 수분을 제거할 때에는 탈수기를 이용하여 수분을 슬러지로부터 탈수시키게 된다.In general, when removing the water contained in the sludge generated from sewage treatment plants and industrial wastewater, the dehydrator is used to dehydrate the water from the sludge.
상기 탈수기로 투입되어지는 슬러지에는 탈수조제(고분자 응집제)를 혼합기에서 참가한 다음, 슈트에 의해 슬러지가 여과포위에 균일하게 펼쳐진 상태로 공급되어 이송되어지게 되고, 상기 여과포에 얹혀진 슬러지내의 수분이 중력에 의해 제거되어지게 되는데 상기와 같이 여과포에서 슬러지가 제거되는 부위를 중력탈수부라 한다.The sludge fed to 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 the chute, and the water in the sludge placed on the filter cloth is moved by gravity. The area where sludge is removed from the filter cloth as described above is called a gravity dehydration part.
상기와 같이 여과포에 실려진 상태에서 중력에 의해 수분이 자연 제거되어진 슬러지는 여과포가 제1탈수부의 가열롤러와 가압롤러들을 지나면서 열과 가압력에 의해 2차 제거되어지게 되고, 제1탈수부에서 수분이 2차 제거되어진 후 여과포에 의해 운반되는 슬러지는 제2탈수부의 드럼롤러와 이 드럼롤러의 외주면을 따라 배치 설치되어진 가압롤러들을 지나면서 슬러지에 함습되어 있는 수분을 탈수시킨다.Sludge which is naturally removed from the water by gravity in the state loaded on the filter cloth as described above, the filter cloth is secondly removed by heat and pressure while passing through the heating roller and the pressure roller of the first dewatering part, and the water in the first dewatering part The sludge conveyed by the filter cloth after this secondary removal is dewatered by passing the drum roller of the 2nd dehydration part and the pressure rollers arrange | positioned along the outer peripheral surface of this drum roller.
상기와 같와 같이 슬러지내의 수분을 제거하는 종래의 고압 탈수기는 첫째, 슬러지가 얹혀진 여과포가 제1탈수부의 가열롤러를 지날때 가열롤러의 열에 의해 수분을 가열하여 증발시킴과 동시에 가압롤러들의 가압력에 의해서만 수분을 제거하는 것이어서 수분 제거효율이 높지 못한 단점을 가비고 있고; 둘째, 가열롤러의 표면이 서서히 가열되는 것이어서 가열에 따른 전기에너지의 사용량이 많아지는 단점을 가지고 있을 뿐만 아니라 부식이 쉽게 발생함은 물론, 폴리프로필렌으로 제작된 여과포에 직접 열이 전달되므로 여과포의 경화현상으로 수명단축과 늘어나는 현상이 발생하는 단점을 가지고 있으며; 셋째, 제2탈수부의 운전부하를 가중시키게 되어 탈수 슬러지의 함수율이 높은 단점을 가지고 있고; 넷째, 기존 탈수방식으로 슬러지 탈수의 어려움이 많은 내부성 수분을 효과적으로 제거하지 못해 최종 탈 수 슬러지의 함수율이 높으며, 다섯째, 가열롤러가 제2탈수부를 지나 슬러지내의 수분이 제거될 때에도 1개의 드럼롤러와 1개의 텐션장치에 의해서 드럼롤러의 l/3정도만 감싸 탈수 하므로 텐션장치에 무리한 힘을 요구하여 실린더의 수명당축 및 롤러의 편심을 초래 고장의 원인이 되기도 함과 동시에 들럼롤러 탈수면적이 커서 압착효과가 낮으며 압력의 효율적 분배가 되지 않아 수분을 완전하게 탈수시키는데 어려움이 있고; 여섯째, 수분을 포함하는 슬러지를 소각 또는 매립하는데 따른 에너지 낭비와 매립에 의한 토양 잠식과 침출수의 발생으로 인한 2차 토양 오염 및 수질 오염을 발생시키는 문제점이 있었다.As described above, the conventional high pressure dehydrator for removing water in the sludge firstly evaporates and heats the water by the heat of the heating roller when the sludge-loaded filter cloth passes through the heating roller of the first dehydration part, and at the same time only by the pressing pressure of the pressure rollers. It has the disadvantage of removing water, so that the water removal efficiency is not high; Second, since the surface of the heating roller is gradually heated, not only has the disadvantage of increasing the amount of electrical energy due to heating, but also easily causes corrosion, and heat is transferred directly to the filter cloth made of polypropylene, thereby curing the filter cloth. Phenomena have shortcomings such as shortening of life span and lengthening phenomenon; Thirdly, the operating load of the second dewatering part is increased, and the water content of the dewatering sludge is high; Fourth, due to the existing dehydration method, the internal moisture of the sludge dehydration can not be effectively removed, so the water content of the final dewatered sludge is high. And only one third of the drum roller is dehydrated by one tensioning device, which requires excessive force on the tensioning device, which causes the cylinder's lifespan and roller eccentricity. Low compressive effect and inefficient distribution of pressure, making it difficult to dehydrate water completely; Sixth, there was a problem of generating secondary soil pollution and water pollution due to the energy waste and land erosion and the generation of leachate due to incineration or landfill sludge containing water.
상기와 같은 종래 탈수기의 문제점을 해결하기 위하여 안출된 본 발명은, 고무코팅된 제1탈수부의 메인롤러의 외주면에 마이크로파를 조사하여 슬러지의 입자를 파괴함과 동시에 슬러지를 가열시키는 마이크로파발생장치를 설치하고, 마이크로파발생장치에 의해 탈수되고 더워진 수분을 슬러지로부터 신속하게 분리시키는진공흡입장치가 설치되어 있으며, 제2탈수부의 드럼롤러의 외주면 양쪽으로 텐션롤러가 설치되어짐과 동시에 가알롤러들의 직경을 드럼롤러의 회전방향으로 가면서 작은 것을 채택함은 물론 슬러지로부터 분리되어 고무벨트의 틈 사이로 빠져나오는 수분을 흡인 제거할 수 있는 진공흡인관으로 이루어진 것으로서, 제1탈수부에서 슬러지의 파괴로 내부수성수분(슬러지내에 숨어 있는 물)을 탈수시키는 것이어서 탈수 효율의 향상으로 제2탈수부의 운전부하를 줄여 줄수 있을 뿐만 아니라, 탈수기 운전에 따른 운전비용을 절감할 수 있고, 슬러지의 입자만을 가열하는 방식이어서 여과포가 경화되어지는 현상을 방지하였을 뿐 아니라, 늘어짐을 방지할 수 있으며, 제2탈수부의 드럼롤러와 양쪽의 텐션장치 및 가압롤러에 의해 가압되어진 슬러지로부터 분리된 수분을 진공흡인관으로 빨아들이므로서 슬러지내 수분을 완전하게 제거할 수 있는 탈수효율을 높인 고압 탈수기를 제공하는데 그 목적이 있다.In order to solve the problems of the conventional dehydrator as described above, the present invention, by irradiating microwaves to the outer circumferential surface of the main roller of the rubber-coated first dewatering unit to install the microwave generator for heating the sludge while destroying the particles of the sludge And a vacuum suction device for quickly separating the dehydrated and heated water from the sludge by the microwave generator, and the tension rollers are installed on both outer circumferential surfaces of the drum roller of the second dewatering part, and at the same time, the diameter of the gaal rollers is drummed. It consists of a vacuum suction tube that adopts a small one while going in the rotational direction of the roller and separates the sludge from the sludge and sucks out the water flowing between the gaps of the rubber belt, and the internal aqueous moisture (sludge) due to the destruction of the sludge in the first dehydration part. Dehydration efficiency by dehydrating the water hiding inside) In addition to reducing the operating load of the second dewatering unit, it is possible to reduce the operating cost according to the operation of the dehydrator, and the method of heating only the particles of the sludge not only prevents the phenomenon that the filter cloth is hardened, but also prevents sagging. High pressure dehydrator which can remove water from sludge pressurized by drum roller of second dewatering part and sludge pressurized by both tensioning device and press roller by vacuum suction tube The purpose is to provide.
도1은 본 발명에 따른 탈수효율을 높인 고압 탈수기의 구성도.1 is a block diagram of a high pressure dehydrator to increase the dehydration efficiency according to the present invention.
도2는 본 발명에 의한 고압 탈수기의 제1탈수부를 발췌한 부분 사시도.Figure 2 is a partial perspective view of the first dewatering portion of the high pressure dehydrator according to the present invention.
도3은 본 발명에 의한 고압 탈수기의 제2탈수부의 텐션롤러에 고무벨트가 설치된 상태를 보인 예시도.Figure 3 is an exemplary view showing a state in which the rubber belt is installed on the tension roller of the second dewatering portion of the high-pressure dehydrator according to the present invention.
※ 도면의 주요 부분에 사용된 부호 설명 ※※ Explanation of symbols used in the main part of the drawing ※
2 : 제1탈수부 10 : 마이크로파발생장치2: first dewatering unit 10: microwave generator
11 : 메인롤러 12 : 방지벽11: main roller 12: prevention wall
13 : 프레임 14 : 마이크로파 발생기13: frame 14: microwave generator
4 : 제2탈수부 20 : 진공흡입장치4: second dewatering unit 20: vacuum suction device
21 : 흡입구멍 22 : 호스21: suction hole 22: hose
31 : 드럼롤러 32 : 가압롤러31: drum roller 32: pressure roller
33 : 아이들롤러 34,35 : 텐션롤러33: idle roller 34,35: tension roller
43a,35a : 고무벨트 36,37 : 진공흡입관43a, 35a: Rubber belt 36,37: Vacuum suction pipe
38 : 가압실린더 T : 틈38: pressurized cylinder T: gap
상기 목적을 달성하기 위한 본 발명의 구성은, 가정용 오수 및 산업폐수로부터 분리되어 탈수조제(고분자 응집제)가 혼합기에서 참가되어 슈트로 공급되면 슈트에 의해 슬러지가 여과포위에 균일하게 펼쳐진 상태로 공급되어 자중중력부에서 수분이 1차 제거되어지고, 자중 중력부에서 수분이 자연 제거된 슬러지는 메인롤로와 가압롤러들로 이루어진 제1탈수부에 의해 수분이 2차 제거되어진후, 제2탈수부를 거치면서 드럼롤러와 가압롤러들에 의해 수분을 3차에 걸쳐 제거하도록 되어 있다.The construction of the present invention for achieving the above object is separated from household sewage and industrial wastewater, the dehydrating aid (polymer coagulant) is supplied in the mixer and supplied to the chute, the sludge is supplied uniformly spread over the filter cloth by the chute The water is first removed from the gravity portion, and the sludge naturally removed from the gravity portion of the gravity is removed by the first dehydration portion composed of the main roller and the pressure roller, and then passes through the second dehydration portion. Drum rollers and pressure rollers are used to remove moisture three times.
상기 제1탈수부(2)는 마이크로파발생부(10)와, 진공흡입장치(20)로 구성되어있다.The first dewatering part 2 is composed of a microwave generator 10 and a vacuum suction device 20.
상기 마이크로파발생부(10)는, 메인롤러(11)의 외주면이 고무로 코팅되어 있고, 그 외주로 메인롤러(11)를 감쌀 수 있는 호형을 이룸과 동시에 양쪽으로 마이크로파가 방출되는 것을 방지할 수 있는 방지벽(12)을 가지고 있는 합성수지재인 프레임(13)이 설치되어 있으며, 프레임(13)의 내측에는 마이크로파발진부에서 생성된 마이크로파를 조사하여 슬러지의 입자를 잘게 파괴 시킴은 물론 진동 에 의한 마찰로 슬러지에 열을 발생시키는 다수의 마이크로파 발생기(14)가 메인롤러(11)의 길이방향을 따라 등간격을 이루며 분포되어 있는 것이다.The microwave generator 10, the outer circumferential surface of the main roller 11 is coated with a rubber, and the outer circumferential surface of the main roller 11 can be formed in an arc shape that can surround the main roller 11 and at the same time can prevent the microwaves from being emitted to both sides. Frame 13, which is a synthetic resin material having a barrier wall 12, is provided, and inside the frame 13 is irradiated with microwaves generated by the microwave oscillation unit to finely destroy the particles of the sludge, as well as by friction by vibration A plurality of microwave generators 14 for generating heat in the sludge is distributed at equal intervals along the longitudinal direction of the main roller (11).
상기 마이크로파발생부(10)에서 입자가 잘게 파괴되어진 슬러지로부터 분리되어진 내부수성수분(슬러지내에 숨어 있는 물)은 진공흡입장치(20)에 의해 제거되어지는데, 상기 진공흡입장치(20)는 마이크로파 발생부(10)를 거치면서 입자가 파괴된 슬러지로부터 분리되어진 내수성수분을 빨아들일 수 있도록 속이 비어 있고, 진공펌프와 호스(22)로 연결되어 있으며, 메인롤러(11)와 대응하는 면에는 진공펌프의 흡인 작동으로 슬러지로부터 분리된 수분이 흡입 제거되어질 수 있이도록 다수의 수분 흡입구멍(21)들이 형성되어 있다.The internal aqueous moisture (water hidden in the sludge), which is separated from the sludge in which the particles are finely broken in the microwave generator 10, is removed by the vacuum suction device 20, and the vacuum suction device 20 generates microwaves. Hollow, connected to the vacuum pump and the hose 22 to suck up the water-resistant water separated from the sludge that particles are destroyed while passing the part 10, the vacuum pump on the surface corresponding to the main roller 11 A plurality of water suction holes 21 are formed so that the water separated from the sludge can be sucked out by the suction operation of the sludge.
상기 마이크로파발생부(10)와, 진공흡입장치(20)로 이루어진 제1탈수부(2)에서 2차 수분이 제거된 슬러지의 수분을 제2탈수부(4)에서 3차 제거하게 된다.The water of the sludge from which the secondary water is removed from the first dewatering unit 2 including the microwave generator 10 and the vacuum suction device 20 is removed from the second dewatering unit 4 in the third manner.
상기 제2탈수부(4)는 드럼롤러(31) 외주면에 가압실린더(38)에 의해 드럼롤러에 밀착되어지는 가압롤러(33)가 삼방향에서 등간격을 이루며 설치되고 있되, 가 압롤러(32)는 드럼롤러(31)의 회전방향으로 가면서 작은 지름을 가짐과 동시에 가압롤러(32) 사이로 아이들롤러(33)가 설치되어 있고, 상기 가압롤러(32)와 아이들 롤러(33)에는 드럼롤러(31)의 양쪽에서 원거리를 이루며 설치되어진 텐션롤러(34)(35)에 여러가닥의 고무벨트(34a)(35a)가 일정 간격의 틈을 이루며 배치되어서 가압롤러(32)와 아이들롤러(33) 사이로 지그재그 권회되어지게 설치되어 있으며, 가압롤러(32)와 아이들롤러(33) 사이에는 가압력에 의해 슬러지로부터 분리되어 고무벨트(34a)(35a) 틈사이로 빠져나오는 수분을 흡인할 수 있는 진공흡인관(36)(37)이 설치되어 있는 것을 특징으로 한다.The second dewatering part 4 is installed on the outer circumferential surface of the drum roller 31 with pressure rollers 33 that are in close contact with the drum rollers at equal intervals in three directions. 32 has a small diameter while going in the rotational direction of the drum roller 31 and the idle roller 33 is provided between the pressure roller 32, the drum roller 32 and the idle roller 33 in the drum roller 33 The rubber rollers 34a and 35a of several strands are arranged in the tension rollers 34 and 35 installed at a distance from both sides of the rollers 31 at a predetermined interval so that the pressure roller 32 and the idle roller 33 It is installed to be zigzag-wound between the vacuum suction pipe between the pressure roller 32 and the idle roller 33, which can separate the water from the sludge by the pressing force and suck out the water flowing out between the gaps of the rubber belts 34a and 35a. (36) 37 is provided.
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 고압 탈수기의 구성도이고, 도2는 본 발명에 의한 고압 탈수기의 제1탈수부를 발취한 부분 사시도이며, 도3은 본 발명에 의한 고압 탈수기의 제2탈수부를 텐션롤러에 고무벨트가 설치된 상태를 보인 예시도 이다.1 is a block diagram of a high-pressure dehydrator with a high dehydration efficiency according to the present invention, Figure 2 is a partial perspective view of the first dewatering portion of the high-pressure dehydrator according to the present invention, Figure 3 is a second perspective view of the high-pressure dehydrator according to the present invention The dehydration part is an exemplary view showing a state in which the rubber belt is installed on the tension roller.
도시된 바와 같이, 본 발명의 고압 탈수기(1)에 폐수로부터 분리된 슬러지가 슈트를 통해 여과포에 실려 이송되어지게 된다.As shown, the sludge separated from the wastewater in the high-pressure dehydrator 1 of the present invention is carried on the filter cloth through the chute.
상기와 같이 여과포에 실려 운반되는 슬러지는 자중중력부에서 슬러지로부터 수분이 분리 탈수되어지게 된다.As described above, the sludge carried on the filter cloth is separated and dehydrated from the sludge in the gravity unit.
자중중력부에서 1차 수분이 탈수된 슬러지는 제1탈수부(2)을 거치면서 2차 탈수되어지게 되는데, 슬러지를 실은 여과포가 제1탈수부(2)의 메인롤러(11)를 지날때 여과포의 장력에 의한 탈수가 이루어짐과 동시에 메인롤러(11)의 외주면으로설치된 마이크로파발생장치(10)에 의해 슬러지의 입자가 파괴되어져 슬러지 내부에 숨어 있는 수분(물)의 탈수가 급속하게 이루어지게 된다.The sludge dehydrated by the first gravity in the self-gravity part is dehydrated secondly through the first dehydration part 2, when the filter cloth carrying the sludge passes through the main roller 11 of the first dewatering part 2. Dehydration by the tension of the filter cloth is carried out and the sludge particles are destroyed by the microwave generator 10 installed on the outer circumferential surface of the main roller 11, so that the water (water) hidden in the sludge is rapidly dehydrated. .
상기 마이크로파발생장치(10)에 의해 슬러지의 입자가 파괴되어지는 원리를 좀더 구체적으로 설명하면, 마이크로파발진부(도시하지 않았음)에서 생성된 마이크로파가 프레임(13)에 설치되어진 마이크로파 발생기(14)를 통해 조사되어지게 된다.The principle in which the sludge particles are destroyed by the microwave generator 10 will be described in more detail. The microwave generated by the microwave oscillator (not shown) is installed in the frame 13. Will be investigated.
상기와 같이 마이크로파 발생기(14)를 통해 조사된 마이크로파 파장에 의해 슬러지의 입자가 파괴되어 슬러지로부터 수분 배출이 급속하게 이루어지게 되고, 마이크로파가 슬러지로 침투 열 변환되어 슬러지 입자 내부에 숨어 있는 수분을 흡입과 동시에 가압탈수시킬 수 있게 되는 것이다.As described above, the particles of the sludge are destroyed by the microwave wavelength irradiated through the microwave generator 14 to rapidly discharge the water from the sludge, and the microwaves penetrate into the sludge and convert the heat into the sludge to suck in the moisture hidden inside the sludge particles. At the same time it will be able to dehydrate.
상기 조사되어지는 마이크로파는 메인롤러(11)의 외표면이 고무로 코팅되어 있어 전기적 소모 없이 안전하게 사용되어질 수 있는 것이다.The microwave to be irradiated is that the outer surface of the main roller 11 is coated with rubber can be used safely without electrical consumption.
상기의 마이크로파발생장치(10)에 의해 슬러지로부터 분리되어진 수분은 진공펌프와 호스(22)연결된 공흡입장치(20)를 지날때 메인롤러(11)와 대응하는 면에 형성되어진 흡입구멍(21)들을 통해 흡입되어 분리(탈수)되어지게 되는 것이다.The water separated from the sludge by the microwave generator 10 is the suction hole 21 formed on the surface corresponding to the main roller 11 when passing through the co-suction device 20 connected to the vacuum pump and the hose 22 It is sucked through them and separated (dehydrated).
상기에서와 같이 제1탈수부(10)에서 수분이 2차제거되어진 슬러지는 제2탈수부(4)를 거치면서 탈수가 완료되어지게 된다.As described above, the sludge from which the water is secondarily removed from the first dewatering part 10 is dehydrated while passing through the second dewatering part 4.
슬러지가 제2탈수부(4)를 지날때에는 드럼롤러(31)의 외주면에 대하여 가압되어질 수 있도록 가압실린더(38)에 의해 설치되어진 가압롤러(32)에 의해 가압되어짐과 동시에 드럼롤러(31)의 양쪽에서 텐션롤러(34)(35)에서 권회되어드럼롤러(31)및 가압롤러(32) 그리고 아이들롤러(33)에 걸쳐 지그재그로 설치되어진 고무벨트(34a)(35a)를 지날때 잔여 수분이 제거되어진다.When the sludge passes through the second dewatering part 4, the drum roller 31 is pressed by the pressure roller 32 installed by the pressure cylinder 38 so as to be pressed against the outer circumferential surface of the drum roller 31. Residual moisture when passing through the rubber belts 34a and 35a, which are wound on the tension rollers 34 and 35 on both sides of the drum roller 31 and the pressure rollers 32, and zigzagly installed over the idle rollers 33. Is removed.
상기 가압롤러(32)에 의해 슬러지가 가압될 때 가압롤러(32)의 직경(구경)이 배출구쪽으로 가면서 조금씩 작아져 가압롤러(32)표면의 압력차와, 상기 가압롤러와 가압롤러의 간격 또한 배출구쪽으로 가면서 작아지게 됨으로서 갑작스런 압력차로 인해 슬러지가 여과포 사이로 빠져 나오는 것을 방지하면서 점진적으로 압력을 가함과 동시에 슬러지의 유입부 압력이 유출부쪽으로 가면서 압력이 증대되기 때문에 수분 제거가 효과적으로 이루어진다.When the sludge is pressurized by the pressure roller 32, the diameter (diameter) of the pressure roller 32 decreases little by little toward the discharge port, so that the pressure difference between the surface of the pressure roller 32 and the distance between the pressure roller and the pressure roller are also reduced. As the pressure decreases toward the outlet, the pressure is gradually increased while preventing the sludge from escaping between the filter cloths due to the sudden pressure difference, and at the same time, the pressure is increased as the inlet pressure of the sludge goes to the outlet, thereby effectively removing water.
아울러 상기와 같이 제2탈수부(4)에서 분리되어지는 수분은 도3에서와 같이 여러가닥으로 설치되어진 고무벨트(34a)(35a)의 틈(T)으로 빠져 나오게 되고, 빠져나온 수분은 진공흡입관(36)이 빨아들여 슬러지로 재차 스며드는 것을 방지하게 되는 것이다.In addition, the water separated from the second dewatering part 4 as described above is released into the gap T of the rubber belts 34a and 35a installed in multiple strands, as shown in FIG. The suction pipe 36 is prevented to be sucked back into the sludge again.
상기된 바와 같이 본 발명의 탈수효율을 높인 고압 탈수기는, 제1탈수부(2)에서 탈수되어지는 슬러지의 수분 탈수를 종래와 같이 전기침투가열방식에서 탈피하여 마이크로파발생장치(10)에서 조사되는 마이크로파에 의해 슬러치의 입자를 잘게 분쇄하여 슬러지가 가지고 있는 수분을 외부로 급속하게 배출시킴과 동시에 슬러지에만 열을 가하고 슬러지로부터 분리된 수분을 진공흡입장치(20)로 흡입 제거하는 것이어서, 제1탈수부(2)에서의 탈수효율을 높임과 동시에 제2탈수부(4)의 운전부하를 줄여 줄수 있는 것이고; 둘째, 슬러지만이 가열되어짐으로서 종래 가열롤러 방식에서 발생하였던 열에 의한 여과포의 경화현상을 방지할 수 있을 뿐만 아니라, 온도변화에 따른 신축에 의한 여과포의 느러짐을 해소하였으며; 셋째, 제2탈수부(4)를 이루는 드럼롤러(31)의 일측으로 고무벨트(34a)가 텐션롤러(34)에 권회되어지는 고무벨트(34a)를 설치하고, 드럼롤러(31)의 다른쪽에는 슬러지가 공급되는 쪽에서 배출되는쪽으로 가면서 작은 직경을 가지는 가압롤러(33)들에 대하여 지그재그로 권회되어지는 고무벨트(35a)가 텐션롤러(35)에 의해 설치되어 있으며, 슬러지로부터 분리된 수분을 흡입 제거할 수 있는 진공흡입관(36)을 포함하는 것으로서 슬러지가 가압되어지는 시간이 증대되어 탈수 효율이 높아졌을 뿐만 아니라, 슬러지로부터 분리되어 고무벨트의 사이로 빠져 나오는 수분을 제거함으로서 수분이 슬러지로 재침투되는 것을 방지할 수 있는 매우 유용한 발명인 것이다.As described above, the high-pressure dehydrator having high dehydration efficiency of the present invention is irradiated from the microwave generator 10 by escaping the water dehydration of the sludge dewatered from the first dewatering unit 2 by the electro-osmotic heating method as in the prior art. The sludge is finely crushed by the microwave to rapidly discharge the water contained in the sludge to the outside, and heat only the sludge, and suction and remove the water separated from the sludge by the vacuum suction device 20. It is possible to reduce the operating load of the second dewatering section 4 while increasing the dewatering efficiency at the section 2; Second, as the sludge is heated, not only the curing phenomenon of the filter cloth due to heat generated in the conventional heating roller method can be prevented, but also the slowness of the filter cloth due to the expansion and contraction due to the temperature change is eliminated; Third, the rubber belt 34a on which the rubber belt 34a is wound on the tension roller 34 is provided on one side of the drum roller 31 forming the second dewatering part 4, and the other of the drum roller 31 is provided. On the side, the rubber belt 35a, which is wound zigzag with respect to the pressure rollers 33 having a small diameter, is installed by the tension roller 35 while going from the side from which the sludge is supplied, to the water separated from the sludge. It includes a vacuum suction tube 36 that can remove the suction, as the time for which the sludge is pressurized is increased, as well as the dewatering efficiency is increased, as well as the water is removed from the sludge to remove the water coming out between the rubber belt to the sludge. It is a very useful invention that can prevent reinfiltration.
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JP2966403B1 (en) * | 1998-07-31 | 1999-10-25 | 株式会社ティー アンド エム設計 | Sludge treatment equipment |
KR100330731B1 (en) * | 1999-04-12 | 2002-04-03 | 한상배 | Dewatering apparatus of sludge and dewaterer |
KR20010036814A (en) * | 1999-10-12 | 2001-05-07 | 양인모 | Process for sludge dehydrating using microwave |
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 |
-
2001
- 2001-04-18 KR KR10-2001-0020960A patent/KR100393943B1/en not_active IP Right Cessation
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101112199B1 (en) * | 2009-08-06 | 2012-02-13 | 이형락 | heating roller and sludge drying apparatus comprising the same |
WO2011099691A2 (en) * | 2010-02-12 | 2011-08-18 | 주식회사 에이케이인터내셔널 | Dehydrating and evaporation-drying apparatus for sludge treatment |
WO2011099691A3 (en) * | 2010-02-12 | 2011-11-17 | 주식회사 에이케이인터내셔널 | Dehydrating and evaporation-drying apparatus for sludge treatment |
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KR100393943B1 (en) | 2003-08-14 |
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