KR900006378Y1 - Filter press type dryer - Google Patents
Filter press type dryer Download PDFInfo
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- KR900006378Y1 KR900006378Y1 KR2019870016162U KR870016162U KR900006378Y1 KR 900006378 Y1 KR900006378 Y1 KR 900006378Y1 KR 2019870016162 U KR2019870016162 U KR 2019870016162U KR 870016162 U KR870016162 U KR 870016162U KR 900006378 Y1 KR900006378 Y1 KR 900006378Y1
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- filter plate
- filter
- plate
- support
- sludge
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
- B01D25/12—Filter presses, i.e. of the plate or plate and frame type
- B01D25/127—Filter presses, i.e. of the plate or plate and frame type with one or more movable filter bands arranged to be clamped between the press plates or between a plate and a frame during filtration, e.g. zigzag endless filter bands
- B01D25/1275—Filter presses, i.e. of the plate or plate and frame type with one or more movable filter bands arranged to be clamped between the press plates or between a plate and a frame during filtration, e.g. zigzag endless filter bands the plates or the frames being placed in a non-vertical position
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
- B01D25/12—Filter presses, i.e. of the plate or plate and frame type
- B01D25/21—Plate and frame presses
- B01D25/215—Construction of the filter plates, frames
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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
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
내용 없음.No content.
Description
제1도는 본 고안의 탈수기의 여과판을 사용하는 탈수기의 구조를 보이는 측면도.1 is a side view showing the structure of the dehydrator using the filter plate of the dehydrator of the present invention.
제2(a)도는 종래의 여과판과 지지고리의 구조를 보이는 정면도,2 (a) is a front view showing the structure of the conventional filter plate and the support ring,
제2(b)도는 동 요부 확대 단면도.Figure 2 (b) is an enlarged cross-sectional view of the recess portion.
제3도는 본 고안에 따라 구성된 여과판과 지지고리의 구조를 보이는 정면도.Figure 3 is a front view showing the structure of the filter plate and the support ring constructed in accordance with the present invention.
제4도는 제3도의 A-A선에 대한 일부 확대 단면도이다.4 is a partially enlarged cross-sectional view taken along line A-A of FIG.
* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings
6 : 여과판지지레일 8 : 가압판6: filter plate support rail 8: pressure plate
9 : 유압실린더 10 : 실린더로드9: hydraulic cylinder 10: cylinder rod
11 : 여액수로 12 : 여액배수관11: filtrate 12: filtrate drainage pipe
13 : 여과판 이송콘베이어 22,32 : 여과돌기13: filter plate conveying conveyor 22,32: filtration protrusion
25,35 : 배수로 35a : 배수통로25,35 drainage passage 35a drainage passage
26,36 : 여과판 지지고리 27,37 : 지지브라켓26,36: support plate for filter plate 27,37: support bracket
28,38 : 지지롤러 29,39 : 이송판28,38: support roller 29,39: transfer plate
30 : 결합돌조 30a : 결합홈30: coupling protrusion 30a: coupling groove
본 고안은 필터 프레스형 탈수기의 여과판 더 상세히는 산업 및 폐수처리용으로 사용하는 등 탈수기의 여과판 구조의 개선에 관한 것이다.The present invention relates to an improvement in the filter plate structure of the dehydrator, such as the filter plate of the filter press type dehydrator, more specifically, for industrial and wastewater treatment.
통상 필터 프레스(filter press)라고 불리우는 형식의 탈수기는 여과포를 씌운 복수의 여과판을 연속시키고, 이에 슬러지(sludge)를 유입 및 가압시켜 여액을 배출하고 난 슬러지의 고형성분으로 이루어 진 케익(cake)을 배출하는 형식의 것이다.A dehydrator of the type commonly called a filter press is a series of filter cloths covered with filter cloth, and sludge is introduced and pressurized to produce a cake composed of solid components of sludge from which the filtrate is discharged. It is of the form to discharge.
그런데 종래의 탈수기에 있어서는 여과판의 형상이 복잡하여 제작이 곤란했을뿐만 아니라, 여과 용적이 작아 다수의 여과판을 필요로 했으며, 여과 돌기의 형상이 사각형 단면이어서 슬러지의 순환 효율이 나빴으며, 여과판의 지지고리가 중앙에 형성되었으므로 여과판 분리시 비대칭 이동을 하여 탈수기의 작동을 방해하는 일이 있었으며, 그 구조상 여액을 집적할수가 없어서 여과된 여액이 타수기 하방으로 바로 배출되는 문제점이 있었다.However, in the conventional dehydrator, the shape of the filter plate was complicated and not only difficult to manufacture, but also required a large number of filter plates due to the small filtration volume. The shape of the filtration protrusions was rectangular in cross section, which resulted in poor circulation efficiency of the sludge. Since the ring was formed in the center, there was a problem that the asymmetrical movement during separation of the filter plate prevented the operation of the dehydrator, and the filtrate could not be accumulated due to its structure, so that the filtered filtrate was discharged directly under the breaker.
이에따라 본 고안의 목적은 상술한 종래의 문제점을 모두 해결한 필터 프레스형 탈수기의 여과판을 제공하는 것이다.Accordingly, an object of the present invention is to provide a filter plate of the filter press type dehydrator which solves all of the above-mentioned conventional problems.
이하에 본 고안을 첨부된 도면을 참조로 하여 상세히 설명한다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
제1도는 필터 프레스형 탈수기의 구조를 보이는 측면도로서, 여과판과 이에 따른 구조 변경을 제외하면 종래의 탈수기와 외형상 동일하다.1 is a side view showing the structure of a filter press type dehydrator, which is identical in appearance to a conventional dehydrator except for a filter plate and a structural change.
도시되지 않은 침전조로 부터 슬러지 펌프(P)를 통해 탈수기내로 유입된 슬러지(sludge)는 가압탱크(T)에 의해 반복 가압됨으로써 여과된다.The sludge introduced into the dehydrator through the sludge pump P from the settling tank (not shown) is filtered by being repeatedly pressurized by the pressure tank T.
필터 프레스형 탈수기는 제1단부판(lst end plate;1)과 제2단 부판(2)과 그 사이을 연결하는 제1프레임(3)과 제2프레임(4)으로 외형이 이루어지며 그 하단에는 지지부(5)가 연결고정된다.The filter press type dehydrator has an outer shape consisting of a first end plate 1 and a second end plate 2 and a first frame 3 and a second frame 4 connecting therebetween, The support part 5 is fixed.
제1프레임(3)의 상부에는 여과판 지지레일(6)이 구비되어 복수의 여과판(F)이 미끄럼 지지되어 매달려 있으며, 제1단부판(1)측에는 탈수기 내에 슬러지를 도입시키는 슬러지 도입관(7)이 연결되며, 제2단부판(2)측에는 각 여과판(F)을 상호 밀착시키는 가압판(8) 및 이에 압력을 제공하는 유입실린더(9) 및 실린더 로드(10)가 구비된다.A filter plate support rail 6 is provided on the upper part of the first frame 3 so that a plurality of filter plates F are slid and suspended, and a sludge introduction pipe 7 for introducing sludge into the dehydrator is provided on the first end plate 1 side. ) Is connected to the second end plate (2) side is provided with a pressure plate (8) for adhering each filter plate (F) in close contact with each other, and an inlet cylinder (9) and a cylinder rod (10) providing pressure thereto.
일체로 여과판(F)의 하방에는 여과된 여액을 배출하는 여액수로(11) 및 여액배수관(12)이 구비되며, 상방에는 구동모터(14)에 의해 구동되어 여과판(F)의 분리시 각 여과판(F)을 일정간격으로 이송배치시키는 여과판 이송콘베이어(13)가 구비된다.The filtrate channel 11 and the filtrate drainage pipe 12 for discharging the filtered filtrate are integrally provided below the filter plate F, and are driven by the drive motor 14 at the upper side to separate the filter plate F. The filter plate conveying conveyor 13 which transfers the filter plate F at predetermined intervals is provided.
각 여과판(F)은 도시되지 않는 여과포에 의해 둘러싸여져서 가압판(8)에 의해 일체로 밀착되며, 각 여과판(F)은 후술하는 슬러지 통로를 구비하여 전체로서 하나의 여과용적(filtering volume)을 형성한다.Each filter plate F is surrounded by a filter cloth (not shown) and is integrally pressed by the pressure plate 8, and each filter plate F has a sludge passage described later to form one filtering volume as a whole. do.
가압탱크(T)에 의해 반복가압되어 여액을 배출하고 나면 여과용적에는 고형성분만으로 이루어진 케익(cake)만이 남게된다.After the pressurized tank (T) is repeatedly pressurized and the filtrate is discharged, only a cake consisting of solid components remains in the filtration volume.
그러면 유압실린더(9)를 축퇴시켜 가압판(8)을 후퇴시킨뒤 구동모터(14)를 구동, 여과판 이송 콘베이어(13)가 회전하면 도시되지 않은 훅(hook)에 의해 각 여과판(F)이 일정간격으로 분리된다.Then, the hydraulic cylinder 9 is retracted to retract the pressure plate 8, and then the driving motor 14 is driven. When the filter plate conveying conveyor 13 rotates, each filter plate F is fixed by a hook (not shown). Separated by intervals.
다음 각 여과판(F)사이의 케익을 탈수기 하방으로 낙하시켜 취출하게 된다.Next, the cake between the respective filter plates F is dropped below the dehydrator and taken out.
제2(a)도는 종래의 여과판(F)의 구조를 보이는 정면도이며, 제2(b)도는 그 요부에 대한 확대 단면도이다.FIG. 2 (a) is a front view showing the structure of the conventional filter plate F, and FIG. 2 (b) is an enlarged sectional view of the main part.
여과판은 보강철판(21)의 양면에 화학적 내구성이 강한 합성고무를 압착 성형한 것으로, 종래의 여과판(F)는 양면에 사각형 단면의 여과돌기(22)를 다수 구비하고 인접 여과판이 상호 맞물려 밀착되도록 결합돌조(30) 및 결합홈(30a)이 형성되어 도시되지 않은 여과포가 씌어 짐으로 구성되었다.The filter plate is a press-molded synthetic rubber having strong chemical durability on both sides of the reinforcing iron plate 21, and the conventional filter plate F includes a plurality of filter projections 22 having a rectangular cross section on both sides, and adjacent filter plates are in close contact with each other. Coupling protrusion 30 and the coupling groove (30a) was formed was composed of a filter cloth not shown.
여과판(F)에는 슬러지통로(23)가 구비되어 슬러지 도입관(7)으로 부터 유입된 슬러지가 각 여과판(F)들이 형성하는 여과 용적으로 유입되며, 복수의 지지블록(24)이 형성되어 밀착 및 가압시 각 여과판(F)간의 여과용적의 간격을 유지하도록 하였다.The sludge passage 23 is provided in the filter plate F so that the sludge introduced from the sludge introduction pipe 7 flows into the filtration volume formed by the respective filter plates F, and a plurality of support blocks 24 are formed to closely contact each other. And it was made to maintain the space | interval of the filter volume between each filter plate F at the time of pressurization.
여과판(F)에는 슬러지통로(23)가 구비되어 슬러지 도입관(7)으로 부터 유입된 슬러지가 각 여과판(F)들이 형성하는 여과 용적으로 유입되며, 복수의 지지블록(24)이 형성되어 밀착 및 가압시 각 여과판(F)간의 여과용적의 간격을 유지하도록 하였다.The sludge passage 23 is provided in the filter plate F so that the sludge introduced from the sludge introduction pipe 7 flows into the filtration volume formed by the respective filter plates F, and a plurality of support blocks 24 are formed to closely contact each other. And it was made to maintain the space | interval of the filter volume between each filter plate F at the time of pressurization.
여과판(F)의 하부에는 하나 또는 복수의 배수로(25)가 구비되어 가압시 슬러지의 여액이 배출되도록 형성된다.The lower portion of the filter plate (F) is provided with one or a plurality of drainage paths 25 are formed so that the filtrate of the sludge is discharged when pressurized.
여과판(F)의 상부에는 지지고리(26)가 나사등으로 결합되어 여과판(F)을 여과판 지지레일(26)에 매달아 미끄럼 지지한다.The support ring 26 is coupled to the upper portion of the filter plate (F) by a screw or the like to suspend the filter plate (F) by hanging on the filter plate support rail (26).
여과판 지지고리(26)는 각각 하부가 여과판(F)에 나사로 고정되는 2개의 지지고리 브라켓(27)과, 그 상단에 부착되어 여과판 지지레일(6)과 미끄럼 접촉하는 지지롤러(Supporting roller;28)와, 상술한 지지고리 브라켓(27)간을 연결하며 여과판 이송콘베이어(13)의 훅(hook;13a)에 걸려 여과판(F)의 분리시 각 여과판(F)을 일정 간격만큼 씩 이격 배치시키는 이송핀(29)으로 구성된다.The filter plate support ring 26 has two support ring brackets 27, each of which has a lower portion screwed to the filter plate F, and a support roller attached to an upper end thereof and in sliding contact with the filter plate support rail 6; ) And the above-mentioned support ring brackets 27 are hooked to the hook 13a of the filter plate conveying conveyor 13 to separate each filter plate F by a predetermined interval when separating the filter plate F. Consists of a feed pin (29).
상술한 종래의 여과판은 다음과 같은 여러가지 문제점을 가지고 있다.The conventional filter plate described above has various problems as follows.
첫째, 여과판(F)의 단면이 인접 여과판(F)과 밀착되도록 하기 위해 결합돌기(30) 및 결합홈(30a)이 구비되므로 형상이 복잡하여 제작 및 취급이 곤란하고 결합돌기(30)가 잘 파손된다.First, since the coupling protrusion 30 and the coupling groove 30a are provided in order for the cross section of the filter plate F to be in close contact with the adjacent filter plate F, the shape is complicated and difficult to manufacture and handle, and the coupling protrusion 30 is well formed. It is broken.
둘째, 여과돌기(22)가 사각형 단면으로 구성되어 슬러지가 유입되어 가압된 경우 슬러지의 고형 성분이 여과돌기(22)간을 막게되므로 여과 효율을 저하시킨다.Second, when the filtration projection 22 has a rectangular cross section and the sludge is introduced and pressurized, the solid component of the sludge blocks the filtration projections 22, thereby lowering the filtration efficiency.
셋째, 배수로(25)가 여과판(F)의 하방으로 직접 연통되어 있으므로, 여과판(F)분리후 케익의 배출 문제상 여액을 집적할수 있는 여액수로를 구비할수 없으며, 이를 구비하기 위해 여과판(F)의 일측방에만 배수로(25)를 설치하면 여액 배출량이 감소되므로 여과 소요 시간을 장시간 소모하게 된다.Third, since the drainage passage 25 is directly connected to the lower side of the filter plate (F), it is not possible to provide a filtrate channel that can accumulate the filtrate after the separation of the filter plate (F) due to the problem of the discharge of the cake, to provide this filter plate (F) If only one side of the drainage 25 is installed, the filtrate discharge is reduced, so that the filtration time is consumed for a long time.
넷째, 지지고리(26)가 여과판(F)과 별개로 구성되어 결합되므로 제작이 복잡하고, 이송핀(29)이 중앙에 하나만 구비되므로 여과판 분리시 훅(13a)의 견인력이 불균형되어 지지롤러(28)가 여과판 지지레일(6)과 걸려 여과판 이송이 중단(jamming)될 우려가 있다.Fourth, since the support ring 26 is configured and coupled to the filter plate (F) separately, it is complicated to manufacture, and since only one feed pin 29 is provided in the center, the traction force of the hook 13a is unbalanced when the filter plate is separated from the support roller ( 28 is caught by the filter plate support rail 6, so that the filter plate transfer may be jammed.
제3도 및 4도는 이상과 같은 종래의 문제점들을 해결하기 위한 본 고안의 여과판 구조를 보이는 도면으로서, 제3도는 정면도, 제4도는 일부 확대 단면도이다.3 and 4 are views showing the filter plate structure of the present invention for solving the conventional problems as described above, Figure 3 is a front view, Figure 4 is a partially enlarged cross-sectional view.
도면에서 종래의 구성과 유사한 부재들에 대하여는 부재 번호에 10을 더하여 즉(30단위임) 사용하며 특징을 제외한 별도의 설명은 생략한다.In the drawings, members similar to those of the conventional configuration are used by adding 10 to the member number (that is, 30 units), and a separate description except for features is omitted.
본 고안 여과판(F')의 특징은 여과돌기(32)의 형상과, 2개의 지지고리(36)와, 여과판(F')의 테두리의 만곡 돌출부(R)와, 배수통로(35a) 및 배수관(40)을 구비한 것이다.The characteristics of the filter plate F 'of the present invention are characterized by the shape of the filtration protrusion 32, the two support rings 36, the curved protrusion R of the rim of the filter plate F', the drain passage 35a and the drain pipe. 40 is provided.
본 고안의 여과돌기(32)는 원형으로 구성되어 슬러지의 고형성분이 막히는 일이 없으므로 여과 효율이 높다.The filtration protrusion 32 of the present invention has a high filtration efficiency because the solid component of the sludge is not blocked by a circular shape.
본 고안의 지지고리(36)는 보강철판(31)과 일체로 형성된 지지브라켓(37)과, 이에 용접 또는 나사 고정되는 롤러 블록(roller block;38a)과, 지지롤러(38)와, 이송핀(39)으로 구성되어, 그 제작 및 조립이 간편할 뿐 아니라, 여과판(F')의 안내 및 여과판(F)의 분리시 양측에는 균형있게 견인되므로 종래와 같이 여과판(F')의 이송이 중단되는 일이 없게 된다.The support ring 36 of the present invention includes a support bracket 37 formed integrally with the reinforcing steel plate 31, a roller block 38a welded or screwed thereto, a support roller 38, and a transfer pin. It is composed of (39), the production and assembly of the filter plate, as well as the guide plate of the filter plate (F ') and when the separation of the filter plate (F) is towed to both sides in a balanced manner, the transfer of the filter plate (F') as usual It will not be possible.
본 고안 여과판(F')의 테두리에는 제4도의 하부의 확대단면도에서 보는 것처럼 종래의 결합 돌조 및 결합홈대신 소정두께(t)의 만곡 돌출부(R)을 형성하여, 가압판(8)의 가압시 인접 여과판(F')간에 압착됨으로써 확실한 밀봉을 제공하게 된다.As shown in the enlarged cross-sectional view of the lower part of FIG. 4, a curved protrusion R having a predetermined thickness t is formed on the edge of the filter plate F ′ of the present invention, and when the pressing plate 8 is pressed. Compression between adjacent filter plates F 'provides reliable sealing.
본 고안 배수로(35)는 여과판(F')의 양면에 복수 구비되어, 배수통로(35a)에 집적되고 여과판(F') 일측방의 배수관(40)으로 배출되므로 배출 효율이 높아 여과 소요시간이 단축될 뿐 아니라, 케익의 제거 작업과 무관하게 여액을 탈수기 일측방의 여액수로(11)를 통해 여액 배수관(12)으로 일괄 배출시킬수 있게 된다.The present invention drainage passage 35 is provided on both sides of the filter plate (F '), is integrated in the drain passage 35a and discharged to the drain pipe 40 on one side of the filter plate (F'), so the discharge efficiency is high and the filtration time is high. Not only is it shortened, irrespective of the cake removal operation, the filtrate can be collectively discharged to the filtrate drain pipe 12 through the filtrate channel 11 on one side of the dehydrator.
기타 본 고안에 따르는 다른 이점들은 명시되지 않았다 하더라도 이상의 설명과 도면에서 쉽게 알 수 있을 것이다.Other advantages according to the present invention will be readily apparent from the above description and drawings even if not specified.
또한 이상의 설명은 본 고안의 범위를 제한 것이 아니라 단순히 실시예의 예시만을 목적으로 한 것이므로 본 고안은 이에 국한되는 것이 아니다.In addition, the above description is not intended to limit the scope of the present invention, but merely for the purpose of illustration of the embodiment is not intended to limit the present invention.
즉, 본 고안의 특징부인 원형 여과돌기의 구성이나, 양면의 지지고리 구성이나, 배수통로 및 배수관이 구성, 또는 만곡 돌출부를 이용하여 밀봉을 제공하는 구성중의 어느 하나를 이용하거나, 상기 각 구성들에 공지의 다른 수단을 부가 또는 변경하는 구성은 당연히 본 고안의 범위내에 포함된다.That is, any one of the configurations of the circular filter projection, the structure of the support ring on both sides, the configuration of the drain passage and the drain pipe, or the configuration of providing a seal using the curved protrusion, or the respective configurations Addition or modification to other means known in the art is naturally included within the scope of the present invention.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR2019870016162U KR900006378Y1 (en) | 1987-09-23 | 1987-09-23 | Filter press type dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR2019870016162U KR900006378Y1 (en) | 1987-09-23 | 1987-09-23 | Filter press type dryer |
Publications (2)
Publication Number | Publication Date |
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KR890006433U KR890006433U (en) | 1989-05-13 |
KR900006378Y1 true KR900006378Y1 (en) | 1990-07-20 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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KR2019870016162U KR900006378Y1 (en) | 1987-09-23 | 1987-09-23 | Filter press type dryer |
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KR (1) | KR900006378Y1 (en) |
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KR102193514B1 (en) | 2020-07-06 | 2020-12-21 | 주식회사 정도 | Safety device for filter press dehydrator |
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1987
- 1987-09-23 KR KR2019870016162U patent/KR900006378Y1/en not_active IP Right Cessation
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