• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    In a tubular filter bodies with at least one tubular filter structure with a porous wall, through which a liquid passes substantially radially, particles above a given size being held back at the entrance surface, made of porous plastic, ceramic material, metal, graphite, etc, continuous operation at constant pressures is made possible by providing at least one groove (or slot) which is closed toward the outside and forms a forced flow path leading from an inlet to an outlet in the circumferential entrance surface of the tubular filter body.
    公开号:SU797548A3
    申请号:SU792706010
    申请日:1979-01-04
    公开日:1981-01-15
    发明作者:Аппенцеллер Валентин；Вальтер Аурих Кристоф；Хартманн Вернер；Кутц Йоханнес
    申请人:Appenzeller Valentin；Kristof Valter Aurikh；Hartmann Werner；Jokhannes Kutts；
    IPC主号:
    专利说明:

    ; 54) FILTERING DEVICE
    one
    The invention relates to filtration, namely to cartridge filters for separating suspensions and ultrafiltering wastewater solutions.
    A filtering device is known comprising a housing divided by a hermetic septum into a chamber of the initial suspension and a concentrate chamber with an outlet, porous filter cartridges placed in the chamber of the concentrate and fixed on a sealed partition, and branch pipes supplying the initial suspension, removal of filtrate and concentrate SC.
    A disadvantage of the known filtrate is that the flow of the initial fluid moves laminarly along the filter cartridge and a layer of sediment or slit separated fractions forms on its surface which reduces the throughput of the filter cartridge and the performance of the device as a whole. In order to preserve the filtering properties, the device must be regularly released from the resulting layer.
    The purpose of the invention is to ensure the continuity of the filtration process.
    by continuous removal of the resulting layer.
    This goal is achieved by the fact that the device is equipped with tubular elements mounted on a hermetic partition, with the filter cartridges placed inside the tubular elements and made with channels on their outer surface
    The channels on the filter cartridges are made along a generatrix in the form of a spiral or meander, and the channels have a cross section in the shape of a triangle, rectangle, or flat segment.
    Filter cartridges may be in the form of equilateral polygons adjacent to each other.
    Filter cartridges are provided with plugs installed on the supply side of the initial suspension, HtssMx junction elements installed on the filtrate outlet side, and the device is equipped with a pressure control valve installed on the outlet port of the concentrate chamber.
    权利要求:
    Claims (1)
    [1]
    Figure 1 shows the filtering device with tubular elements and spiral-shaped channels, a longitudinal section} in figure 2 - section AA in figure 1; Fig. 3 shows an embodiment of filter cartridges with straight channels; 4 is another embodiment of the filtering device, a general view; in Fig.5 a filtering device with filter cartridges in the shape of an equilateral polygon, transverse .. section; figb are embodiments of the shape of the grooves; figure 7 - shaped element of the partition; Fig. 8 is an embodiment of a filtering device with square-shaped filter cartridges; figure 9 - transition elements. . The filtering device consists of a housing 1 which includes a cylindrical shell 2 and covers 3 and 4 installed on the ends. On the ledge 5 of the shell there is a partition b with a seal 7 for sealing. Tubular elements 8 are fixed on the partition parallel to the housing axis; filter cartridges 9 are tightly mounted, made of porous ceramics and plugged from the side of the cover 3 with plugs 10. Channels 11 are made along the outer perimeter of the filter cartridges, which can be in the form of a spiral 12 or meander . The open end of the filter cartridge protrudes beyond the tubular element and is fixed in the cover with 4 sealing rings 14. The partition b divides the inside of the housing into the chamber 15 for the initial suspension and the chamber 16 for the concentrate. In the crake 3, an opening 17 is made for the inlet of the suspension, and in the cover 4 there are openings for the outlet of the filtrate 18 communicating with the internal cavity 19 of the filter cartridges. In the shell 2 there is a hole 20 for the discharge of the concentrate, equipped with a pipe 21, on which a control valve 22 is installed. The channels 11, closed from above by the tubular element 8, form closed channels 23 for passing the suspension being filtered along the filtering surface of the cartridge 9 from the chamber 15 to the chamber sixteen. . Filter cartridges can have the shape of a regular equilateral polygon 24 in cross section and are adjacent to each other in the housing tightly. In this case, the channels 23 form with the walls of the adjacent filter cartridges. The remaining space between the shell 2 and the filter cartridges is filled with fitting elements 25, which form an airtight partition between chambers 15 and 16. The channels on the surface of the filter cartridges can have a triangular 26 square 27 or a flat segment type 28. At tight installation, filter cartridges are supplied with transition elements 29 connecting the internal cavity 19 of the cartridge with the outlet of the filtrate separated from the concentrate chamber by a partition 30 in which the free ends of the transition elements are fixed. The filtering device operates as follows. I The filtered liquid through the inlet 17 in the lid 3 enters the chamber 15 of the initial suspension, from where it moves along channel 11 along the filtering surface of the cartridge 9 and into the concentrate chamber 16, from which it is removed from the filter through conduit 21. The pressure in chambers 15 and 16 is regulated by valve 22. As it passes through channel 11, a portion of the filtered fluid passes through the wall of the filter cartridge 9 and enters its internal cavity 19 and through holes 18 is removed from the filter. The suspension particles deposited on the surface of the channels are picked up by the liquid being filtered and discharged into the chamber 16, collecting the concentrate. Part of the concentrate can be re-fed / to the input of the filtering device, circulating it and thus ensuring the continuity of the separation process. Filter cartridges can be used as a substrate for the membrane, and the entire device can be used for ultrafiltration. An important case of the use of a filtering device is the wastewater treatment of chemicals when finishing textiles. Claim 1. A filtering device comprising a housing divided by a hermetic partition into the chamber of the initial suspension and a concentrate chamber with an outlet, porous filter cartridges placed in the concentrate chamber and fixed on the hermetic partition, and supply pipes of the initial suspension, removal of filtrate and concentrate, characterized by the fact that, in order to ensure continuity of the filtering process, the device is equipped with tubular elements mounted on a sealed partition, while the filter The tubes are placed inside the tubular elements and are made with channels on their outer surface. The device according to claim 1, characterized in that the channels of the filter cartridge are formed along a generator in the form of a spiral or meander. 3. The device according to A.1. rectangle or flat segment. 4. A device according to claim 1, characterized in that the filter cartridges are made in the form of equilateral polygons adjoining each other. 5. A device according to claim 1, characterized in that the filter cartridges are provided with plugs * installed on the supply side of the source
    8 67 5 P 2 19
      // II
    FIG. 2
    L
    /
    Fig.Noy. Suspensions and transitional elements installed on the outlet side of the filtrate. 6. The device according to claim 1, which is equipped with a pressure control valve installed on the outlet of the concentrate chamber. Sources of information taken into account in the examination 1. Japanese patent number 43-5428, cl. 72 C 343.21, published 02.04.71.
    21
    26
    FIG, b
    25
    P
    FIG. five
    7
    25
    类似技术:
    公开号 | 公开日 | 专利标题
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    US4211660A|1980-07-08|Filter-purifier cartridge
    SU1346193A1|1987-10-23|Gang filter
    同族专利:
    公开号 | 公开日
    DE2800425C3|1980-08-21|
    US4172038A|1979-10-23|
    DE2800425B2|1979-12-13|
    DE2800425A1|1979-07-12|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US1669461A|1925-08-24|1928-05-15|Charles B Gamble|Gas filter|
    US2014105A|1933-05-31|1935-09-10|Clarence H Dooley|Filter|
    US2577217A|1950-03-09|1951-12-04|Elmer J Wolfer|Filter|HU200285B|1987-03-04|1990-05-28|Tatabanyai Banyak Vallalat|Cross-flow liquid filter operating under pressure|
    US5190651A|1991-06-24|1993-03-02|Sta-Rite Industries, Inc.|Filter cartridge|
    EP0922476A3|1991-06-28|1999-07-07|Pall Corporation|Filter assembly with a spin welded end cap|
    US6103120A|1995-10-23|2000-08-15|Pall Corporation|Fluid processing apparatus|
    JPH10512798A|1994-10-21|1998-12-08|ポールコーポレイション|Fluid treatment equipment|
    JPH08192006A|1995-01-13|1996-07-30|Pall Corp|Filter|
    DE19957641C1|1999-11-30|2001-06-13|Membraflow Gmbh & Co Kg Filter|Filter membrane module with integrated heat exchanger|
    US6397666B1|1999-12-28|2002-06-04|Eastman Kodak Company|Method for generating a solution with a predetermined osmotic pressure|
    US6450014B1|1999-12-28|2002-09-17|Eastman Kodak Company|Method and apparatus for measuring osmotic pressure|
    CN103551043B|2013-11-06|2016-01-20|中国石油化工股份有限公司|A kind of cleaning method of ceramic membrane|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19782800425|DE2800425C3|1978-01-05|1978-01-05|Filter arrangement|
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