• 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:
    An intermittently operating pressurized filter for concentrating a solid matter suspension, comprising a filtering tank with an inlet conduit provided with a feed pump for introducing under pressure the suspension to be filtered, and a draining conduit provided with valve for removal of the concentrated sludge, and a plurality of filtering elements suspended from the roof, through which the filtrate flows and of which the interior communicates with a filtrate collecting tank located above and which thereby collect on their external surface sludge, which has been arranged to be periodically removed by voiding the pressure within the filtering tank by opening for the suspension therein an exit flow path through a draining conduit. The filtrate in the collecting tank will pass in countercurrent fashion through the filtering elements. In the pressurized filter the filtrate has been arranged to be removed during the filtering step by a filtrate draining conduit departing from the collecting tank, by effect of the pressure produced by the feed pump in the suspension inlet conduit. The collecting tank is of enclosed construction. The sludge has been arranged to be removed from the surface of the filtering elements by the aid of the hydrostatic pressure of the filtrate in the collecting tank, by placing th draining conduit of the collecting tank under atmospheric pressure.
    公开号:SU1069604A3
    申请号:SU792850265
    申请日:1979-11-28
    公开日:1984-01-23
    发明作者:Лумико Юха；Ланкинен Матти；Саволайнен Якко；Толванен Мартти；Луукайнен Ирхе；Энгдал Хольгер
    申请人:Энсо Гутцайт Осакейхтие (Фирма)；
    IPC主号:
    专利说明:

    2. The filter according to Claims 2, characterized in that the upper chamber for removing the filtrate is syabzhen by vertical partitions dividing it into sections, each of which is made up with an outlet branch pipe for the filtrate connected through a stop valve to a pipeline for draining the filtrate.
    one
    This invention relates to filtration, in particular to cartridge filtrate.
    A pressure filter is known that comprises a housing divided by a partition with filter elements with an outer filtration surface to an upper chamber for draining filtrate and supplying fluid for regenerating filter elements and a lower filtration chamber with an inlet pipe connected to the feed Pump and the pipeline through a check valve. m with valves for removal of concentrated sludge connected to a container for concentrated sludge 1.
    A disadvantage of the known filter is the difficulty of removing sediment from the filter elements.
    The goal is to simplify the removal of sediment from the filter elements.
    This goal is achieved by the fact that in a pressure filter containing a housing divided by a partition with filtering elements with an outer filtration surface to the upper chamber for draining the filtrate and supplying fluid for regeneration of filtering filters: and lower chamber filtration with inlet pipe connected through valves with a feed pump and a pipeline with valves for discharging concentrated sludge connected to a container for concentrated sludge, supply line w dkosti for the regeneration of filter elements is connected at one end with the container for the concentrated sludge and the other - with a conduit for withdrawing a filtrate before its stop valve connected to atmosphere.
    It is advisable to provide the upper chamber for the removal of the filtrate with vertical partitions dividing it into sections, each of which is made with a by-pass branch for the filtrate connected to a pipeline for the removal of the filtrate through the shut-off fittings.
    FIG. 1 shows the filter section; in fig. 2 - filter with a vertical partition, cut; in fig. 3 shows section A-A in FIG. 2
    The filter includes a housing 1, divided by a partition 2 into an upper chamber 3 for
    discharging the filtrate and supplying liquid for the regeneration of the filter elements 4 fixed in the partition 2.
    Cereborne 2 with a lower part of the housing 1 forms the lower filtration chamber 5 with an inlet pipe 6 connected through a shut-off valve 7c with a feed pump 8. A pipe 9 for discharging concentrated sediment through a shut-off valve 10 is connected to a tank 11 for a concentrated sludge, which through
    5, the pipeline with valves 12 is connected to pipe 13 to drain the filtrate and the regeneration fluid, which is connected to the atmosphere through valves 14. The upper chamber 3 is divided by one or several vertical partitions 15 into sections 16, each of which is connected by means of branch pipes 17 with stop valves to the pipeline 13.
    5 The filter works as follows.
    The liquid to be filtered, predominantly milk of lime, enters the lower chamber 5 through line 6 under the action of pump 8. The liquid under pressure under pressure in the lower chamber is filtered through the filter elements 4, the filtrate enters the upper chamber 3, and the solid particles are deposited on the filter elements. The filtrate enters the upper chamber 3, from where it is transported via pipeline 13 to the autoclave unit.
    5 or in cumulative capacity. The removal of sludge that accumulates on the filter elements 4 is retracted by stopping the feed pump 8 when the shut-off valves 7 and 14 are closed. Shut-off valves
    0 10 and 12 open. The filtrate from the upper chamber flows through the filtering elements 4 into the lower chamber 5, at the same time the layer seated on the filtering elements separates. Sludge from the lower chamber through conduit 9 enters tank 11, from where the mixture is injected either into the filter section or into the cleaner. During the washing stage, air passes through the check valve 12 through the filter.
    After the filter has been emptied, the shut-off valve 10 is closed and the valve 7 is opened and the feed pump 8 is started. When the filter is full, the shut-off valve 12 is closed and the valve 14 is opened. In this way, another filtration cycle begins. All these operations are automated.
    The filter is operated periodically, with its operation divided by the filtration period and the washing period, and the duration of the filtration period is determined by the sludge content.
    The implementation of the upper chamber with vertical partitions dividing it into sections, each of which has a pipeline with shut-off valves connected to the pipeline, allows you to turn off any section when a contaminated filtrate enters it.
    13
    ll
    .2
    Fig.Z
    权利要求:
    Claims (2)
    [1]
    1. FILTER OPERATING
    UNDER PRESSURE, comprising a housing divided by a partition with filtering elements with an outer filtration surface on the upper chamber for filtrate discharge and fluid supply for regeneration of the filtering elements and the lower filtration chamber with an inlet pipe connected through shut-off valves to the feed pump and a pipeline with shut-off valves for drainage concentrated sludge connected to a container for concentrated sludge, characterized in that, in order to simplify the removal of sediment from the filter elements, oprovod liquid supply for the regeneration of filter elements is connected at one end with the container for the concentrated sludge and the other - with a conduit for discharging the filtrate prior to its locking arma ture connected with the atmosphere.
    [2]
    2. Filter by π. 1, characterized in that the upper chamber for discharging the filtrate is provided with vertical partitions dividing it into sections, each of which is made with a drain pipe for the filtrate, connected through a stop valve with a pipe for discharging the filtrate.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1069604A3|1984-01-23|Pressure filter
    US4818420A|1989-04-04|Backwash filter
    GB1351955A|1974-05-15|Filtration of fluids
    JPH07185213A|1995-07-25|Method of processing back flow fluid of back flow filter and settling device for cleaning fluid
    US3342334A|1967-09-19|Filter and scouring gas blower system
    JPH06170364A|1994-06-21|Filter device using permeation membrane
    US5013457A|1991-05-07|Pressurized backwash filter
    SU1181521A3|1985-09-23|Batch-type filter operating under pressure
    RU2411719C1|2011-02-20|Installation to treat water mainly for drip irrigation systems
    JPH0768107A|1995-03-14|Sludge filtering and concentrating device
    US3549012A|1970-12-22|Method and equipment for automatic washing of rapid filters
    JPH07251041A|1995-10-03|Membrane separation apparatus and washing method therefor
    JP4150119B2|2008-09-17|Sludge concentration method
    KR900002815B1|1990-05-01|Regenerating method of filter bed
    RU2050921C1|1995-12-27|Device for removing mechanical additives and water from oil and oil products
    KR960003781A|1996-02-23|Simultaneous filtration method and filtering device for filtration member
    SU1611381A1|1990-12-07|Filter for purifying water
    SU1500627A1|1989-08-15|Apparatus for cleaning waste water from petroleum products and mechanical impurities
    SU560627A1|1977-06-05|Liquid clarification filter
    SU829135A1|1981-05-15|Filter for cleaning sewage
    SU1270117A1|1986-11-15|Installation for removing suspended substances and petroleum products from waste water
    RU1787042C|1993-01-07|Water cleaning device
    SU560628A1|1977-06-05|Cartridge filter
    RU2046003C1|1995-10-20|Membrane plant
    KR910000468Y1|1991-01-25|Automatic upward filtering apparatus
    同族专利:
    公开号 | 公开日
    FI62772C|1983-03-10|
    NO148839C|1984-01-11|
    UA2167A1|1994-12-26|
    IN151556B|1983-05-21|
    FR2442648B1|1986-10-24|
    JPS5953082B2|1984-12-22|
    SE7909774L|1980-05-29|
    CA1129786A|1982-08-17|
    FR2442648A1|1980-06-27|
    FI783633A|1980-05-29|
    NO148839B|1983-09-19|
    AT376904B|1985-01-25|
    ATA747379A|1984-06-15|
    JPS5588813A|1980-07-04|
    DE2947579A1|1980-06-04|
    US4264445A|1981-04-28|
    BR7907738A|1980-07-22|
    FI62772B|1982-11-30|
    SE435681B|1984-10-15|
    NO793854L|1980-05-29|
    AR221388A1|1981-01-30|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2562699A|1949-06-17|1951-07-31|Permutit Co|Filter and method of backwashing same|
    US2862622A|1955-08-10|1958-12-02|Detrex Chem Ind|Filters|
    DE2140159C3|1971-08-11|1975-07-31|Braunschweigische Maschinenbauanstalt, 3300 Braunschweig|Continuously working thickening filter for the sugar industry|FI65918C|1980-05-29|1984-08-10|Enso Gutzeit Oy|FOERFARANDE FOER ATT AVSKILJA SODASEDIMENT FRAON GROENLUTSUSPENSION GENOM FILTRERING|
    AT27407T|1984-03-08|1987-06-15|Heinz Schumacher|METHOD AND DEVICE FOR CLEANING FILTER ELEMENTS, IN PARTICULAR FILTER CANDLES.|
    US4525274A|1984-04-06|1985-06-25|Dorr-Oliver Incorporated|Filtrate discharge system for pressure filter|
    US4528103A|1984-04-06|1985-07-09|Dorr-Oliver Incorporated|Pressure filter|
    JPS6365920A|1986-09-04|1988-03-24|Mitaka Kogyosho:Kk|Washing of filter medium of filter|
    US4861498A|1987-12-30|1989-08-29|R & L Filtration Limited|Backwash system for filter-thickeners|
    ES2013662A6|1989-02-21|1990-05-16|Filter system for liquids with particles in suspension|
    JPH02150006U|1989-05-26|1990-12-25|
    SE501068C2|1989-10-04|1994-11-07|Caustec Ab|Method and apparatus for filtering a suspension|
    NO172882C|1991-06-14|1993-09-22|Goetaverken Energy Ab|PROCEDURE FOR REGULATING A FILTERING DEVICE|
    US5518609A|1992-04-14|1996-05-21|Caustec|Device for cleaning of caustic liquid mixtures|
    FI103870B1|1996-12-30|1999-10-15|Kari Aalto|Method and apparatus for treating fluid|
    SE0100411L|2001-02-07|2001-12-10|Kvaerner Pulping Tech|Pipe system for receiving and transporting mesa from a white liquor filter|
    SE0702702L|2007-12-06|2008-09-09|Metso Fiber Karlstad Ab|System for receiving and transporting mesa from a white liquor filter|
    CN103967775B|2014-05-21|2016-03-23|何丽进|There is the water plug of liquid reservoir tank and sliding conical bearing|
    CN107963797A|2016-10-19|2018-04-27|北京华德创业环保设备有限公司|A kind of concentrated phase red mud pipe carrying method|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI783633A|FI62772C|1978-11-28|1978-11-28|TRYCKFILTER|
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