• 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:
    Periodically operating pressure filter for the concentration of a solid matter suspension, comprising a filtering tank with an input conduit for introducing the suspension to be filtered under pressure, and a drain conduit for removal of the concentrated sludge, and a number of filtering elements suspended from the ceiling, through which the filtrate flows and which are internally in communication with a filtrate collecting tank located above and which thereby collect sludge on their outer surface. The sludge has been arranged to be periodically detached by making the pressure inside the filtering element higher than on its outside. The filtrate is under atmospheric pressure in the collecting tank. For detaching the sludge periodically from the outer surfaces on the filtering elements the pressure has been arranged to be removable from the filtering tank by opening for the suspension residing there, an exit flow, whereby the filtrate in the collecting tank will pass under hydrostatic pressure effect in counter-current fashion through the filtering elements.
    公开号:SU1181521A3
    申请号:SU792738102
    申请日:1979-03-12
    公开日:1985-09-23
    发明作者:Саволайнен Якко；Энгдал Хольгер；Лууккайнен Ирье；Тольванен Марти；Суракка Йорма
    申请人:Энсо-Гутцайт Осакейхтие (Фирма)；
    IPC主号:
    专利说明:

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    This invention relates to pressure batch filters designed to separate solids from a slurry and can be used to filter white liquid from known milk in the manufacture of synthetic fertilizers on sulphate cellulose waters, as well as in other industries.
    The purpose of the invention is to increase the efficiency of the filter in operation.
    FIG. 1 shows a longitudinal section filter; in fig. 2 shows section A-A in FIG. one.
    The filter includes a housing 1 divided by a partition 2 with filtering elements 3 into the upper chamber 4 with openings 5 for draining the filtrate and the lower filtration chamber 6. Radial vertical partitions 7 are installed in the upper chamber 4, which divide chamber 4 into sections 8, each of which is equipped with a drain pipe 9 with shut-off valves 10. The pipelines 9 of contaminated filtrate are connected by a common annular cavity 11 located outside the housing 1. Part of the chamber 4 on its outer surface is a collector 12 for removal of the filtrate. Each section 8 has an inlet 1E for sampling the filtrate. The filter element 3 consists of a filter casing 14 on which a sediment layer 15 is formed, and the filter casing 14 itself is placed on a frame 16 made of a metal mesh welded to a mirror 17 of the filter element 3. The bottom chamber 6 is provided with an inlet pipe 18, from which down pipeline 19 with a valve 20, which is normally closed, moves away. In the lower part of chamber 6 there is a rotating blade 21, which serves to prevent sediment from sticking to the bottom of chamber 6, and a drain channel 22. The collector 12 has a pipe 23 for filter removal to the consumer, and the annular cavity 11 has a pipe 24 for discharging contaminated filtrate.
    The filter works as follows
    The suspension to be filtered enters the pressure chamber 6 of the filter through the inlet pipe 18, passes into the inner 12
    a new cavity of filter elements 3, forming a sediment 15 a on their outer surface C. The filtrate passes inside the filter elements 3. The metal mesh 16 prevents the filter elements 3 from squeezing. From the internal cavity of the group of filter elements 3, the filtrate enters the upper chamber 4 divided by partitions 7 into sections 8. Since the partitions 7 have a greater height than the lower edge of the opening 5, the filtrate that is located in different sections x5 cannot move until the moment of overflow. As the filtrate is collected in sections 8, it is poured through the openings 5 into the collector 12, from where it passes through the pipe 23 to the consumer,
    From each section 8, a sample is periodically taken through the nozzle 13. If the sample shows that contaminated filtrate enters this section, i.e. if any of the filter casing 14 is damaged, this section is removed from the filtration process. It opens the valve 10 and the contaminated filtrate through pipe 9 enters the common annular cavity 11 and then through pipe 24 to the suction line of the pump (not shown), from where it is again supplied to the inlet pipe 18.
    The inlet of the conduit 9 is located below the upper edge of the partitions 7, but above the bottom of the section 8 This always ensures the presence of filtrate in section 8, which is necessary to remove the sediment layer 15 accumulated on the filter casing 14.
    In order to remove the sediment layer 15, valve 20 is opened, as a result of which the pressure in chamber 6 is reduced and the hydrostatic pressure of the fluid in section 8 causes the contaminated filtrate to flow in the opposite direction through the frontal elements 3. As a result, sediment layer 15 is removed and falls to the bottom of chamber 6 The precipitate is discharged through the drain channel 22, and the rotating blade 21 prevents the sediment from sticking to the bottom of the chamber 6. Then the valve 20 is removed and the filtration begins again.
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    权利要求:
    Claims (1)
    [1]
    PERIODIC ACTION FILTER OPERATING UNDER PRESSURE, comprising a cylindrical body divided by a baffle with filter elements with an outer filtration surface into an upper chamber with openings for draining the filtrate and periodically supplying liquid for regenerating filter elements and a lower filtration chamber with an inlet pipe, a collector for draining filtrate, characterized in that, in order to increase the efficiency of the filtrate in operation, the upper chamber is equipped with radial vertical partitions with the formation sections, each of which is equipped with a drain pipe with shutoff valves located below the opening for the filtrate, with the upper edges of the partitions located. above the hole for drainage of the filtrate.
    ... "SU 1181521>
    1 "81521
    类似技术:
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    SU1174389A1|1985-08-23|Dewatering apparatus
    JP2503079Y2|1996-06-26|Tandem type automatic strainer
    SU563992A1|1977-07-05|Apparatus for sewage treatment
    同族专利:
    公开号 | 公开日
    JPS54128066A|1979-10-04|
    FI55937C|1979-11-12|
    NO790838L|1979-09-14|
    ATA182279A|1983-06-15|
    JPS6145482B2|1986-10-08|
    FI55937B|1979-07-31|
    CA1120868A|1982-03-30|
    BR7901521A|1979-10-16|
    AT373503B|1984-01-25|
    NO147862B|1983-03-21|
    US4243533A|1981-01-06|
    NO147862C|1983-06-29|
    FR2419744A1|1979-10-12|
    SE435137B|1984-09-10|
    SE7902173L|1979-09-14|
    FR2419744B1|1986-01-24|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2391534A|1944-06-02|1945-12-25|Air Preheater|Separator|
    US2862622A|1955-08-10|1958-12-02|Detrex Chem Ind|Filters|
    US3356215A|1965-04-22|1967-12-05|Dorr Oliver Inc|Apparatus and method for the filtration-thickening of suspensions of solids|
    US3513638A|1968-03-08|1970-05-26|Henry T Young|Filter|
    US3524548A|1968-09-16|1970-08-18|Kaiser Aluminium Chem Corp|Filter medium for molten metal|
    US4039441A|1974-04-08|1977-08-02|The De Laval Separator Company|Coalescing method and apparatus|
    US4165283A|1976-10-28|1979-08-21|Industrial Pollution Control Corp.|Multi-stage purification system|US4528103A|1984-04-06|1985-07-09|Dorr-Oliver Incorporated|Pressure filter|
    US4525274A|1984-04-06|1985-06-25|Dorr-Oliver Incorporated|Filtrate discharge system for pressure filter|
    US4861498A|1987-12-30|1989-08-29|R & L Filtration Limited|Backwash system for filter-thickeners|
    DE3913744A1|1988-06-18|1990-10-31|Krupp Koppers Gmbh|PRINT FILTER|
    US4994332A|1989-07-11|1991-02-19|Eltech Systems Corporation|Metal hydroxide crystallizer and filter|
    US5518609A|1992-04-14|1996-05-21|Caustec|Device for cleaning of caustic liquid mixtures|
    US5441633A|1992-09-25|1995-08-15|Schewitz; Jonathan|Liquid filter using filtration aid|
    US5569381A|1995-05-24|1996-10-29|Spokane Industries, Inc.|Upflow clarifier|
    GB9805233D0|1998-03-12|1998-05-06|Barth Richard N|A filter|
    US7799235B2|2004-07-23|2010-09-21|Contech Stormwater Solutions, Inc.|Fluid filter system and related method|
    US8123935B2|2007-08-15|2012-02-28|Monteco Ltd.|Filter for removing sediment from water|
    US8287726B2|2007-08-15|2012-10-16|Monteco Ltd|Filter for removing sediment from water|
    FI123885B|2011-03-16|2013-11-29|Andritz Oy|Pressure filter and method in connection therewith|
    FI123587B|2011-10-04|2013-07-31|Andritz Oy|PRESSURE FILTER|
    CN111185036B|2020-01-13|2021-08-31|池州市三真智能科技有限公司|Agricultural sewage treatment equipment|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI780792A|FI55937C|1978-03-13|1978-03-13|TRYCKFILTER|
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