• 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:
    1. A method of cleaning multi-chamber bag filters by supplying purge inert gas to one of the chambers that are turned off from the filtering process in the opposite direction to filtration, characterized in that, in order to increase the efficiency of the method by reducing the consumption of inert pelvis, before supplying purge inert gas, some of the chambers under the filter element are filled with inert gas. CO with with about 00 with
    公开号:SU1109039A3
    申请号:SU802889599
    申请日:1980-02-28
    公开日:1984-08-15
    发明作者:Ремилье Жан
    申请人:Эр Эндюстри (Фирма)；
    IPC主号:
    专利说明:

    2. A method according to claim 1, characterized in that an additional stream of inert gas is fed in countercurrent into the chamber after the purging of inert gas is supplied.
    3. A device for cleaning multi-chamber bag filters comprising a housing including filter chambers, each of which is provided with at least one bag filter element
    with the outer surface of the filter, exhaust chambers connected
    through valves with a collecting chamber and through valves with a purge manifold for supplying a purge inert gas, an inlet chamber common to all filter chambers, with an inlet pipe and a chamber for settled dust, characterized in that, in order to prevent an explosion hazard and to save purge inert gas The device is additionally provided with a manifold for supplying an inert gas interconnected through a stop valve with each outlet chamber.
    The invention relates to filtering, in particular to filtering devices with several chambers, where bag filters are installed, and methods of cleaning bag filters.
    A known method of cleaning multi-chamber bag filters by supplying purge inert gas to one of the cameras that are disconnected from filtration in the direction opposite to that of CU.
    The disadvantage of this method is the large consumption of inert gas, which leads to high economic costs.
    The purpose of the invention is to increase the efficiency of the process by reducing the consumption of inert gas. A device for purifying gas from impurities is known, comprising a housing, including filter chambers, each of which is provided with at least one tubular filter element with an external filtering surface, outlet chambers connected via valves to a collecting chamber and through gates to a purge manifold for supplying a purge an inert gas, an inlet chamber, which is common to all filter chambers, with an inlet pattern for the sponge, and a chamber for settled space. MZ The disadvantages of the known device are high flow rates of the blowdown valve. gas and explosion hazard of the installation.
    The purpose of the invention is to prevent the danger of an explosion and to save the purge inert gas.
    This goal is achieved in that according to the method of cleaning multi-chamber sleeve filters by supplying purge inert gas to one of the chambers that are turned off from the filtering process in the direction opposite to filtration, before supplying purge inert gas, a portion of this chamber under the filter element is filled with an inert gas.
    It is advisable in the specified chamber after the supply of purge inert gas to the top of the filter element to submit a countercurrent additional stream of inert gas.
    The goal is also achieved by the fact that the device for cleaning multi-chamber bag filters containing a housing includes 1st filter chambers, each of which is equipped with at least one bag filter element with an external filtering surface, flow chambers connected through valves to a collection chamber and through gates with a purge manifold for supplying a purge inert gas, an inlet chamber common to all filter chambers, with an inlet port and a chamber for settled dust, additionally sleep Jeno collector dp supplying an inert gas through the locking vzaimyosv bound veins, Til to each discharge chamber. The proposed method proceeds with the following. The drainage chamber to be cleaned is turned off from the filtration process I and a countercurrent purge of the bag filter element with an inert gas with preservation of the accumulated dust on the surface 4 of the spinning element, i.e. Partial production: filling of the filter chamber under the filter element, after which an additional stream of inert gas is fed in with a countercurrent with discharge of settled dust from the filter element. Before purging, it is possible to partially fill with an inert gas and a filter chamber at the top of the filter element. On. The drawing shows schematically the device, the section. The device comprises a housing 1 with several filter chambers 2, each of which includes at least one bag filter element 3 with an external filter surface. Under the filter chambers there is an inlet chamber 4 with an inlet manifold 5. The internal cavity of the bag filter elements of each filter chamber is from dinene with its own exhaust chamber 6, and each chamber 6 through valves 7 with a collecting chamber 8 and through the gates 9 s a purge manifold 10. The purge means for supplying an inert gas to each outlet chamber 6 are independently controlled and are supplied from an inert gas source 11 with such a flow rate that it does not cause the dust layer to separate from the outer surface STI baghouse filter elements. A bunker is provided in the lower part of the housing under each filter chamber. The device additionally provides a manifold 12 for supplying an inert gas interconnected via a shut-off valve 13 with each outflow chamber 6 and connected to an Additional source 14 of inert gas. The shut-off valves i3 have separate control for each outlet chamber 6. The device operates as follows. At first filtering takes place, valves 7 of each outlet chamber 6 are open, and valves 9 and shut-off valve 13 of collectors with inert purge gas are closed. Regeneration is performed by shutting off valve 7 with one of the chambers. The valve 9 of the purge manifold 10 is opened to carry out the first purge, then the valve 9 is closed and the valve 13 of the collector 12 is opened to separate the settled dust. After closing the valve 13, the dumped dust is removed from the hopper. The first purge can be repeated. The filtering is regenerated: their elements of other chambers are produced in a similar way, after which the device switches to the filtering mode.
    权利要求:
    Claims (3)
    [1]
    1. A method of cleaning multi-chamber bag filters by supplying a purge of inert gas to one of the chambers that are turned off from the filtering process in the reverse filtration direction, characterized in that, in order to increase the efficiency of the method by reducing the consumption of inert gas, part of the specified cameras under the filter
    09) SU (D) 1; 1 09039
    [2]
    2. The method according to claim 1, characterized in that an additional inert gas stream is supplied countercurrently to the said chamber after the inert gas purge is fed into the filter element.
    [3]
    3. A device for cleaning multi-chamber bag filters, comprising a housing including filter chambers, each of which is equipped with at least one bag filter element with an outer filter surface, exhaust chambers connected through valves to the collection chamber and through valves with a purge manifold for supplying a purge inert gas, an inlet chamber common to all filter chambers, with an inlet pipe and a chamber for settled dust, characterized in that, in order to prevent the risk of explosion and saving inert gas purge, the device is additionally equipped with a collector for inert gas supply, interconnected through a shut-off valve with each exhaust chamber.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1109039A3|1984-08-15|Method of cleaning multichamber bag filters and device for effecting same
    US3868237A|1975-02-25|Dust filter
    US3513638A|1970-05-26|Filter
    SU1069604A3|1984-01-23|Pressure filter
    US3861893A|1975-01-21|Filter device with scavenger system
    US2326484A|1943-08-10|Filtering apparatus
    JP3831876B2|2006-10-11|Apparatus and method for cleaning filter elements
    KR100689855B1|2007-03-08|Automatic backwash filter
    CN109502816A|2019-03-22|A kind of Zhi Xian factory sewage disposal system and method
    GB1392084A|1975-04-23|Apparatus for filtration
    CN214551799U|2021-11-02|Renewable pre-coated membrane medium filter unit
    CN208389473U|2019-01-18|A kind of fixed bed filtering purification system
    CN214862257U|2021-11-26|Chamber air box pulse bag-type dust collector
    GB2128098A|1984-04-26|Multilayer filter bed regeneration
    JP3218934B2|2001-10-15|Media transfer device for mobile filter bed filter
    SU747519A1|1980-07-15|Filter for removing suspended substances and non-soluble liquids from sewage
    SU364332A1|1972-12-28|«VIILOTECA Southern Research Institute of Hydraulic Engineering and Land ReclamationFILTER for water purification
    JP3294021B2|2002-06-17|Freestanding bag filter
    SU799808A1|1981-01-30|Filter-adsorber
    SU1526749A2|1989-12-07|Filter for purifying water
    SU1103886A1|1984-07-23|Bag filter
    SU388762A1|1979-01-30|Method of regeneration of framework filtering bags
    RU1816474C|1993-05-23|Liquid cleaning radial filter
    SU700167A1|1979-11-30|Sand filter for purifying vodka from activated carbon
    SU1033157A1|1983-08-07|Unit for cleaning liquid by filtering
    同族专利:
    公开号 | 公开日
    US4292053A|1981-09-29|
    FR2450628B1|1983-08-19|
    FR2450628A1|1980-10-03|
    JPS55119410A|1980-09-13|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR636274A|1928-04-05|
    GB156753A|1914-04-29|1921-06-16|Halbergerhuette Gmbh|New or improved method of treating or handling filter plants employed for the filtration of combustible gases|
    GB344227A|1930-03-06|1931-03-05|John Philip Baxter|Improvements in the removal of solid particles from hot or corrosive gases|
    US3178868A|1959-07-06|1965-04-20|Pangborn Corp|Dust filter with pressure jet cleaning|
    FR1344468A|1962-10-18|1963-11-29|Unclogging device and filtering devices or sediment separators incorporating this device|
    US3212237A|1963-02-12|1965-10-19|Ashland Oil Inc|Method and apparatus for filtering gas streams|
    FR2058422A5|1969-09-01|1971-05-28|Commissariat Energie Atomique|Gas filter with automatic reverse - pressure cleaner|
    FR2132929A5|1971-04-01|1972-11-24|Usuelli Imero Figli Eco|Gas filter automatically cleaned - by reversing gas flow consecutively through several discrete filter elements|
    US3893833A|1972-04-26|1975-07-08|Flex Kleen Corp|Compartmented pulse jet dust collector|
    US4058379A|1975-05-27|1977-11-15|Phillips Petroleum Company|Filtering apparatus|
    US4046526A|1976-01-12|1977-09-06|Aerodyne Development Corporation|Bag collector for dirt with selective half-bag cleaning|
    US4022595A|1976-01-30|1977-05-10|Air-O-Matics, Inc.|Self-cleaning filter arrangement|
    JPS6018204B2|1977-01-20|1985-05-09|Kawasaki Heavy Ind Ltd|US4590039A|1982-06-02|1986-05-20|Phillips Petroleum Company|Auto-preseparation of carbon black|
    JPS58132524U|1982-02-26|1983-09-07|
    US4507130A|1983-03-21|1985-03-26|General Electric Environmental Services, Inc.|Staggered method cleaning cycle for fabric filter system including multiple-baghouses|
    US4701192A|1985-05-31|1987-10-20|Tidewater Industrial Components, Inc.|Vacuum system|
    JPH0341769Y2|1986-06-11|1991-09-02|
    US4719791A|1986-12-05|1988-01-19|Ets, Inc.|Individual filter bag monitoring system for baghouses|
    US4759781A|1987-03-09|1988-07-26|Olson Robert P|Filtering and dust collecting apparatus|
    US5062872A|1989-05-12|1991-11-05|Pneumafil Corporation|Air filter with horizontal filter elements|
    US5185019A|1990-10-22|1993-02-09|Westinghouse Electric Corp.|Filtering apparatus|
    CH683502A5|1991-06-05|1994-03-31|Galipag|Air-filter device.|
    US5108473A|1991-06-19|1992-04-28|Hayden Sr Robert E|Dust collector with atmospheric backflush|
    US5261934A|1992-03-17|1993-11-16|Nordson Corporation|Powder collection method and apparatus with isolated filter pulsing and compression mounted cartridges|
    US5549734A|1995-03-08|1996-08-27|Astec Industries, Inc.|Baghouse cleaning method|
    JP3108639B2|1996-11-12|2000-11-13|核燃料サイクル開発機構|Cyclone type dust collector|
    DE10246126A1|2002-10-01|2004-04-15|Nordson Corp., Westlake|Filter device and method for cleaning a gas loaded with powder particles|
    CN100475310C|2005-10-11|2009-04-08|塞巴斯蒂安·崔玛|Process and apparatus for purifying filter material of gas filter|
    SE0502856L|2005-12-22|2007-05-22|Alstom Technology Ltd|Textile filter with fluidized bed, and ways to maintain it|
    DE502007005411D1|2007-06-01|2010-12-02|Balcke Duerr Gmbh|Method for backwashing filters|
    EP3031508A3|2014-12-08|2016-10-26|Svoboda Piotr Slebioda|The louver regeneration system for horizontal bag filter|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7905659A|FR2450628B1|1979-03-05|1979-03-05|
    [返回顶部]