• 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:
    Die Filtervorrichtung besteht aus einem Druckbehälter (1) mit vertikal übereinander angeordneten Filterträgern (3) für je eine Schicht eines körnigen Filtermittels. Um ein von Strömungs-, Druck- und Temperaturschwankungen des zu filtrierenden Mediums unabhängiges Filtrationsergebnis zu erhalten, bildet jede von einer trübedurchlässigen, aber filtermittelundurchlässigen Hülle (17) umschlossene Fil- termittelschicht eine Filterpackung (4), die durch die jeweils oben und unten anliegenden Filterträger (3) unter konstantem Druck zusammengepresst ist. Zum Zuführen der Trübe bzw. zum Abführen des Filtrats sind zwischen jeder Filterpackung (4) und den beiden anliegenden Filterträgern (3) Kanäle (18) vorgesehen.
    公开号:SU1417788A3
    申请号:SU833547555
    申请日:1983-02-04
    公开日:1988-08-15
    发明作者:Шаффт Хельмут
    申请人:Хельмут Шаффт (DE)；
    IPC主号:
    专利说明:

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    The invention relates to devices for the purification of liquids by filtration and can be used in the food industry for filtering beverages.
    i The purpose of the invention is to improve the reliability of the filtrate in operation.
    FIG. 1 shows a filter, a longitudinal section; in fig. 2 - filtering element, cross section; in fig. 3 - the same, option; on . / g of FIG. 4 — filter element for two-stage filtration; in fig. 5 is a section A-A in FIG. four.
    The filter consists of a housing 1 with a pressure chamber 2. A central axis 3 is installed in the housing, on which is placed a filter bag made in the form of filter carriers 4 arranged vertically one above the other, having the form of inverse truncated cones between which filter elements are located under compression pressure between two pressure heads 5 and 6. The filter element is made of granular filter material 7, such as kieselguhr enclosed in a fluid-permeable casing 8.
    In order to avoid any displacement of particles of granular filter material inside the filter media 4, the particles of filter material must adhere under the action of externally applied forces, and changes in conditions in the flow area of media through the filter assemblies should not lead to pressure drops causing the displacement of filter material particles. For this reason, any significant change in pressure must be compensated for by a corresponding change in pressure applied to the filter assembly. For this purpose, the pressure head 5 is connected to a clamping actuator .9 consisting of a working cylinder 10 made in the form of a cylinder with an annular piston. With this arrangement, the annular gap 11 is firmly supported by a housing 12 flanged to the pressure chamber 2 and the cylinder 13 is pressed against the pressure head 5, which can move axially along the central axis 3 until it stops, if working fluid is supplied to the working cylinder 10 through line 14. Through line 15. which, like line 14,
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    Connecting alternately to the source, working fluid and collector of working fluid, the working cylinder 10 can be loaded in reverse order, and between pressure heads 5 and 6 the minimum preliminary voltage, as in this, is maintained; In this case, the pressure head 5 is in the stop.
    To evenly distribute the filtered fluid on the filter media x 4, ribbed grids 16 are formed, forming channels 17 for supplying and draining the filtered fluid to the filter elements.
    The nozzle 18 serves to supply the initial suspension to the working cylinder 10, in the upper part of the housing, a degassing valve 19 is located. In the housing 1 there are annular collectors 20 for supplying the initial suspension and annular collectors 21 for draining the filtrate located at the outer edge 22 of the filter media connected to drainage conduits 23. These drainage conduits 23 are evenly placed around the perimeter of the filter media 4 to ensure flow distribution over the filter package and connected to a common upper annular collector 24, to The bottom pipe 25 is connected to the collection of filtrate 26, the pipe 27 serves to drain the filtrate from the filter housing.
    Filter elements can be configured for two-stage filtration. Dp of this, each lower truncated cone is made in the form of a sieve with through-holes 28, to ensure strong support, push bolts 29 are used, which keep one filter-carrier 4 adjacent filter elements apart from each other to form a space of 30 for suspension. To prevent blockage, the holes 28 are covered with filter cloth 31, which is secured with clamp nuts 32 screwed onto clamp bolts 331 This filter weave 31 retains coarse impurities, thus achieving two-stage filtration ...
    Since, due to the granular structure of the filtering material, the filter assemblies do not have a solid simple3.
    it is necessary to give the required shape before installing it into the pressure chamber. For this purpose, it is possible to fasten the filtering material using a certain form soluble in the substance in the form of a body. However, this requires removal by dissolving the substance from the filtering assemblies before the introduction of the filtering device into operation. Another possibility is (Figs. 4 and 5) in fixing the filter elements on the clamping cone 34, which defines the shape of the filter elements. The forces acting on the filter assembly when attaching the filter assembly to the outer surface of the clamping cone provide the necessary grip and thereby the dimensional stability of the filter assembly. After installing these filter assemblies into the housing 1, the clamping cone 34 should be removed to make space for the filter media 4. To this end, the lateral surface 35 of the clamping cone 34 is torn along the generatrix, so that the cone diameter and clamping cone are reduced as a result of mutual displacement of the broken edges removed. To facilitate rupture, there is a cut along the side surface 35 along the generatrix and the junction 36 of the edges of the side surface is covered with a tear film 37. After removing the tear film, the diameter of the clamping cone can be easily reduced to any degree
    the more so that the joint 36 runs obliquely between the edges of the side surface.
    The filter works as follows
    At the beginning of filtration, the filtered slurry is fed from below through the pipe 18 through the working cylinder 10 to the pressure chamber 2 to ensure degassing through the upper and degassing valve 19. As between the central axis 3 and the filter carriers 4, the annular inlet collector 20 remains free, the suspension from the top the hollow cones formed by the filter media 4 can get onto the filter elements, so that when the pressure chamber is degassed at the beginning of the filtration, gas, such as water or 00 (2 ,, contained in the filter elements, is forced out top and out of the pressure chamber through the pipes
    eight
    intended for removal of filtrate. After filling the pressure chamber, the initial fluid is supplied through the upper supply nozzle 38, after passage. day through the filter elements enters the annular collectors 21, located in the zone of the outer edge 22 of the filter media 4 and connected
    with branching and axially diverting conduits 23. These drainage conduits 23 are evenly distributed around the perimeter of the filter media 4 in order to ensure proper distribution of the flow through the filter assemblies and connected to a common upper annular collector 24 which is connected to the filtrate collection 26.
    From this collection 26, the filtrate is withdrawn from the chamber through a riser pipeline 27, and due to the presence of constantly rising channels, the gas displaced upward cannot accumulate in stagnant zones.
    On the contrary, this channel arrangement makes it possible to completely empty the pressure chamber 2, since in the opposite direction along
    the current is constantly passing down the channels. Through the pipe 18 in the lower part of the pressure chamber 2, passing through the annular working cylinder, with the corresponding gas supply, a complete
    emptying without any special measures.
    Of great importance for the smooth operation of the presented filtering device is the creation of sufficient constant compression pressure on the filter media 4 in order to avoid displacement of the filtering material inside the filtering assemblies. Therefore, the filter carriers must be able to transmit the compression forces received through the pressure transfer devices 39 to the filter assemblies. In this case, the filter carriers 4, ck pk- leaking from above and below to the filter element, do not mutually rely in order to create fluid-tight receiving spaces between the filter carriers. For this reason, the filter media
    4 are located with axial gaps. In order to avoid a short circuit between the
    5 14 channels t7 for supplying the suspension and removal of filtrate, on the outer edges 22 and inner edges 40 of the filter media, there is a step 41 to which the filter assembly is tightly pressed by compression pressure, so that in the step zone there can be no flow between the filter carrier and the filter assembly .
    权利要求:
    Claims (3)
    [1]
    1. Filter for cleaning liquids, mainly beverages, comprising a housing with a pressure chamber, a filter bag installed under it between the pressure heads in the form of vertically one above the other on the central axis of the friction sensor, which is in the form of inverse truncated cones, and placed between the last filter elements with the formation of flow channels for the supply of cleaned fluid and removal
    sriе.2
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    filtrate, and ring collectors for supplying the cleaned fluid and removing the filtrate, made respectively for large and smaller bases of truncated cones, characterized in that, in order to increase reliability in operation, one pressure head is fixedly connected to the central axis, and the other has a clamping drive, the filter holders are installed with the possibility of axial reciprocating movement and the filter element is made of granular filter material enclosed in a liquid-permeable space. little bull.
    ten
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    [2]
    2. The filter according to claim 1, characterized in that the filter carriers are equipped with ribbed grids.
    [3]
    3. The filter according to claim 1, about tl and h a-y y and a and c, so that the drive ma made in the form of a hydraulic cylinder or spring. y
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    类似技术:
    公开号 | 公开日 | 专利标题
    SU1417788A3|1988-08-15|Filter for cleaning liquids
    US4081379A|1978-03-28|Filter bag arrangement for a pressure vessel and method of manufacture thereof
    US3441143A|1969-04-29|Plural element filter assembly
    US4647377A|1987-03-03|Filter apparatus
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    US4750999A|1988-06-14|Filter employing barrier
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    US3872015A|1975-03-18|Apparatus for separating fluids into two fractions by means of semipermeable membranes
    US4407720A|1983-10-04|Method and apparatus for filtration of contaminated liquids
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    GB2098499A|1982-11-24|Apparatus and method for fitering particles from a liquid
    US4454033A|1984-06-12|Filtering apparatus
    US3244286A|1966-04-05|Filtration apparatus
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    US2417958A|1947-03-25|Apparatus for reducing the fluid content of a fluid-solid intermixture
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    RU200267U1|2020-10-15|MEMBRANE DEVICE
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    同族专利:
    公开号 | 公开日
    EP0086770B1|1989-08-30|
    DE8226284U1|1982-12-16|
    ES8402727A1|1984-03-01|
    YU21583A|1985-10-31|
    DE3234560C2|1986-03-06|
    AT371359B|1983-06-27|
    DE3234560A1|1983-08-18|
    US4655919A|1987-04-07|
    BR8300689A|1983-11-08|
    EP0086770A3|1986-02-05|
    EP0086770A2|1983-08-24|
    ES519711A0|1984-03-01|
    DE3380478D1|1989-10-05|
    CS235305B2|1985-05-15|
    DD206739A5|1984-02-08|
    ATA50682A|1982-11-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE192887C|1900-01-01|
    US884765A|1908-01-29|1908-04-14|George Schlemmer|Filter.|
    FR755265A|1933-05-08|1933-11-22|Filtration process and filter for clarifying liquids|
    DE648160C|1935-12-01|1937-07-26|Georg Heuchemer|Multi-stage metal gap filter, especially for vehicle engines|
    DE849886C|1942-03-27|1952-09-18|Jacques Muller|Filter for gaseous or liquid substances with automatic cleaning|
    DE944065C|1951-12-14|1956-06-07|Schenk Filterbau Gmbh|Filter device with ring-shaped filter discs lined up on a central tube|
    US2750045A|1953-01-26|1956-06-12|Melville C Hoffmann|Filter|
    CH321854A|1953-09-26|1957-05-31|Vevey Atel Const Mec|Device for filtering liquids|
    DE1104491B|1959-01-15|1961-04-13|Fr August Neidig Soehne Maschi|Filter insert with sieve and support disks stacked on top of one another|
    CH385795A|1961-08-24|1964-12-31|Diebold Pierre|Filter for the filtration of a liquid-solid mixture|
    US3141845A|1962-12-06|1964-07-21|Ametek Inc|Filter element assembly|
    AT269901B|1966-06-07|1969-04-10|Inst Chemieanlagen|Apparatus for filtering liquids|
    FR1541107A|1967-08-24|1968-10-04|filter elements and filters fitted with such elements|
    US3731466A|1971-07-14|1973-05-08|Us Agriculture|Continuous flow multiple trap for low temperature reduced pressure gas chromatography|
    JPS5436991B2|1975-05-21|1979-11-12|
    US4292178A|1979-08-02|1981-09-29|Takehiko Mori|Filtering apparatus|DE3403738C2|1984-02-03|1990-12-20|Helmut 7074 Moegglingen De Schafft|
    DE3448377C2|1984-02-03|1993-01-28|Helmut 7074 Moegglingen De Schafft|Filter element mfr.|
    DE3518718C2|1985-05-24|1987-03-19|Wiederaufarbeitungsanlage Karlsruhe Betriebsgesellschaft Mbh, 7514 Eggenstein-Leopoldshafen, De|
    DE3542449C1|1985-11-30|1987-04-30|Eduard Kumpitsch|Apparatus and method for filtering liquids|
    DE8813974U1|1988-11-08|1988-12-22|Albert Handtmann Armaturenfabrik Gmbh & Co Kg, 7950 Biberach, De|
    DE4120971A1|1991-06-25|1993-01-28|Thomas Handtmann|FILTERING METHOD AND FILTERING DEVICE FOR FILTERING LIQUIDS|
    DE4309366C1|1993-03-23|1994-04-21|Thomas Handtmann|Stackable filter holder - with distributor element seal pref. of polyamide, e.g. for sterile filtration of beer|
    DE4332361A1|1993-09-23|1995-03-30|Schenk Filterbau Gmbh|Device for receiving stabilizing agents for beverages and other liquids|
    DE19705855A1|1997-02-15|1998-09-03|Seitz Filter Werke|Filtration device|
    US6171536B1|1998-04-10|2001-01-09|Arteva North America S.A.R.L.|Apparatus and method for melt spinning of molten polymeric material|
    DE10003678C2|2000-01-28|2002-11-14|Seitz Schenk Filtersystems Gmb|Device and method for deep filtration|
    CN101422663B|2007-11-02|2012-11-28|王自治|Efficient rinsing desorption technique of sand filteration tank|
    EP2168469B1|2008-09-25|2013-07-17|Nestec S.A.|Filter cartridge for a beverage machine and beverage machine with a filter cartridge|
    CN111567813A|2020-04-26|2020-08-25|安徽省金宜食品有限公司|Fruit juice extraction equipment for beverage production|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    AT0050682A|AT371359B|1982-02-11|1982-02-11|FILTER DEVICE, ESPECIALLY FOR BEVERAGES|
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