Lisc filter
专利摘要:
Disk filter comprising a tank for the liquid to be filtered, a tubular shaft carrying, spaced in its longitudinal direction, filtering disks which consist of functionally independent, hollow filtering sectors communicating through holes made in the mantle of the tubular shaft and located at the tips of the sectors with the interior space of the tubular shaft, the different filtrates coming from the filtering sectors being removed from the different chambers with the aid of vacuum introduced into said interior space. The chambers are established when within the tubular shaft there is placed a slide member which is stationary as the shaft rotates and which divides the interior of the shaft in the transversal direction into sectors and which is confined by ends at either of the shaft. 公开号:SU847898A3 申请号:SU772501365 申请日:1977-07-01 公开日:1981-07-15 发明作者:Коскинен Энсио 申请人:Энсо-Гутцайт Осакейхтие (Фирма); IPC主号:
专利说明:
one This invention relates to filtration, in particular, to disk filtrates for cleaning liquids. A disc filter for cleaning fluid is known, comprising a bath, a hollow shaft with filter discs made of sectors communicating with a shaft cavity, filtrate drain pipes and a source of vacuum JQ The disadvantage of this filter is the initial clogging of the filtrate with impurities and its mixing with the cleaner filtrate. The purpose of the invention is improving the cleaning efficiency. The goal is achieved by the fact that the filter is fixedly equipped with a ribbed 20 core mounted inside the shaft with an end wall separating: the shaft cavity into the chambers, the filtrate drainage, X1 each of the co-i is connected to the drainage outlet of the filtrate IT regeneration chamber connected to the source vacuum. It is advisable to supply the filter with a bracket on which a ribbed liner is fixed. FIG. 1 shows a filter, general view, section; FIG. 2 - section A-A in Fig. 1; ya in Fig. 3 - section B-B in Fig. 1.
权利要求:
Claims (2) [1] The filter includes a bath 1 in which the fiber suspension to be filtered is fed. Hollow shaft 2 is a pipe that runs along the entire length of bath 1 and rests at its ends on bearings 3 installed at the ends of bath 1. On the shaft 2, filter disks are installed perpendicular to it at some distance from each other. Sectors 4 having a surface made of a frequent mesh made of plastic, so that zag: keep on their surface fibers that are desirable to filter out from the suspension in bath 1, but can pass liquid. To remove floor filtrate, the inside of each sector is connected through holes 5 in the shaft wall with the inside of shaft 2, a ribbed liner 6 is placed inside the shaft, having a length equal to the length of the entire shaft, and which divides the shaft inside in the transverse direction into three separate chambers: chambers the filtrate outlet 7 and 8 and the regeneration chamber 9. At the ends of the liner there are end walls 10 and 11 having a diameter corresponding to the inner diameter of the shaft 2. The filter is equipped with a bracket 12 fixed on the end wall of the shaft, so that the contributions The w 6 cannot rotate in place with the shaft 2 when the latter is rotated by a drive (not shown) connected to the roller pin 13. Through the wall 11 into the chamber 7 and 8 are inserted the drainage pipes of the filtrate 14 and 15, through which the filtrate is taken from the shaft 2 Nozzles 14 and 15 and through h0x also chambers 7 and ..8 communicate with a vacuum source (not shown. The disc filter works as follows. When the disc filter rotates, each sector 4 in turn is immersed in a fiber suspension of the bath. Suction acting in the chamber 7 over the entire length of the shaft 2, pulls the wave in slurry exists on the surface of the filter sectors 4, finding schihs in one angular position, and the filtrate passes through from Verstov 5 in the chamber 7 and from there through the pipe 14 out from the filtrate ,. As a rule, this first filtrate also contains a fine fibrous matter, since for practical reasons the mesh of the filtering sectors cannot be made so frequent that it retards all solids of the filament to be filtered. In the next stage, when the sector comes under the effect of vacuum in chamber 8, the fiber layer is already laid on the surface of sector 5 and acts as an agent that effectively delays the thin material. As a result, from all filtering sectors connected to chamber 8, a filter is obtained of higher purity, from sectors connected to chamber 7. The filtrate coming from chamber 8 / is removed through pipe 15 and leaves from the filter, and the filtrates from each nozzle 14 and 15 are separately processed in further steps. The vacuum in sector 4 disappears after lifting the sector above the surface of the bath’s liquid, since the chamber 9 is now at atmospheric pressure, because the fiber layer on the sector opposite to chamber 9 is removed by jets of water located between the filter discs (not shown, which are layers into the receivers between the disks. The water jets also wash the mesh surfaces of the sectors before re-immersion in the bath 1, after which the described operation is repeated. Formula 1. Disc filter for cleaning liquids containing bath, hollow shaft with filter discs made of sectors communicating with the shaft cavity, filtrate drainage pipes and a vacuum source, due to the fact that, in order to increase cleaning efficiency, the filter is equipped with a ribbed liner with end walls fixedly mounted inside the shaft separating the internal cavity of the shaft into the filtrate drain chambers, each of which is connected to the filtrate drain nozzle and a regeneration chamber connected to a vacuum source. [2] 2. The filter according to claim 1, characterized in that it is provided with a bracket on which the ribbed liner is fixed. Sources of information taken into account during the examination 1. USSR Author's Certificate No. 448875, cl. B 01 O 33/26, 05.11.74.
类似技术:
公开号 | 公开日 | 专利标题 SU847898A3|1981-07-15|Lisc filter US4136028A|1979-01-23|Method for filtering a fibrous material by means of a disc filter as well as a disc filter for performing the method JP3103593B2|2000-10-30|Liquid filtration device US5759397A|1998-06-02|Filter with spray cake removal means FI94839B|1995-07-31|Device for filtration of sludge and method of use of the devices FI93800B|1995-02-28|Device and process for treatment of pulp US2022069A|1935-11-26|Filter JP2782477B2|1998-07-30|Press for slurry processing US3000507A|1961-09-19|Rotary filter US4370231A|1983-01-25|Rotary drum filter US4138338A|1979-02-06|Filter for thickening suspensions of fibrous material US2581210A|1952-01-01|Positive pressure machine for forming continuous strips of asbestoscement compositions and the like US3306460A|1967-02-28|Wire wound filter with underlying peripherally spaced cover elements US3375932A|1968-04-02|Continuous filtration device of the pressure type CA2164146C|2007-07-03|Rotary filter with a device for separating a solids/liquid mixture, particularly a pulp suspension FI86261C|1992-08-10|SKIVFOERTJOCKARE. US4539827A|1985-09-10|Belt washing improvements US2070074A|1937-02-09|Apparatus for discharging filters US5073264A|1991-12-17|Apparatus for treating fiber suspension US3254772A|1966-06-07|Filter US8281936B2|2012-10-09|Vacuum washer drum having a center and end drains and method for draining US5192454A|1993-03-09|Method for treating fiber suspension SU1139783A1|1985-02-15|Apparatus for washing fibrous suspension JP2701198B2|1998-01-21|Filter media blockage prevention device for vacuum dehydrator of hydrate US3066731A|1962-12-04|Papermaking machine
同族专利:
公开号 | 公开日 SE7707651L|1978-01-03| FI55446B|1979-04-30| NO144948C|1981-12-16| SE419944B|1981-09-07| CA1090711A|1980-12-02| FI55446C|1979-08-10| FI761930A|1978-01-03| US4123363A|1978-10-31| BR7704313A|1978-04-04| JPS6034409B2|1985-08-08| NO144948B|1981-09-07| DE2729022A1|1978-01-12| NO772284L|1978-01-03| JPS5334177A|1978-03-30|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US2027652A|1935-04-25|1936-01-14|Municipal Sanitary Service Cor|Filter| US3471026A|1966-12-09|1969-10-07|Dorr Oliver Inc|Continuous rotary disc filters| US3452874A|1967-11-02|1969-07-01|Dorr Oliver Inc|Trunnion valve for continuous rotary filters|FR2535214B1|1982-10-28|1987-06-12|Hospal Ind|SPACER FOR MEMBRANE APPARATUS| ES2031191T3|1987-09-16|1992-12-01|Andreas Kufferath Kg|DISC THICKENER.| SE9000571L|1990-02-16|1991-08-17|Frykhult R Ingf Ab|ROOTABLE FILTER, WIRELESS STEP FOR DRAINING FIBER PASS PENSIONS| US5296152A|1990-02-16|1994-03-22|Ingenjorsfirman R. Frykhult Ab|Apparatus for filtering suspensions and a method of operating the apparatus| EP0515502B1|1990-02-16|1995-06-07|Beloit Technologies, Inc.|Apparatus for filtering liquids| ES2065010T3|1990-02-16|1995-02-01|Nordic Water Prod Ab|APPARATUS FOR FILTERING LIQUIDS.| SE501550C2|1992-11-20|1995-03-13|Kvaerner Pulp Equipment As|Suction head disposed between a filtrate channel and a drop tube at a rotating filter| FI91938C|1993-02-09|1994-09-12|Ahlstroem Oy|Device for treating pulp| FI20041518A|2004-11-25|2006-05-26|Andritz Oy|Method and apparatus for treating mesa| US11000791B2|2019-03-06|2021-05-11|Veolia Water Solutions & Technologies Support|Rotary disc filter having backwash guides| IT201900011058A1|2019-07-05|2021-01-05|Carmine Elia|THICKENER FILTERING MACHINE|
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申请号 | 申请日 | 专利标题 FI761930A|FI55446C|1976-07-02|1976-07-02|SKIVFILTER| 相关专利
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