Filtering apparatus for separating solid and suspended substances from liquid
专利摘要:
1. A filtering apparatus for separating solids and suspended particles from liquids, comprising a cylindrical casing (1), a cylindrical filter basket (3) coaxially installed therein and delimiting a space accommodating the liquid to be filtered relative to an outer annular space (II) accommodating the filtrate, and a backflush means axially movable by a drive (13) and provided with two piston disks (11) arranged at a constant distance and including channels connecting the outer annular space (II), via perforations (27) of the filter basket (3), with an inner space (III) of a central tube (7) provided coaxially relative to the filter basket (3), the piston disks (11) abutting on the inner surface of the filter basket (3) via seals, characterised in that - the central tube (7) is fixedly arranged in the cylindrical casing (1) so that the space accommodating the liquid to be filtered forms an annular space (I), - the piston disks (11), via seals, abut on the outer surface of the central tube (7) in a liquid-tight manner, and are supported for an axial guidance, and - the drive (13) directly engages in at least one of the piston disks (11). 公开号:SU1085497A3 申请号:SU823390758 申请日:1982-02-15 公开日:1984-04-07 发明作者:Кляйн Вальтер 申请人:Хемифазер Ленцинг (Фирма); IPC主号:
专利说明:
The invention relates to a ui-uvr vaping unit for a site) (en1 -:;. The space of the weighed sestet or bones and may be MSPOL-ANNUAL, in particular, to filter it to remove hard gel particles and so on-; osgg A filtering device is known in which the floor connects raj is connected on one side, at least with a piston MP; and on the other hand, with a shaft, a goal is located inside the centerpiece with a hole. Around deEgr and b. pipe5 is located large. 4VTc. ;; c of the driving elements. However, for the crossbar. telnoy shtangr necessary. advanced; geo-iosidionic device GEO ,, additionally, the lack of installation ;;; - - la ffltrOschg i-p surface: chytochk production-; her g d x „ Well known is: oka filter; : schA i NOBKa.) In which the filter C; OSTOI two coaxially dispersed g-erfs vannyk cylinders, g; evlu K00prjj meschega 1shchlindrietska prp: ol;: 1 -;: grid ,, Setanopky-oogashhen device -; 2 j, However nerfsch agdey obsi;: h vn..rv must precisely with) ENADA1L; between /, her and drilling holes CZ for 1O; Shimr: -: Lack of installation / a ::; however, significant costs are incurred; b: rJiY bones due to leakage into the gap between the hologram;, ;;: the device and the wall Kopi yca: The closest m Msoope vc ;; according to the technical essence, according to the result, f | -; lt :; valka installation containing with located coaxially znu: sn filter element with pzpfor ;; expanding from within trawl pipe and connection an; Disc element with CKBOSH channel set mezvdu c Rialnaya pipe and filtrushgnym e cop with the possibility ssavogg Relative to the latter The disadvantage of the known installation is a significant loss of a non-filthy suspension The purpose of the invented - ukek1-: neno amount of fluid for reverse flushing and increasing the number of; -os-tg: h); - l). ;; what is the depletion of ;; x: o / L vrHOTi - ;;: - i-1 -,: h i-eiKriy fk.g; tryu K: ;; e; -, ichi e / iHbj .: zlekeitamk. aBjicHriaH the tel is reached by a U installation containing a rnus with a spaced coaxially inside the wi-iJibTpyionsiK wedge element with a perforated ring; and-, v) ac pp; pkyush; f -; c - inside ipy j;: - ,. ::: er tr, lt.uo pipe and connect the tetyv 1T; er-: gl n as a disk with nllll-; ::.: -.а on, С usganovteknyy; l / U n, nral};.; -. ::, th .1,; / battle and filterHOCJH ::: :: la; e; 1 f.i, nozmezhkostiga EU: o tteleg-lHk; :: relatively n: nel: ll: -:. :. vlHTejT ny element n :::: en .--; - nt. diene with n. o;:.. ny.) :: ghana, mrs.- ,. - located . / ,.: n;: ji / Hn l, Ltru103 ;; o dis; onornoy: ruoyoy "placed l; HV:;. ;, lo1; o ;; delicate -;.;:,. V: e, ..:; :) ira; sa central ijyiiy nrn;:; -o / - .: nornus is fulfilled, dr1: - eu / gsn- :. mr; Gs-Lentenoye Nabrylp, 1,: hedgehog; -:;, e; l;: rap :: oh to the reference W.L. and SEDIN -; : with CROSS Ml ll: r.ub; ,; supply disks :. :: /. s - ;; H; A v Л Л сг: НС нкнлл and нригоноч-Р-И Ч- ;;; wasps; J; ; -: -; l, |; -: amétroEnerHI H: Not n .- :: Luck Oioh. t: / 1n; ll-nol1s o. n ;; ement sos: v: ri; :: l. 25 ;;; Essential Q-n: from the third spacing - from the distance; from L; :) Hi -; - 4 ieTpa non-perforation on the / -th: - -th filtering machine : -o; -; with L;., 1AHL.N. on the walls of the filter C: kO-. zl :: tapes;.; ra; n-; a 2,5 diameter: p :: i :); lower to the ugly side .-s; -ola, GlNn (:; sd-larnalOll rameagen--; l -,; 1rul ;; oh ln; 1 ;;. :) hnost of fkltn,: i (::: ii-1p 2dsta1 ;: lena fn / 1tron ..-: l. -y-g:;: n f1, yr. /; on, 4 - scheu: 7 parasni fi; tirovalnoy fatigable ll in fig. L-srgliruyu ale:. lnn, zid on the s / a: - blind1; a l; lpot: burner g (erfora-; i;: a shchgt v-ioi :;; -; - non-compliant; figure 7 is another variant of the filter element Fig. 8 is a general view of the section; Fig. 9 shows a section B-B in Fig. 8. The installation consists of a cylindrical body 1 with clamps 2. Inside the case there is a filter element with perforations 3, on the outside side to The filter material 4 is expensively installed by a clamping means 5. On the inner side of the collar 2, T1 directing members 6 are provided for centering and sealing the filter element having reinforcing rings 7 and 8. The coaxially arranged central pipe 9 is designed to drain the liquid during backwash through the valve 10 and holes 11. The partition 12 serves to shorten the drainage path of the liquid. The installation has a connecting element consisting of two disks 13 and 14. The disks are set apart from each other by means of a support pipe 15 surrounding the central pipe 9. The connecting element can occupy two positions, abutting one of the crust 2 of the housing 1 ( the right position is indicated in FIG. 1 by the dashed line). For the drive of the connecting element, an eccentrically located lead screw 16 is provided, the screw installed in support 17.X, the screw 16 has a threaded connection with the disk 14, and the sealing of the screws in the cracker is carried out by means of a stuffing box 18. The driving screw 16 is connected to the actuator 19 by means of couplings 20. Limit switches 21 are wired (not shown) connected to the actuator 19. On one and covers 2 of case 1 there is a nozzle 22 for feeding the filtered liquid. On the cylindrical case 1, a regulating or drain valve is installed. apan 23 and valve 24 precipitate. The installation works as follows. The liquid to be filtered is fed through the nozzle 22 into the annular space between the central tube 9 and the perforated filter element 3. Liquid through the perforations 3 of the filter element enters the filter material 4. The solids are retained by the filter material 4, and the cleaned liquid enters the annular space between the filter element, and the housing 1, from where it is discharged through a regulating or drain valve 23. As the discs are spaced from each other at a distance equal to 1/2 of the length of the filter element, t In either of the two positions, one of them is in the middle part of the filter element that does not have perforations. In the filtering process, the filter material 4 is gradually clogged with particles of solid contaminants, as a result of which the hydrodynamic resistance increases and a pressure difference is created. Upon reaching a certain pressure difference between the annular space. above and below the futton element, the backwash process begins. At the same time, using the actuator 19, the friction m: -phth 20 and the lead screw 16 soy), the transfer element is moved from one position to another with a predetermined constant speed along the inner surface of the filter element. During the movement of the connecting member, the filtering process continues and only two narrow sections in the form of a ring corresponding to the thickness of the discs are closed for filtering. Since the pressure in the annular space above the filter element is higher than that in the through channel of the discs, a small part of the already filtered liquid is pushed out of this space into the through channel, and the filter material is freed from solid particles settled on it. The dilution fluid passes through the annular space between the central tube 9 and the support tube 15 and the orifices 11 into the inner space of the central tube 9 and is discharged from there through the valve 10. Depending on the solids content in the filtered fluid, the pressure difference is reached at various time intervals. The filter unit control system (Fig. 4) contains two devices 25 and 26 for receiving data. measured pressure and differential pressure switch 27. When a certain pressure difference is reached, depending on the conditions of the process, the actuator switch 28 is actuated, and the actuator 19 moves the connecting element from one position to another. After reaching the new position with the connecting element, the limit switch 21 turns off the switch 28. The pressure is increased with the help of the pump. 29 in the supply line for the filtered liquid The perforations of the filler element can be made, according to a preferred form, in the form of tapered bores 30, in which the ratio of the diameter of the holes on the inner and outer sides of the filter element is equal to 2.5 times the axis of the bores. the diameter of the holes on the inside of the filter element. The drillings are located offset from each other so that the holes on the outside of the filter element are as close as possible to each other and their depth is around 70% of the total surface area of the filter element. The wall thickness of the filter element is 2j5 perforation diameter on the inside of the filter element. Conical drillings 30 can be made with a short cylindrical part (mainly on the inner side of the filter element), the cylindrical part having a length equal to 0-1 of the thickness of the filter element. The disks of the connecting element (Fig. 8) have internal external and internal fixing parts 31 to 32, secured with a bolt 33 and an annular intermediate part. 34, B of the annular space formed between them, a ring 35 is installed with a gap 36. The ije piston ring is clamped with locking parts and has grooves in the joint gap area into which a super-shaped fitting 37, is inserted. To prestress the piston ring with, uncoupling the spring 38, the action of which is indicated by arrows in FIG. 9. As soon as the piston rings begin to move from one position E to the other and are in the zone of the filter element with conical bore holes 30, the differential pressure between the annular spaces below and above the filter element as a result of which the piston the rings begin to create a uniform sealing yci. thereby preventing fluid leakage. Also, the fittings 37 are pressed under the action of a pressure difference to the inner surface of the filter element and provide a seal in the area of the butt clearance 36 of the piston rings. Since there is a pressure difference between the annular space under the filter e, filter, and channels inside the discs communicated through the space between the central tube 9 and the supporting tube 15 with the inner space of the central tube S, the piston rings 35 and fittings 37 are also attached to the inner locking parts 31 and compacted installation. Due to the presence of these elements, the amount of liquid required for the backing is reduced and the effective filter is also increased;)) due to the provision of the fluid seal between the coupling elements: o: cc vi. Vida yy 2 5-5 YU 2.25d 32 J i 27 27 FIG. B FIG. 7 (Pas. 9
权利要求:
Claims (5) [1] 1. FILTER INSTALLATION FOR SEPARATION OF SOLID AND WEIGHTED SUBSTANCES FROM LIQUID, comprising a housing with a filter element arranged coaxially inside it with perforations expanding from the inside outward, a central pipe and a connecting element in the form of a disk with a through channel mounted between the central pipe and the filtering element with the possibility axial displacement relative to the latter, characterized in that, in order to reduce the amount of liquid for backwashing and improve filtration efficiency due to For reliable sealing between the filter and connecting elements, the latter is equipped with an additional disk with a through channel located at a distance from the main disk equal to 1/2 the length of the filter element, and a support pipe placed between the main and additional disks and coaxially surrounding the central pipe, this case is made cylindrical, - the annular space between the central and supporting pipes is connected to the through channels of the disks and the inner space of the central pipe, and the disks are equipped with ltsevymi seals and shims segments with springs. [2] 2. The installation according to claim 1, wherein the ratio of perforation diameters on the outer and inner sides of the filter element is 1: 2.25, and the perforation axes are placed one from another at a distance equal to 2.5 perforation diameters on the inner side of the filter element. [3] 3. The installation according to claim 1, characterized in that the thol (qing of the walls of the filter element is equal to. 2.5 diameters of perforations on the inside of the filter element. [4] 4. Installation according to claim 1, characterized in that it is equipped with filter material placed on the outer surface of the filter element. [5] 5. Installation according to claim 1, characterized in that the connecting element is provided with an eccentrically mounted spindle connected to the drive. SU, .., 1085497 y i n -
类似技术:
公开号 | 公开日 | 专利标题 SU1085497A3|1984-04-07|Filtering apparatus for separating solid and suspended substances from liquid US5164079A|1992-11-17|Filtering apparatus for separating solid and suspended matter from a liquid US5152891A|1992-10-06|Self-cleaning strainer US3380591A|1968-04-30|Fluid filter with automatic cleaning device US3574509A|1971-04-13|Backwash filter US4350590A|1982-09-21|Filtration system US4698156A|1987-10-06|Rotating filter apparatus for separating fine particles of solids from a liquid US7208091B2|2007-04-24|Assembly for withdrawing and filtering partial volumes of process fluid US6090279A|2000-07-18|Access valve devices, their use in separation apparatus, and corresponding methods EP0641292B1|1998-09-09|Water clarifier with first filtrate isolation, improved backwashing and improved bubble generation US4673495A|1987-06-16|Enclosed cyclone separators US4415448A|1983-11-15|Flush-back filter US6461513B1|2002-10-08|Secondary-flow enhanced filtration system EP0429551A1|1991-06-05|Continuous backwashing filter apparatus. US5453194A|1995-09-26|Back-flushing filter device for the filtration of highly viscous liquids US3074560A|1963-01-22|Positive pressure backwash strainer US4339333A|1982-07-13|Filtration device US5080791A|1992-01-14|Apparatus for multisized filter element cartridge insert for paper towel filters US4897192A|1990-01-30|Rotary filtration device US3919087A|1975-11-11|Continuous pressure filtering and/or screening apparatus for the separation of liquids and solids US5833847A|1998-11-10|Apparatus for the filtration of industrial liquids and gases EP1286781B1|2004-10-27|Centrifuge with a sieve system and method for operating the same DE4033012A1|1992-04-23|Dewatering esp. of clarification sludge -by combined centrifugal filtering and pressurised gas filtering SU1097378A1|1984-06-15|Oil cleaning centrifuge DE3311054A1|1984-09-27|DEVICE FOR SEPARATING THE LIQUID PART FROM THE SOLID PART OF A CERAMIC SLICKER
同族专利:
公开号 | 公开日 RO86507A|1985-03-15| IN157782B|1986-06-14| DD201854A5|1983-08-17| EP0058656B1|1984-11-07| FI72049C|1987-04-13| DE3261155D1|1984-12-13| ATA70081A|1982-01-15| AT377709B|1985-04-25| FI820462L|1982-08-17| JPS57153711A|1982-09-22| EP0058656A1|1982-08-25| JPH0440045B2|1992-07-01| FI72049B|1986-12-31| BR8200766A|1982-12-21| RO86507B|1985-03-31|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 RU2553901C2|2010-03-08|2015-06-20|Геа Вестфалиа Зепаратор Груп Гмбх|Self-cleaning filter module|DE1905832U|1964-09-16|1964-12-03|Hermann Finckh G M B H|SECURE FOR PAPER FABRIC SUSPENSIONS.| CH484687A|1969-01-24|1970-01-31|Filtrox Maschb Ag|Filter candle| US3994810A|1975-07-28|1976-11-30|Brunswick Corporation|Onstream backflush filter| IL52332A|1977-06-16|1980-02-29|Hydro Plan Eng Ltd|Self cleaning filtration device|GB8704582D0|1987-02-26|1987-04-01|Dowty Mining Machinery Ltd|Fluid filtering systems| AT392217B|1989-07-18|1991-02-25|Chemiefaser Lenzing Ag|FILTER APPARATUS FOR SEPARATING SOLIDS AND HANGING SUBSTANCES FROM LIQUIDS| IL94630A|1990-06-06|1993-08-18|Filtration Ltd Herzliya And Yt|Self-cleaning filter| US5198111A|1991-01-10|1993-03-30|Delaware Capital Formation, Inc.|Filter with reciprocating cleaner unit| GB2290726B|1994-07-01|1997-10-08|Longwall Roof Supports Ltd|A fluid filtering unit| US5527462A|1994-11-15|1996-06-18|Delaware Capital Formation, Inc.|Filter with axially movable wiper| US5569383A|1994-12-15|1996-10-29|Delaware Capital Formation, Inc.|Filter with axially and rotatably movable wiper| AT11727U1|2010-03-12|2011-04-15|Lenzing Technik Gmbh|METHOD FOR FILTRATION OF FLUIDES AND FILTER APPARATUS FOR CARRYING OUT THE PROCESS| DE102010013507A1|2010-03-31|2011-10-06|Gkn Sinter Metals Holding Gmbh|Filter system, in particular for viscose filtration| CN102072218A|2010-11-15|2011-05-25|昆山市汇新电气机械有限公司|Double-piston portal cylinder| DE102014100415A1|2014-01-15|2015-07-16|Krone Filter Solutions Gmbh|Apparatus and method for filtering a liquid with cleaning device without process interruption| CN104548714B|2015-02-06|2016-03-16|袁帅|A kind of equipment for separating liquid from solid|
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申请号 | 申请日 | 专利标题 AT0070081A|AT377709B|1981-02-16|1981-02-16|FILTER APPARATUS FOR SEPARATING SOLIDS FROM LIQUIDS| 相关专利
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