WO2012016846A2 - Schmutzabscheider für hochviskose medien - Google Patents

Schmutzabscheider für hochviskose medien Download PDF

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Publication number
WO2012016846A2
WO2012016846A2 PCT/EP2011/062561 EP2011062561W WO2012016846A2 WO 2012016846 A2 WO2012016846 A2 WO 2012016846A2 EP 2011062561 W EP2011062561 W EP 2011062561W WO 2012016846 A2 WO2012016846 A2 WO 2012016846A2
Authority
WO
WIPO (PCT)
Prior art keywords
channel
screen
dirt separator
sieve
channels
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/EP2011/062561
Other languages
German (de)
English (en)
French (fr)
Other versions
WO2012016846A3 (de
Inventor
Robert Middler
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CRAMER ISABEL
Original Assignee
CRAMER ISABEL
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CRAMER ISABEL filed Critical CRAMER ISABEL
Priority to EP11741546.3A priority Critical patent/EP2601036B1/de
Priority to US13/813,820 priority patent/US9539753B2/en
Priority to CN201180038327.2A priority patent/CN103097106B/zh
Priority to JP2013522191A priority patent/JP6040152B2/ja
Priority to BR112013002547A priority patent/BR112013002547A2/pt
Publication of WO2012016846A2 publication Critical patent/WO2012016846A2/de
Publication of WO2012016846A3 publication Critical patent/WO2012016846A3/de
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/69Filters or screens for the moulding material
    • B29C48/691Arrangements for replacing filters, e.g. with two parallel filters for alternate use
    • B29C48/6914Arrangements for replacing filters, e.g. with two parallel filters for alternate use the filters being fitted on a rotatable or pivotable disc or on the circumference of a rotatable or pivotable cylinder
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/254Sealing means
    • B29C48/2545Sealing means for filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/255Flow control means, e.g. valves
    • B29C48/2554Flow control means, e.g. valves provided in or in the proximity of filter devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/27Cleaning; Purging; Avoiding contamination
    • B29C48/2725Cleaning; Purging; Avoiding contamination of filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/27Cleaning; Purging; Avoiding contamination
    • B29C48/2725Cleaning; Purging; Avoiding contamination of filters
    • B29C48/273Cleaning; Purging; Avoiding contamination of filters using back flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/69Filters or screens for the moulding material
    • B29C48/691Arrangements for replacing filters, e.g. with two parallel filters for alternate use
    • B29C48/6914Arrangements for replacing filters, e.g. with two parallel filters for alternate use the filters being fitted on a rotatable or pivotable disc or on the circumference of a rotatable or pivotable cylinder
    • B29C48/6916Continuously rotating cylindrical filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/69Filters or screens for the moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling

Definitions

  • the invention relates to a dirt separator for highly viscous media, having the features of the preamble of claim 1.
  • the housing elements is provided per ⁇ wells an inflow and a flow channel, said inflow and a flow channel located behind each other, in particular in alignment, and forming in succession with in each case one of the apertures in the rotary filtration system a continuous flow channel. If the current flow through the sieve is too dirty, the sieve wheel will turn an angle turned so that the next following sieve is pivoted into the flow channel. As the screen wheel rotates, whether stepwise or continuously, the soiled screen is placed in the area of a screen change port in the housing where the screen is freely accessible. There, the sieve can be removed and replaced.
  • the dirt separator described in EP 379 966 A2 also discloses a backwashing function in order to be able to detach deposits from the dirty side of the sieve and thus to be able to clean the sieve without complete removal from the sieve opening.
  • the melt is diverted from the flow channel at the back of the housing and returned from the clean ⁇ sieve side through the screen.
  • Adhesive particles adhering to the screen element can thus be released by the dynamic pressure applied from the rear and flushed out of the housing.
  • the projectisseff ⁇ tion which establishes the connection to the outside of the housing, can be closed with a movable slide.
  • a disadvantage of the known generic dirt separator is that in each case only a few Siebstellen in function and are within a continuous F grease ⁇ nals, while distributed over the screen at ⁇ their Siebstellen, which are still filled with the medium, remain idle, whereby the throughput is limited to the flow channel cross section of the currently in production screen position.
  • screening elements are provided which are significantly larger than the opening cross-section of the inlet and outlet channels, so that funnel-like transitions must be provided.
  • the fluid flow in the outer regions of a flow channel has to travel longer distances than in the center. The result is an inhomogeneous fluid retention time spectrum in the area of the screen.
  • the object of the present invention is to increase the throughput in the case of a dirt separator with a screen wheel of the type mentioned at the outset and, in particular, to increase the flow rate. reduce material decomposition at the not in production position Siebstellen.
  • sieve position is used for those places where in the housing inlet and outlet (part) channels are in alignment one behind the other and there is a sieve opening in the screen between them.
  • inlet channel, the outlet channel and the sieve opening are "in line" in at least one working position, does not necessarily require elongate geometric bodies with exactly aligned central axes, but merely means that in one working position the clear cross sections of the mouths of and flow passages and the screen opening at least partially overlap, so that a flow is enabled.
  • annular zone refers to a pro in the direction of flow ⁇ ji formede annular surface on the rotary filtration and the adjacent FLAE ⁇ surfaces of the housing elements.
  • the sieve ⁇ openings as well as the openings of the inlet and outlet ducts are arranged.
  • the screen openings can within the annular zone on a common be arranged in a uniform pitch circle, but also on a plurality of pitch circles spaced apart from each other of a revolver, only a few or a few sieve positions - ie a maximum of 35 - 40% of the screen positions available on the sieve wheel - are driven into the flow channel and out of this when they are dirty, the invention consciously goes the other way and gives the majority The Siebstellen in the production operation, with less than half of the Siebstellen, especially so ⁇ even only a quarter or even less, are not in production and can be cleaned or replaced nen ⁇ nen.
  • the screen openings may be designed so that they largely fit into the cross-section of the inlet and outlet, resulting in more favorable flow conditions than in known genus ⁇ proper sieve devices, which are provided on the screen openings sometimes considerable widening to ei ⁇ ne To be able to provide larger filter area.
  • the particular effect of the design principle according to the invention is that self-leveling of the flow paths occurs with highly viscous media.
  • the change in the position of the sieve positions with respect to inlet and outlet channels due to the rotation of the sieve wheel can also contribute to setting similar flow conditions at all sieve openings over a longer production period.
  • the inlet channel and / or the Drainage channel centrally, so in the region of the central axis of the sieve, be arranged, but also decentralized, so outside the range of the central axis of the sieve wheel.
  • the central arrangement of complex design provided a storage of Siebrads in the housing is provided over a Oh ⁇ se or shaft in the center, because then the storage has to be bypassed by the flow paths.
  • the central arrangement enables a Auftei ⁇ development of supply and / or discharge channel into individual sub-channels that are geometrically similar.
  • similar flow conditions due to the self-leveling effects do not set in with increasing production time, but already at the beginning of production.
  • a decentralized arrangement of inlet and outlet channel he ⁇ facilitates the arrangement of a central axis or shaft for supporting the sieve wheel.
  • inlet part channels and / or the outlet part channels have similar flow resistances by appropriate adaptation of channel lengths and channel cross sections.
  • a branching of the inlet channel and the outlet channel takes place in a plurality of inflow or Drain section channels.
  • the fluid flow is distributed on the front housing element in the flow direction to a plurality of sieve locations and united on the back of the housing as ⁇ .
  • angle positions of Sieb ⁇ rads constantly up to 90% of the screen openings in registration with the inlet or outlet channels and can be flowed through. Only at least one screen position is not powered in the produc ⁇ tion operation, so that there, at a provided in the housing screen changing position, the screen element can be removed and the breakthrough in the screen can be cleaned in total.
  • the branch of the inlet conduit can be effected in several star-shaped ducts Zulaufteilka-, so that in each case from a central inlet channel an inlet part of channel leads radially outwards ⁇ sizes up to the respective screen cavity.
  • a distribution channel is provided, which is arranged in the annular zone or which passes through the annular zone and which is connected to a plurality of Siebpositionen and which can feed several Siebstellen simultaneously.
  • This distribution channel is fed or discharged, for example, from one or both of its ends the middle out. From screen to screen, al ⁇ lead sub-channels, which line up in a chain.
  • a ⁇ to running and a flow channel leading in the housing part in each case at least to a subset of mög ⁇ union Siebpositionen and that at a number
  • n 12 and the openings of the drain and Zulaufteilkanäle and the screen positions are arranged on the screen as the numbers of a clock on a common pitch circle.
  • This distribution of sieve positions in 12 x 30 ° steps is easy to manufacture and uses the available space in an annular area on a sieve wheel with a manageable diameter of 400mm to 2000 mm, with a diameter of the sieve positions of 100 mm to to 200mm, optimal.
  • the inlet and / or the flow channels widen part preferably on the side facing the rotary filtration surface of the housing elements in a funnel shape, so that the eigentli ⁇ chen flow channels remain lean and only their openings are so large that the trained with larger cross-section sieve openings in the sieve wheel can be completely flowed through.
  • a particularly advantageous embodiment provides that the respective next but one positions on both sides of the screen changing position are elongated, in particular slot-shaped, at least in the rear housing element. This ensures that the sieve can be flowed through longer than at the other positions and that until they almost have the screen change point he ⁇ reaches. Only shortly before the melt flow stalls then, with but can the clean side also reduce the pressure in the screen cavity so that a melt of ⁇ occurs is avoided at the Siebroarö réelle.
  • Extended in the sense of the present invention refers to any elongated contours that extend beyond a circular shape and thus extend further along the annular zone, including oblong shapes in the conventional sense as well as ellipses or asymmetrical shapes.
  • a branch channel can also connect laterally to the opening cross section of the drain part channel.
  • an elongated hole is preferably also provided, so that the screen cavity be ⁇ can at the next to the Sieb grillposition following passage already returned from the clean side ago with melt aufschlagt when just the sieve ⁇ change position has left.
  • at least one of the Siebpositionen is formed as a breather ⁇ processing position, wherein in the rear housing member performs at least a flow sub-channel to the clean side of the vent position, and wherein from the Dirt side of the venting position from a breather ⁇ tion opening extends to the outside of the housing.
  • At least one of the sieve positions is designed as a backwashing sieve position, wherein in the rear housing part at least one discharge subchannel to the clean side of the rear - Rinsing screen position leads and wherein extending from the dirty side of Ruth Cyprussiebposition from a backwash opening to the outside of the housing.
  • venting position and the backwash position can be made similar.
  • a flooding of an empty sieve opening and a vent can be effected from both the dirt and the clean sieve side.
  • Only a ventilation duct to be provided for the escape of the air must be arranged so that it preferably adjoins the top of the sieve opening.
  • the screen change point can be arranged, for example, at the 3 o'clock position.
  • the 2 o'clock position as a blocking position and the 4 o'clock position as a venting position tion then remain in the respective housing elements free of melt channels, so that the respective Siebstellen in the sieve there are not flown. This will si ⁇ cherric that no melt from the neighborhood reaches the Siebcicö réelle, even if the screen cavities are arranged closely alongside each other.
  • At least one inlet and one outlet part channel leads to a number of at most n-3 screen positions of n possible positions, which result with uniform distribution on a pitch circle.
  • At an m-th wire position is a Sieb Lobö réelle in at least one of the housing elements vorgese ⁇ hen, where m ⁇ n.
  • each slot-shaped drain part ⁇ channels are provided.
  • rollers may be provided, wherein the roller assembly surrounds the outer periphery of the screen wheel.
  • a central shaft on the sieve wheel which is rotatably mounted in a hub in the housing.
  • a circular recess in the center of the screen wheel vorzuse ⁇ hen and at least one of the housing elements form a corresponding shoulder or pin on which the screen is then stored in a bearing recess in the housing.
  • FIG. 1 shows a dirt separator according to a first embodiment in front view
  • FIG. 2a - 2d a dirt trap in a schematic
  • Fig. 3 shows a front housing element in a schematic
  • Fig. 4 shows an alternative embodiment form of a front
  • FIG. 6 is a partial development of a flow channel in the embodiment form according to the figures 4 and 5.
  • FIG. 1 shows a complete dirt separator 100 with a view from the front, seen in the direction of flow, of a housing comprising a front housing element 30 and a rear housing element 20.
  • the Gerissausele ⁇ elements 20, 30 are spaced from each other and between them include a rotatable sieve wheel 10 with a plurality of sieve points 11.1 ... 11.12.
  • a drive unit 40 which in this case comprises a pneumatic cylinder which is pivotally mounted and which has at its end a driver element 41 which engages teeth 10 formed in the 42 at Rajum ⁇ fang of Siebrades. Due to the weight of the drive unit 40, the driver element 41 always rests on the toothing 42. With a slight feed movement, it gets over the edge of the next tooth and sagging behind it, so that it in the next retraction movement of the driver element, the screen wheel 10 by a certain angle in Twisted clockwise direction.
  • This design of the drive which is known per se, represents a particularly simple and effective implementation of a Shaschaltbe ⁇ drive.
  • a shutter 50 is arranged with a Sieb cartiklappe 51 in the region of Sieb cappe which relative to the housing can be locked via a Hebelele ⁇ element 52 and which will be explained in more detail below.
  • shutoff unit 60 is arranged, with which an outlet opening of a backwash ⁇ and the vent passage 35 (see FIG.. 2a-2d) is closable.
  • Fig. 2a shows a view of the dirt separator 100 with removed front housing member, thus facing directly to the rotary screen 10 and the underlying back ⁇ tere housing element 20.
  • the screen 10 has twelve screen points 11.1 ... 11.12, which are arranged like the numbers on a dial.
  • the sieve stations 11.1... 11.12 are in this example designed as circular openings in the disk-shaped sieve wheel 10, which are each provided with wire mesh-shaped sieve elements.
  • a discharge part channel 21.1... 21.12 leads from each screen 11.1... 11.12 in the shape of a spoke to a central outflow channel 23 in the housing 20.
  • the screen position 11.1 lies in Fig. 2a with the left part of the mouth 22.1 in coverage.
  • the part to the right is partly open, but overlaps a bit with the next screen 11.2 at the 2 o'clock position. If, at the 2 o'clock position, the melt is now conducted through the sieve 11. 2 at the front housing element (not illustrated), then it can flow away via the mouth 22. 1 of the drain part channel 21. 1; The same applies to the other sieve stations 11.2 ... 11.12 and partial drain channels 21.2 ... 21.12.
  • the dot-dash line at 34 ° indicated at 34 indicates a screen change port 34 present in the housing front 30.
  • the screen 11.3 lies exactly at the 3 o'clock position and thus within the screen change port 34 ,
  • the turn next next screen 11.4 is in the position of the screen wheel 10 according to Figure 2a on the Reinsieb ⁇ page in partial overlap with the elongated hole-shaped mouth of the drain part channel 22.5 and
  • a backwash and vent channel 35 which on the dirty side, ie in the front hous ⁇ seelement 30, is arranged and which leads to the outside of the housing.
  • the medium such as art ⁇ material melt, can over the overlapping area of the screen cavity 11.4 with the opening 22.5 of the flow channel part 21.5 to flow through the screen 11.4 on the clean side and can flow from there via the channel 35 to the outside of the housing, which can be washed away on the dirty side before ⁇ present deposits.
  • Fig. 2b shows a position of the screen wheel 10, which is changed by we ⁇ nige degrees with respect to the position shown in FIG. 2a.
  • the screen 11.3 has now emerged from the Sieb ⁇ exchange opening 34 and is already connected to the backwash and vent 35 in connection.
  • the sieve 11.4 is located in the region of the slot-shaped mouth 22.5 and is there again traversed.
  • the screen 11.3 is advised in overlap with the extension 32.1.
  • the screen 11.3 can now also be flooded on the dirty side of the screen with melt;
  • the rear area on the clean side of the screen has already been flooded by the previous backwashing process.
  • Still in the sieve 11.3 remaining air can escape via the channel 35.
  • Fig. 3 shows a view in the direction of flow on the front housing part with its central inlet channel 33, the branches in a plurality of Zulaufteilkanälen 31.1 ... 31.12 star-shaped.
  • the star-shaped inlet sub-channels 31.1 ... 31.12 again combine on an arcuate distribution channel 32. This extends starting at a position between 2 o'clock and 3 o'clock over an arc of almost 270 ° counterclockwise to an end position between "4 o'clock" and "5 o'clock".
  • the end of the arcuate distribution channel 35 in the region of Zulaufteilkanals 31.5 no longer runs on the pitch circle, but goes with a greater curvature than extension 32.1 in the direction of the center.
  • This particular end-side design of the distribution channel 32 has the purpose, in a close arrangement with as many sieve positions on the sieve 10, so with little distance from each other, yet a separation between the functions "backwash” according to Figure 2c and “venting” according to Figure 2a and 2d, and thus occupy only one possible Siebposition on the pitch circle for both functions together.
  • FIGS. 4 to 6 show another embodiment of a dirt separator 100 ', in which, for reasons of drawing, only eight sieve sections 11. 1' are shown.
  • Figure 4 shows in a schematic perspective view of a front housing member 30 'which consists of ferti ⁇ supply technical reasons of two sub-plates 36' is formed, 37 '.
  • Right in Figure 4 is the outer housing ⁇ surface with a central inlet channel 33.
  • On the left is the rear housing face to which the inlet channels open part and to which the rotary screen 10 'is applied.
  • the through ⁇ flow direction in Figure 4 therefore is from right to left.
  • an arcuate distribution channel 38 ' is provided, which extends from an angular position at 45 ° over an arc of about 270 ° to an angular position at 315 °.
  • the distribution channel 38 ' has directly on the rear housing surface no openings, so that there is a continuous, arcuate distribution channel, which can supply all the front of the sieve screen uniformly.
  • the webs 38.2 are used to wrap the material regions within the bogenför ⁇ -shaped distributor channel 38 'bear against the outer material areas and to achieve a high total Steifig ⁇ ness of the housing.
  • a further arcuate distribution channel 39 ' is provided which extends only over about 180 ° and whose radius is significantly smaller than the radius of Verteilerka ⁇ Nals 38'.
  • the webs 38.2 ', 39.2' also serve as a flow divider within the open flow passage portions 38.1 ', 39.1', as shown by the provision of a F forcedka ⁇ Nals shown in Fig. 7.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Lubrication Details And Ventilation Of Internal Combustion Engines (AREA)
  • Centrifugal Separators (AREA)
  • Electrostatic Separation (AREA)
PCT/EP2011/062561 2010-08-03 2011-07-21 Schmutzabscheider für hochviskose medien Ceased WO2012016846A2 (de)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP11741546.3A EP2601036B1 (de) 2010-08-03 2011-07-21 Schmutzabscheider für hochviskose medien
US13/813,820 US9539753B2 (en) 2010-08-03 2011-07-21 Dirt precipitator for a highly viscous medium
CN201180038327.2A CN103097106B (zh) 2010-08-03 2011-07-21 用于高粘度介质的污物分离器
JP2013522191A JP6040152B2 (ja) 2010-08-03 2011-07-21 高粘度の媒体用の異物分離器
BR112013002547A BR112013002547A2 (pt) 2010-08-03 2011-07-21 separador de impurezas para meios altamente viscosos

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102010036810.5A DE102010036810B4 (de) 2010-08-03 2010-08-03 Schmutzabscheider für hochviskose Medien
DE102010036810.5 2010-08-03

Publications (2)

Publication Number Publication Date
WO2012016846A2 true WO2012016846A2 (de) 2012-02-09
WO2012016846A3 WO2012016846A3 (de) 2012-09-13

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2011/062561 Ceased WO2012016846A2 (de) 2010-08-03 2011-07-21 Schmutzabscheider für hochviskose medien

Country Status (7)

Country Link
US (1) US9539753B2 (enExample)
EP (1) EP2601036B1 (enExample)
JP (1) JP6040152B2 (enExample)
CN (1) CN103097106B (enExample)
BR (1) BR112013002547A2 (enExample)
DE (1) DE102010036810B4 (enExample)
WO (1) WO2012016846A2 (enExample)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013208637A1 (de) * 2013-05-10 2014-11-13 Gneuss Gmbh Verfahren und Vorrichtung zum Betreiben eines Siebradfilters
DE102013208628A1 (de) * 2013-05-10 2014-11-13 Gneuss Gmbh Verfahren zum Betreiben eines Siebradfilters und Siebradfilter zur Durchführung des Verfahrens
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US9539753B2 (en) 2017-01-10
US20140001111A1 (en) 2014-01-02
BR112013002547A2 (pt) 2016-05-31
WO2012016846A3 (de) 2012-09-13
EP2601036B1 (de) 2016-01-06
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DE102010036810B4 (de) 2018-05-30
DE102010036810A1 (de) 2012-02-09

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