EP0778790A1 - Dispositif pour retirer des matieres a eliminer d'un liquide qui s'ecoule dans une rigole - Google Patents

Dispositif pour retirer des matieres a eliminer d'un liquide qui s'ecoule dans une rigole

Info

Publication number
EP0778790A1
EP0778790A1 EP96924855A EP96924855A EP0778790A1 EP 0778790 A1 EP0778790 A1 EP 0778790A1 EP 96924855 A EP96924855 A EP 96924855A EP 96924855 A EP96924855 A EP 96924855A EP 0778790 A1 EP0778790 A1 EP 0778790A1
Authority
EP
European Patent Office
Prior art keywords
separated
grate bars
channel
conveyor
clearing
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.)
Withdrawn
Application number
EP96924855A
Other languages
German (de)
English (en)
Inventor
Hans Georg Huber
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of EP0778790A1 publication Critical patent/EP0778790A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • E—FIXED CONSTRUCTIONS
    • E03—WATER SUPPLY; SEWERAGE
    • E03F—SEWERS; CESSPOOLS
    • E03F5/00—Sewerage structures
    • E03F5/14—Devices for separating liquid or solid substances from sewage, e.g. sand or sludge traps, rakes or grates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
    • B01D29/035—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting with curved filtering elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/44—Edge filtering elements, i.e. using contiguous impervious surfaces
    • B01D29/46—Edge filtering elements, i.e. using contiguous impervious surfaces of flat, stacked bodies
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
    • B01D29/52—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in parallel connection
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/62—Regenerating the filter material in the filter
    • B01D29/64—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element
    • B01D29/6469—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers
    • B01D29/6476—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element scrapers with a rotary movement with respect to the filtering element
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/76—Handling the filter cake in the filter for purposes other than for regenerating
    • B01D29/80—Handling the filter cake in the filter for purposes other than for regenerating for drying
    • B01D29/82—Handling the filter cake in the filter for purposes other than for regenerating for drying by compression
    • B01D29/828—Handling the filter cake in the filter for purposes other than for regenerating for drying by compression using screws

Definitions

  • the invention relates to a device for removing material to be separated from liquid flowing in a channel with the features specified in the preamble of claim 1.
  • This device can be used in particular in sewage treatment, but can also be used in other areas, for example in the textile industry, in slaughterhouses, poultry farms, tanneries, etc., in order to get separating material, ie screen and / or screenings, from the respective liquid.
  • a device of the type described above is known from DE 40 06 970 AI.
  • the semicircular grate bars of the separating surface are firmly connected to one another, arranged in a stationary manner and form the separating surface with their inner circumference, since they only extend over the lower circumferential region.
  • the of part of the cylinder jacket not occupied by the grate bars is formed by a cover in the form of a semi-cylindrical sheet metal shell.
  • the front of this cylinder jacket is open and thus forms the inflow opening for the liquid loaded with the material to be separated.
  • the separation area is flowed through from the inside to the outside, so that the material to be separated is deposited on the inner circumference, ie on the concave side of the grate bars.
  • a clearing arm with clearing elements is driven in rotation about the axis of this cylinder jacket.
  • the clearing element engages with the clearing elements in a comb-like manner in the slots between the grate bars from the inside outwards and picks up the material to be separated as it rotates.
  • a conveying device is arranged outside the cylinder jacket of the separating surface and consists of a tubular housing, a shaft and a conveying helix.
  • the conveyor device has a receiving opening for the material to be separated.
  • the tubular housing is closed, with the exception of the receiving opening and the delivery point.
  • a free space is provided between the sheet-metal covers and the beginning of the semicircular grate bars for the material to be separated to pass from the separator into the conveying device.
  • a comb-like scraper is arranged in this transfer area. Reversing the direction of rotation of the clearing arm, the material to be separated is stripped from the clearing elements of the clearing arm, so that the material to be separated then falls into the receiving opening of the conveying device. It is not clear where the water level of the flowing liquid is. Since the inflow to the separating device can only take place via the end face and, on the other hand, as large a part of the separating surface as possible from the semicircular grate bars should be used appropriately, the water level should be at a corresponding height. Then, however, the receiving opening of the conveying device lies at least with a large part of its extent below the water level, so that the material to be separated can only be thrown off into the water by the comb-like scraper.
  • the housing of the conveying device is otherwise designed to be closed, a flow can only develop in the area of the separating surfaces, so that there is a risk that the separating material thrown off by the comb-like scraper will be fed again and again via the liquid flow to the separating surface. This results in a collection of material to be separated in the area of the separation area.
  • the water level is selected to be very much lower, there is the possibility that the receiving opening of the conveying device is capable of receiving the discharged material to be separated, the effective area of the separating surface is correspondingly greatly reduced. In the case of changing water levels, the disadvantages described arise to a corresponding extent.
  • Another disadvantage of this known device is the fact that the clearing arm and thus also the clearing elements work together with the inner circumference of the semicircular grate bars.
  • the clearing arm is thus arranged on the side of the separating surface on which the material to be separated is still in the flowing liquid. There is therefore a risk that the material to be separated will also settle on the clearing arm, so that there will be blockages.
  • Another particular disadvantage is that the clearing elements of the clearing arm work in the direction of flow of the liquid through the separating surface. There is a considerable push-through effect, ie a large part of the material to be removed is pressed between the grate bars from the inside out and remains in the liquid, so that the cleaning effect of the device is limited.
  • Another device for removing material to be separated from liquid flowing in a channel is known from DE 3019 127 C2.
  • grate bars which are firmly connected to one another are used to form the separating surface, the grate bars extending approximately over 270 ° of the circumference of the cylinder jacket.
  • the grate bars are flowed through from the inside to the outside, ie the concave side of the grate bars is arranged facing the direction of flow of the liquid in the channel.
  • the inflow into the separating surface takes place via the open end face.
  • a clearing arm which is occupied by clearing elements, cooperates with the grate bars and the drive of the conveying device is used to drive it.
  • the conveyor with its shaft, housing and conveyor helix, is arranged concentrically with the axis of the cylinder jacket.
  • the receiving opening of the housing of the conveyor is located in large areas below the water line, in some cases even outside the discharge area of the material to be separated, so that here too there is a risk that the material to be separated will be deposited several times on the separation surface instead of entering the conveyor.
  • the push-through effect also occurs here disadvantageously, ie the material to be separated is pressed in an undesired manner by the clearing elements through the gaps between the grate bars in the direction of flow of the liquid and in this respect is not separated.
  • the invention is based on the object of providing a device of the type described at the outset, the use of which is fundamentally no longer restricted with regard to different channel depths and different water levels in the channel, but also operates reliably under these different conditions of use.
  • this is achieved in a device of the type described in the introduction in that the stationary, at least approximately semicircular grate bars of the separating surface are arranged with their convex side facing the liquid arriving in the channel in the direction of flow, and the separated material is thus deposited on the outside of the fixed separating surface that the broaching elements are provided on the driven broaching arm extending between the grate bars against the direction of passage of the liquid, that the roughly semicircular shaped grate bars not taken part of the cylinder jacket is designed open, and that the conveyor is set with an inclined axis in the channel.
  • the invention is based on the idea of flowing through the semicircular grate bars of the separating surface on the outside, that is to say with respect to the cylinder jacket, from the outside inwards and in doing so depositing the material to be separated on the convex separating surface facing outwards.
  • the end faces of the cylinder jacket are closed, so that the flow, that is to say the inflow and the flow, takes place exclusively on the area of the jacket surface of the cylinder which faces the liquid arriving in the channel and loaded with material to be separated.
  • the fundamental or principal dependence of the mode of operation of the device on the level of the liquid is lost, i. H. the separation area can be used optimally regardless of the water level.
  • the inclination of the device in the channel can easily be changed and adapted, resulting in short lengths in the direction of the channel.
  • the cylindrical jacket-shaped separating surface can be set into the channel in particular with a vertical axis, so that a short overall length results.
  • Another major advantage of the new device is that it can be standardized. It can be easily adapted to different conditions and construction sites by adding or removing grate bars on the one hand and elements of the clearing arm on the other. This makes it possible to assemble and set up the device from standardized individual parts even in countries far from the place of manufacture.
  • the grate bars which are essentially semicircular, extend in this shape by approximately 180 ° and are extended at both ends in the direction of flow.
  • Each individual Ro ⁇ t ⁇ tab has the shape of a walking stick, with the extensions attached to the semicircle on both sides of different lengths can be trained.
  • the extension facing the conveyor is preferably longer than the other extension.
  • the axes or bars are arranged, onto which the grate bars are threaded and thus held with the interposition of spacers. The axes and the spacers do not hinder the circulation of the clearing arm with the clearing elements.
  • this mounting also results in sufficient positioning of the grate bars at a distance in the semicircular part.
  • the clearing elements enter the gap between the grate bars close to an axis, that is to say at a point at which the spacing between the grate bars is exactly maintained by the spacers.
  • the clearing elements can grind on the semicircular grate bars and change them relative to one another in their relative position.
  • this is not disadvantageous because, as a result of the closure, mutual adjustment takes place, so that manufacturing tolerances do not play a role and are, as it were, eliminated.
  • the free-standing ends of the broaching elements withdraw behind the grate bars, as a result of which the material to be separated is transferred at this point without the need for a separate detaching device.
  • the flow of the waste water at this point helps to transfer the material to be separated into the conveying device.
  • the transfer point of the material to be separated from the clearing elements of the clearing arm into the area of the conveyor is arranged below the water level.
  • the direction of flow of the liquid is used to detach the material to be separated from the clearing elements and to feed it to the conveying device.
  • the housing of the conveyor device must be perforated at least over the axial length of the receiving opening, so that not only a flow through the separating surface but also one Flow through the housing of the conveying device takes place in order to favor the transfer of the material to be conveyed to the conveying device and to prevent the separated material from being re-fed to the separating surface.
  • the flow of the liquid is thus advantageously used to transfer the material to be separated.
  • the separating surface and the clearing elements of the clearing arm result in a certain concentration of the material to be separated in the flow upstream of the conveying device.
  • the concentrated material to be separated is then grasped by the conveyor screw of the conveyor under water and led upwards out of the liquid, a portion of the liquid flowing through the openings in the housing of the conveyor.
  • Another important advantage of the invention is that the shaft of the clearing arm and the clearing elements work simultaneously on the cleaned side of the liquid. This not only prevents deposits from being deposited on the clearing arm and clearing elements, but also eliminates the push-through effect, since the clearing elements become effective against the direction of liquid flow through the separating surface.
  • the clearing elements extend from the inside through the gaps between the grate bars and protrude somewhat from the outer convex separation surface, so that they can grasp the separated material to be separated there. Floating material is not pressed through the separation surface in this way, but is intercepted on the convex side.
  • the conveying device also produces a considerable washing effect, since the concentrated material to be separated is moved below the water surface in the area of the conveying device and is pressed against the perforated housing wall of the conveying device.
  • the device also offers the advantage of standardizing the conveying devices, ie a conveying device with a fixed to assign different separators with different diameters of the semicircular grate bars.
  • the conveyor is a separate component that is only spatially assigned to the unit consisting of separating surface and clearing arm.
  • the new device can also be used for very different applications, for example even when a liquid has to be cleaned of separated material. The same applies to channels that have a much greater depth than width.
  • a gusset-like connecting wall can be provided between the semicircular grate bars and the receiving opening of the housing of the conveying device, the axis of the cylindrical jacket-shaped separating surface and the axis of the conveying device being adjustable into the channel with different angles of inclination.
  • the connecting wall can also go through to below the conveyor.
  • the connecting wall can be closed, e.g. B. as a sheet metal wall.
  • the connecting wall can, however, also consist of the walking stick-like extensions of the semicircular grate bars and can thus be open.
  • the connecting wall is designed as a flat surface, which on the one hand connects as tangentially as possible to the separating surface and on the other hand also as tangentially as possible to the housing of the conveyor. This makes it possible to position and assemble the conveyor independently of the arrangement of the separation surface in the channel. It is particularly advantageous if the separation surface is arranged with its axis perpendicular and the conveyor device with its axis inclined at an angle in the channel.
  • the housing of the conveyor can be provided with openings at least over the axial length of the receiving opening. This favors an inflow of the separating material collected and released by the clearing elements into the conveying device.
  • the semicircular grate bars of the separating surface can be lined up on axes using spacers and can be arranged interchangeably and supplemented. Standardization is thus achieved in a simple manner. The adaptation of the device to the given application can be achieved directly on the construction site. On the other hand, the elements of the separation surface can be mass-produced inexpensively.
  • spacers which can generally be designed as spacers, makes it possible in a simple manner to realize different slot widths with identical semicircular grate bars.
  • spacing pieces of different heights can be provided between the grate bars. This is to be understood not only from device to device, but also within a device. So it makes sense and is possible to achieve a narrower slot width in the lower area of the separation area and a larger slot width in the upper area of the separation area, so that small incoming water volumes are carefully sieved, but larger water volumes accelerated by the separation system while reducing the hydraulic resistance ⁇ surface can be passed. An emergency overflow can also be implemented in this way.
  • the housing of the conveyor device can be designed as a sieve or slot wall at least over the axial length of the receiving opening.
  • care must be taken that the total sum of the free area is sufficiently large so that the amount of water flowing directly into the housing of the conveyor is not deflected in the direction of the separating surface.
  • the water flow in this area is used to feed the concentrated separation material to the conveyor - and not to the separation surface again.
  • the gusset-shaped connecting wall can be designed as a closed flat wall and can be arranged in the channel parallel to the direction of flow. The connecting wall can support the support of the separation surface.
  • the clearing arm with its clearing elements can also consist of individual parts which are arranged to be easily exchangeable or supplementary by varying the axial length. This makes it possible to adapt the clearing arm with the clearing elements to a modified axial overall length of the separating surface which is adapted in individual cases.
  • Two separating surfaces with their counteractively driven clearing arms can be assigned to a common conveying device. It goes without saying that the receiving opening of the conveying device is then formed symmetrically to a vertical longitudinal central plane, so that material to be separated is transferred from both separating surfaces into one conveying device and can be fed together to the delivery point. In this way it is possible to take into account different channel widths.
  • the conveyor can have a pressing zone for the material to be separated, which is arranged upstream of the delivery point.
  • the housing of the conveying device is also provided with openings through which the liquid pressed out can be discharged and returned to the channel.
  • a graft of compressed material is formed in the press zone. The material to be separated is thrown off at the delivery point and collected, for example, in a container.
  • the clearing arm on one side and the conveying device on the other hand can each be provided with separate drives. This creates separate units that are spatially assigned to each other. Can be net, and that without ⁇ ie drivingly connected to each other or are dependent on each other. This is useful in order to be able to select the drive of the respective device, in particular the peripheral speeds, in a sensible and independent manner. For example, it makes sense to choose the circumferential speed of the clearing elements to be lower than the flow speed of the liquid in the channel, so that the described detaching effect of the material to be separated runs particularly effectively. Furthermore, it is then readily possible to separately select the periods in which one or the other device is driven or stopped.
  • the end faces of the cylindrical jacket-shaped separating surface are designed to be closed, so that the inflow and throughflow takes place solely in the area of the cylinder jacket on the semi-circular grate bars.
  • the separating surface is closed off by the bottom of the channel, in the case of an oblique arrangement, a bottom crack or a wall of the closure can provide.
  • FIG. 1 shows a schematic side view of a first embodiment of the device
  • FIG. 3 shows a side view of a device in a second embodiment
  • FIG. 4 shows a top view of the device according to FIG. 3,
  • FIG. 5 shows a section through the device according to the line V-V in FIG. 3
  • 6 is a side view of a device in a third embodiment
  • FIG. 7 is a view of the device according to FIG. 6;
  • FIG. 8 is a side view of a device in a fourth embodiment.
  • FIG 9 shows a side view of a further device.
  • the device 1 shows a schematic side view of the device 1 with its parts essential for the invention.
  • the device 1 is set with its axis 2 obliquely into a channel 3, of which only the bottom 4 and a side wall are indicated.
  • the channel 3 is flowed through by the liquid loaded with the material to be separated in the direction of flow 5.
  • the water level can change within wide limits.
  • a comparatively low water level 6 and a comparatively high water level 7 are indicated.
  • the water level can fluctuate below and beyond, because it is e.g. B. largely dependent on rain events.
  • the device 1 has a separating surface 8, which is formed on a cylinder jacket 9 about the axis 2 by a plurality of grate bars 10 which are delimited approximately in a semicircle.
  • the grate bars 10 are only indicated. They go through the height or axial length of the cylinder jacket 9.
  • the grate bars 10 are held or arranged at a mutual distance, so that gaps 11 are formed between the grate bars 10 for the passage of the liquid. Due to the relative arrangement of the semicircular grate bars 10 with their convex side facing the flow direction 5 of the liquid, it can be seen that the cylinder jacket 9 is flowed through from the outside inwards and the separating surface 8 is provided on the outside of the cylinder jacket 8.
  • the separation material contained in the liquid will thus be deposited on the outside of the separating surface 8 of the cylinder jacket 9, while the liquid freed from the material to be separated flows through the gaps 11.
  • the cylinder jacket 9 forming the separating surface 8 is installed here after a step in the bottom 4 of the channel 1 in order to force the liquid to flow through the gaps 11. It is understood that the end faces of the cylinder jacket 9 and the corresponding connections to the side wall of the channel 3 are designed to be closed. For reasons of clarity, these elements are not shown.
  • a clearing arm 12 which is designed in the manner of a bracket, is non-rotatably connected to a shaft 13, the axis of which is arranged in the axis 2. It is understood that the shaft 13 is mounted and held accordingly, although these elements are also not shown for reasons of clarity. The shaft 13 is extended upwards so far that it surely looks out of the water level.
  • An indicated motor 14 is provided as the drive element.
  • the clearing arm 12 is equipped with clearing elements 15, these clearing elements 15 being matched in their geometric arrangement and design to the gaps 11 between the grate bars 10.
  • the clearing elements 15 engage like a comb from the inside to the outside between the grate bars 10 and inside the slots 11, in such a way that they exceed the outer circumference of the cylinder jacket 9 and thus the separating surface 8 by a fixed amount, which is sufficient to at Rotation of the clearing elements 15 or the clearing arm 12 to take up the deposited material deposited on the separating surface 8, to push it forward and to convey it laterally in accordance with the direction of rotation 16 of the clearing arm 12.
  • the material to be separated is largely conveyed below the water level 6 or 7. Only in the upper area of the separation surface 8 can it occur that the material to be separated is above the respective water level is raised; but this material to be separated is also pressed under the water surface towards the end of the conveying movement.
  • a conveying device 17 is provided as a separate, separate unit, which is also arranged with its axis 18 inclined in the channel 3.
  • the conveyor 17 is connected to the device 1 neither in terms of drive nor in any other way. These can be completely separate units, which are set up in channel 3 only in spatial association with one another.
  • the essential features of the conveyor device 17 are a shaft 19 (FIG. 2) which is equipped with a conveyor helix 20.
  • a reduction gear can be provided between the motor 21 and the shaft 19.
  • Another essential element of the conveyor 17 is a tubular housing 22, which is designed to be continuously closed over a large part of the axial extent of the conveyor 17.
  • the housing 22 Only in the lower area - corresponding to the axial length of the separating surface 8 or the cylinder jacket 9 - does the housing 22 have a receiving opening 23 and in its semicircular area facing away from the flow direction, openings 24, which are provided as holes, slots, recesses or the like could be.
  • the openings 24 also extend in the axial direction over the axial length of the cylinder jacket 9 or the separating surface 8.
  • the tubular housing 22 has no openings.
  • In the upper area of the conveyor 17 or the housing 22 is a pressing zone
  • the separated and compressed material to be separated arrives, for example, in a container or other conveying device. direction.
  • the housing 22 can have openings 27 (FIG. 3) through which the liquid squeezed out can be removed from the pressing zone 25 and returned to the channel 3.
  • the openings 27 and the openings 24 can have the same or different, in each case adapted shape.
  • the semicircular grate bars 10 connect in one end region to the one side wall of the channel 3.
  • the grate bars 10 can have extensions 28 which form a transfer point for the material to be separated, which is separated on the separating surface 8 and removed via the clearing elements 15 and concentrated.
  • the housing 22 of the conveyor 17 is arranged so that it connects to the extensions 28, with its receiving opening 23 in the relative position shown in FIG. 2.
  • the extensions 28 extend partly radially with respect to the axis 2 and partly also in the direction of flow 5 of the liquid in the channel 3.
  • the grate bars 10 can be mounted threaded on axes 32 with the interposition of spacers 31, the height of the spacers 31 determining the width of the gaps 11. It is understood that the axes 32 and the spacers 31 are arranged outside the circumferential area of the free ends of the clearing elements 15.
  • the grate bars 10 can be provided with eye-like protrusions 33. The shape of these protrusions 33 is selected so that the deposition of material to be separated is avoided as far as possible.
  • the spacers 31, which can be designed in the simplest form as spacers, can also have different overall heights, so that it is possible to produce different distances or widths of the gaps II.
  • this modular system offers the possibility of changing the axial length of the separating surface 8 in a very simple manner, of adapting it to the relevant application or of exchanging individual grate bars 10.
  • the clearing arm 12 in the embodiment shown in FIG. 3 is divided into individual elements 34, 35, 36, so that the axial length of the assembly is also included within this kit Räumarme ⁇ 12 can be easily changed and adjusted.
  • the respective axial length of the elements 34, 35 and 36 can be selected according to a grid.
  • two separators with their separating surfaces 8 can be assigned to a single conveying device 17, as can be seen in particular from the illustrations in FIGS. 4 and 5.
  • the conveyor 17 is then arranged in the middle, and the clearing arms 12 of the two separators are then driven in opposite directions so that both separators throw the material to be separated into the conveyor 17.
  • two receiving openings 23 or a continuous receiving opening are then provided.
  • the flow of the liquid in the channel 3 in the direction of flow 30 is used to request the material to be separated into the conveying device 17, so that the conveying coil 20 can detect e ⁇ .
  • FIGS. 6 and 7 An embodiment of the device is shown in FIGS. 6 and 7, which is characterized by particular advantages.
  • the cylindrical jacket-shaped separating surface 8 is arranged here in the channel 3 with a vertical axis 2.
  • the semicircular grate bars 10 have extensions 37 on one side, so that they take on a walking stick-like shape.
  • the extensions 37 extend straight in the flow direction 5.
  • the extensions 37 form a connecting wall 38, which here is rectangular in FIG. 6 Has shape. However, only the zwickei-shaped part, which extends above the conveyor 17 and in this respect forms a tangential transition between the semicircular grate bars 10 and the housing 22 of the conveyor 17, is structurally important.
  • the connecting wall 38 created by the extensions 37 is designed as a flat surface. It can be open, as shown in FIG.
  • the connecting wall 38 makes it possible for the separating surface 8, on the one hand, and the conveying device 17, on the other hand, to be set independently of one another in a channel 3 as separate structural units.
  • the axis 2 of the separating surface 8 can be arranged vertically and the axis 18 of the conveying device 17 can be arranged obliquely with a variable angle of inclination. This change in inclination is illustrated by a double arrow 39.
  • the axes 32 are arranged in the region of the extensions 37. Here the parts are threaded and held onto the axes 32 by means of corresponding openings and with the interposition of the spacers 31.
  • the semicircular grate bars 10 In the area of the semicircular grate bars 10, no axes 32 are provided. On the other hand, extensions 40 can also be provided on the semicircular grate bars, but are generally comparatively shorter than the extensions 37. Here, too, the axes 32 are arranged in the area not covered by the clearing elements 15.
  • the semicircular grate bars 10 at the point at which the clearing elements 15 enter the gaps 11 between the grate bars are kept at a precise distance from one another by means of the spacers 31, so that trouble-free entry is possible.
  • the clearing elements 15 circulate, self-adaptation to the semicircular grate bars 10 takes place.
  • the clearing elements 15 collect and push the material to be separated on the separating surface 8 together on the outside on the convex side.
  • spacers 31 of different heights can also be used in all other embodiments. Coarse and fine rakes can be realized with this. It is also possible to use spacer portions 31 of different heights in some areas of a device (FIG. 9), so that, depending on the water level, z. B. an emergency overflow can be created.
  • the axis 2 of the separating surface 8 is arranged inclined.
  • the extensions 37 of the grate bars 10, which are not illustrated, are kinked and the connecting wall 38 is clad by a gusset-shaped sheet 43 and is thus closed.
  • FIG. 9 corresponds to wide areas of the device according to FIG. 6.
  • An emergency circulation is formed in the upper area of the separating surface 8.
  • the normal maximum water level 6 is shown.
  • a spray bar 44 can be arranged under water, with which a flow directed towards the conveying device 17 is generated through the gaps between the extensions 37.
  • a nozzle bar 45 can be arranged, which is used to spray out used water in order to achieve a washing effect for the material to be separated in the area of the conveying device 17.
  • the housing 22 of the conveying device 17 is designed open here or the receiving opening 23 is correspondingly extended.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Hydrology & Water Resources (AREA)
  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Water Supply & Treatment (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Water Treatment By Sorption (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Treatment Of Sludge (AREA)

Abstract

Ce dispositif sert à enlever des matières à éliminer d'un liquide qui s'écoule dans une rigole (3), notamment dans des installations d'épuration. Le dispositif comprend une surface d'élimination (8) notamment verticale, de forme cylindrique, partiellement immergée dans le liquide et constituée de barreaux fixes et mutuellement espacés au moins approximativement semi-circulaires (10). Au moins un bras de raclage (12) entraîné en rotation autour de l'axe (2) de la surface d'élimination (8) comprend des éléments racleurs (15) qui passent de l'intérieur vers l'extérieur entre les barreaux (10). Un convoyeur (17) de matières à éliminer, pourvu d'un boîtier tubulaire (22) avec une ouverture (23) pour les matières à éliminer et d'une vis sans fin entraînée, est adjacent à la surface d'élimination (8) et mène à une zone de distribution située à l'extérieur du liquide. La face convexe des barreaux fixes (10) au moins approximativement semi-circulaires de la surface d'élimination (8) est orientée dans la direction du liquide arrivant dans la rigole (3) dans le sens d'écoulement, de sorte que les matières à éliminer s'accumulent du côté extérieur de la surface fixe d'élimination (8). Les éléments racleurs (15) sur le bras entraîné de raclage (12) s'étendent entre les barreaux (10) de la grille en sens opposé au sens de passage (29) du liquide. La partie de l'enveloppe cylindrique (9) qui n'est pas occupée par les barreaux approximativement semi-circulaires (10) de la grille est ouverte. L'axe du convoyeur (17) est incliné lorsqu'il est placé dans la rigole (3).
EP96924855A 1995-07-04 1996-07-03 Dispositif pour retirer des matieres a eliminer d'un liquide qui s'ecoule dans une rigole Withdrawn EP0778790A1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19524276A DE19524276C2 (de) 1995-07-04 1995-07-04 Vorrichtung zum Entfernen von Abscheidegut aus in einem Gerinne strömender Flüssigkeit
DE19524276 1995-07-04
PCT/EP1996/002900 WO1997002081A1 (fr) 1995-07-04 1996-07-03 Dispositif pour retirer des matieres a eliminer d'un liquide qui s'ecoule dans une rigole

Publications (1)

Publication Number Publication Date
EP0778790A1 true EP0778790A1 (fr) 1997-06-18

Family

ID=7765942

Family Applications (1)

Application Number Title Priority Date Filing Date
EP96924855A Withdrawn EP0778790A1 (fr) 1995-07-04 1996-07-03 Dispositif pour retirer des matieres a eliminer d'un liquide qui s'ecoule dans une rigole

Country Status (16)

Country Link
US (1) US5755958A (fr)
EP (1) EP0778790A1 (fr)
JP (1) JPH10505643A (fr)
KR (1) KR970705426A (fr)
CN (1) CN1158091A (fr)
AU (1) AU700567B2 (fr)
BR (1) BR9606465A (fr)
CA (1) CA2198006A1 (fr)
CZ (1) CZ64497A3 (fr)
DE (1) DE19524276C2 (fr)
HU (1) HUP9702442A3 (fr)
NZ (1) NZ313171A (fr)
PL (1) PL318805A1 (fr)
RU (1) RU2156641C2 (fr)
TR (1) TR199700122T1 (fr)
WO (1) WO1997002081A1 (fr)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE507499C2 (sv) * 1996-10-07 1998-06-15 Spirac Engineering Ab Separationsanordning försedd med transportspiral och silorgan
US5840180A (en) * 1997-06-02 1998-11-24 John Meunier Inc. Water flow segregating unit with endless screw
ATE288975T1 (de) * 1997-09-03 2005-02-15 Brian Warren Leahy Schadstoff-auffänger
DE19755588C2 (de) * 1997-12-15 2001-03-22 Hans Huber Ag Masch & Anlagenb Vorrichtung zum Entfernen von Abscheidegut aus in einem Gerinne strömender Flüssigkeit
AU6972200A (en) * 1999-08-25 2001-03-19 Wolfgang Lindner Cleaning device for a flowing medium, in particular waste water
GB2360001B (en) * 2000-03-07 2002-09-04 Stephen David Rivers Storm water screen
GB0008055D0 (en) * 2000-04-03 2000-05-24 Apoc Limited Up-flow rake bar screen
CN1314867C (zh) * 2004-11-25 2007-05-09 江苏省农业机械研究所有限公司 下水道泥水分离设备
EA018541B1 (ru) * 2012-03-07 2013-08-30 Егор Алексеевич Курятников Устройство для комплексной механической очистки сточных вод
CN102755773B (zh) * 2012-08-07 2014-03-05 李连乐 一种压榨式滤袋过滤机
CN105060362B (zh) * 2015-07-31 2017-10-31 艾迪机器(杭州)有限公司 一种污水池用耙松机
CN109589675B (zh) * 2018-12-12 2020-12-18 嘉兴市盛康信息科技有限公司 一种管道过滤装置
CN110433544A (zh) * 2019-07-08 2019-11-12 范国江 一种污水过滤装置
US11633680B2 (en) * 2020-07-23 2023-04-25 Parkson Corporation Bar screen filter apparatus and method
CN112755604A (zh) * 2020-12-10 2021-05-07 无锡帝浦瑞斯环保科技有限公司 一种高负荷的侧向流进水装置及其工艺
CN113214352B (zh) * 2021-05-26 2023-07-25 江苏海洋大学 一种新型从微藻中提取蛋白的装置及其方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2910181A (en) * 1956-07-02 1959-10-27 Passavant Werke Combined rake and crushing system
DE2411626A1 (de) * 1973-04-18 1975-09-18 Schreiber August Rechenharke zum reinigen eines in einem wasserkanal angeordneten rechens
DE3019127C2 (de) * 1980-05-20 1983-02-03 Günther 7913 Senden Abel Vorrichtung zum Entfernen von Rechengut aus Zulaufgerinnen, insbesondere von Kläranlagen
DE3138674A1 (de) * 1980-09-29 1982-06-16 Passavant-Werke AG & Co KG, 6209 Aarbergen Sieb- oder rechenvorrichtung zur mechanischen rinigung von schmutzwasser
WO1991013672A2 (fr) * 1990-03-06 1991-09-19 Abel Guenther Appareil servant a separer les liquides des solides
DE4006970A1 (de) * 1990-03-06 1991-09-12 Abel Vorrichtung zur reinigung von abwasser
DE4308333A1 (de) * 1993-03-16 1994-09-22 Geiger Maschf Helmut Reinigungsvorrichtung zur Reinigung von in einem Gerinne fließendem Wasser
DE9303867U1 (fr) * 1993-03-16 1993-05-06 Maschinenfabrik Hellmut Geiger Gmbh & Co Kg, 7500 Karlsruhe, De

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9702081A1 *

Also Published As

Publication number Publication date
NZ313171A (en) 1998-01-26
BR9606465A (pt) 1997-09-30
AU6517996A (en) 1997-02-05
JPH10505643A (ja) 1998-06-02
WO1997002081A1 (fr) 1997-01-23
RU2156641C2 (ru) 2000-09-27
CZ64497A3 (en) 1997-08-13
AU700567B2 (en) 1999-01-07
KR970705426A (ko) 1997-10-09
DE19524276A1 (de) 1997-01-16
HUP9702442A3 (en) 1998-12-28
US5755958A (en) 1998-05-26
PL318805A1 (en) 1997-07-07
DE19524276C2 (de) 1999-06-17
CA2198006A1 (fr) 1997-01-23
CN1158091A (zh) 1997-08-27
HUP9702442A2 (hu) 1998-03-30
TR199700122T1 (tr) 1997-08-21

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