EP1424449B1 - Dispositif d'épandage avec dispositif d'humidification du matériau épandable - Google Patents

Dispositif d'épandage avec dispositif d'humidification du matériau épandable Download PDF

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Publication number
EP1424449B1
EP1424449B1 EP03026873A EP03026873A EP1424449B1 EP 1424449 B1 EP1424449 B1 EP 1424449B1 EP 03026873 A EP03026873 A EP 03026873A EP 03026873 A EP03026873 A EP 03026873A EP 1424449 B1 EP1424449 B1 EP 1424449B1
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EP
European Patent Office
Prior art keywords
openings
opening
hollow chamber
nozzle
spreading material
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.)
Expired - Lifetime
Application number
EP03026873A
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German (de)
English (en)
Other versions
EP1424449A2 (fr
EP1424449A3 (fr
Inventor
Richard-Peter Seidl
Reinhold Otto Dankwart
Karl-Rudolf Schmidt
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.)
Kuepper Weisser GmbH
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Kuepper Weisser GmbH
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Publication of EP1424449A3 publication Critical patent/EP1424449A3/fr
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Publication of EP1424449B1 publication Critical patent/EP1424449B1/fr
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Classifications

    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01HSTREET CLEANING; CLEANING OF PERMANENT WAYS; CLEANING BEACHES; DISPERSING OR PREVENTING FOG IN GENERAL CLEANING STREET OR RAILWAY FURNITURE OR TUNNEL WALLS
    • E01H10/00Improving gripping of ice-bound or other slippery traffic surfaces, e.g. using gritting or thawing materials ; Roadside storage of gritting or solid thawing materials; Permanently installed devices for applying gritting or thawing materials; Mobile apparatus specially adapted for treating wintry roads by applying liquid, semi-liquid or granular materials
    • E01H10/007Mobile apparatus specially adapted for preparing or applying liquid or semi-liquid thawing material or spreading granular material on wintry roads

Definitions

  • the invention relates to a salt spreader device, which comprises a device for moistening spreading material, for winter service use.
  • Streusalz to be scattered is usually moistened before it is spread. It is assumed that with moistened salt the tau effect of the salt starts faster and the flying properties of the road salt are positively influenced. However, a moistening of the road salt can lead long before spreading to clumping the road salt still in the reservoir, whereby the spreading would be much more difficult. Humidification therefore takes place essentially only at the moment of the scattering process.
  • the road salt and the sols used to moisten the road salt are carried in separate containers on a winter utility vehicle and mixed together only at the time of actual scattering by the two components are selectively supplied, for example, a rotating spreading disc specifically in a narrowly defined area.
  • the brine supply takes place by means of an overflow container at a central point of the spreading plate, while the road salt is directed against a baffle plate, from which it strikes with a radial component on the spreading plate.
  • the mixing of salt and brine takes place on the spreading plate.
  • Object of the present invention is therefore to show ways how a better moisture penetration of the scattering material can be achieved.
  • the device of the invention has a Streussoffanfeuchtungsvorraum with a passage for the scattering material to which the liquid for moistening the scattering material is supplied from several sides simultaneously.
  • openings in particular nozzles, are arranged distributed around the passage in this wall or in its wall, which are connected via at least one supply line to a liquid reservoir and supplied by the latter with the pre-wet liquid.
  • the liquid supplied via the supply line then flows through the openings or nozzles into the passage and mixes with the passed through the passage through the scattering current. In this way, uniform wetting of the scattering substance can be achieved.
  • the device according to the invention is comparable to an annular nozzle.
  • the term “ring nozzle” will be used below.
  • the scattering material is usually supplied by a scattering container, a downpipe or a chute, through which the scattering material of gravity is fed to the spreading plate.
  • the annular nozzle is provided at the upper end of the drop tube, particularly advantageously directly at the feed opening, since then a further thorough mixing of the scattering substance with brine takes place over the entire drop zone.
  • the drop tube does not necessarily have to be vertical, but may be wholly or partially inclined and form a chute.
  • annular nozzle has between the openings or nozzles and the liquid supply at least one hollow chamber which surrounds the passage.
  • the liquid is then supplied to the hollow chamber and can be distributed in the hollow chamber around the passage so that it flows through all the orifices simultaneously and with the same pressure into the passage.
  • the liquid flows in the radial direction into the passage, so that the individual jets meet with sufficient jet pressure in the center of the hollow chamber and the liquid atomized and / or swirled accordingly.
  • This effect is maximum when two nozzles are arranged diametrically opposite each other, as the Liquid jets then meet perpendicular to each other.
  • the radial orientation of the nozzles offers the advantage that the quantity of scattering material is already penetrated into the interior of liquid at the first contact with the liquid.
  • a structurally particularly simple embodiment provides that the openings or nozzles are formed as holes in a wall of the passage or in a wall of the hollow chamber surrounding the passage.
  • the beam width then depends essentially on the opening diameter, the number of openings over the circumference of the passage and the height of the liquid column in the hollow chamber.
  • the hollow chamber may also be pressurized, so that the beam width depends not on the liquid column but on the pressure applied from the outside to the liquid.
  • a preferred embodiment of the invention provides a spout-like, projecting into the passage protuberance of the nozzle openings.
  • a plurality of groups of openings or nozzles are arranged distributed around the passage and each form a nozzle ring.
  • the nozzle rings can be spaced apart in the direction of the scattering substance passage be, ie be superimposed, and / or may differ from each other in that the nozzles of a nozzle ring have a different diameter than the nozzles of another nozzle ring.
  • the diameter of the nozzles of the lowermost nozzle ring is smaller than the diameter of the nozzles of one or more overlying nozzle rings. Because due to the smaller passage openings, the liquid level in the lower part of the hollow chamber initially rises relatively quickly, so that even with small spread rates and correspondingly small amounts of brine, a sufficiently high pressure is built up to inject the brine to the center of the annular nozzle. In particular, it is prevented that the brine runs down only on the annular wall.
  • the supply of the liquid to the hollow chamber is preferably carried out over two or more uniformly around the circumference of the hollow chamber arranged feed connection points, so that the hollow chamber fills as uniformly as possible with liquid and the liquid accordingly emerges from all nozzles of a nozzle ring with approximately the same jet pressure.
  • the feed connection points are preferably placed so that the liquid supplied does not impinge directly on the nozzle outlet openings but preferably between the nozzles. This serves the favorable distribution of the liquid within the ring, which is considered optimal when the liquid is introduced via the supply connection points in the radial direction in the hollow chamber, so that it impinges perpendicular to the opposite hollow chamber wall between the nozzle openings provided there.
  • a baffle plate can be provided in front of the supply connection points.
  • FIG. 1 is shown schematically in cross section the side view of a spreader.
  • the scattering material is supplied from a storage container, not shown, by means of a suitable conveying device, for example a conveyor belt or a screw conveyor, through a feed channel 1 to the upper end 2 of a drop tube 3.
  • a suitable conveying device for example a conveyor belt or a screw conveyor
  • the scattering material exits and falls onto a scattering agent distributor in the form of a rotating about a rotation axis 5 scattering plate 6, from which the scattering material is dropped by centrifugal force approximately in the horizontal direction.
  • the downpipe 3 is formed telescopically in order to adapt the device to different gritting vehicles.
  • the inclination of the downpipe may be greater or lesser than that in the FIG. 1 is shown.
  • the use of a continuously vertical downpipe is not completely excluded, although the slip effect of an inclined at least in the lower part downpipe facilitates a positionally accurate supply of the scattering material on the spreading plate 6.
  • a moistening device 8 Between the upper end 2 of the drop tube 3 and an opening 7 in the feed channel 1, through which the supplied scattering material passes, is a moistening device 8 provided.
  • the moistening device 8 has a passage 12 bounded by a wall 13. It preferably comprises an annular hollow chamber 9, in which via two opposing feed lines 10 in the radial direction liquid or brine is introduced. The brine then passes through nozzles 11 out of the hollow chamber 9 into the passage 12 formed in this embodiment by the wall 13 of the annular hollow chamber in the direction of the single arrows.
  • the openings 11 in the wall 13 of the passage 12 for introducing the liquid into the passage 12, or the preferred nozzles, are formed by holes in the inner housing wall 13 of the hollow chamber 9.
  • the nozzle openings 11 are distributed at regular intervals around the inner housing wall 13 and in several planes. Each in-plane group of nozzles form a nozzle ring.
  • the in FIG. 1 illustrated passage 12 has three such superimposed nozzle rings with 8 nozzles per nozzle ring.
  • the flow pressure with which the liquid, in particular brine, is forced out of the hollow chamber 9 through the openings 11 essentially depends on the liquid column prevailing in the hollow chamber 9, which in turn depends on the quantity of liquid supplied by the supply lines 10.
  • the nozzles 11 of the lower nozzle ring level in approximately the same amount in the passage 12 inject as the nozzles of the overlying nozzle ring levels, the nozzles 11 of the lower nozzle ring plane have a correspondingly smaller diameter, which increases the throttle effect of these nozzles.
  • nozzles 11 are located in FIG. 1 illustrated nozzle rings vertically above one another. But the nozzle rings could also be arranged offset from each other for the purpose of more uniform humidification of the nozzle scattering material by a certain angle relative to the scattering material passage direction.
  • moistening device 8 has three superimposed nozzle rings. Instead, however, only one or two or optionally more than three nozzle rings may be provided.
  • FIG. 2 A moistening device equipped with three nozzle rings and a hollow chamber 9 is shown in detail in FIG. 2 shown.
  • the hollow chamber 9 is in turn formed by two concentric hollow cylinders, which are closed on both sides by cover rings 14, 15.
  • cover rings 14, 15 In the inner housing wall 13, three nozzle rings were produced in a simple manner by means of a pulling tool, of which in each case only the nozzles 11 cut in the illustration are shown, which project into the passage 12 in the manner of a spout.
  • the flow direction of the scattering material through the passage 12 is indicated by a large arrow.
  • the nozzles 11 are oriented radially to the Streustoff matströmeuros, and two nozzles 11 of each nozzle ring are arranged diametrically opposite each other, so that emerging from the nozzles 11 Brine jets in the center of the passage 12 approximately perpendicular to each other.
  • FIG. 3 illustrating the moistening device 8 in plan view. Shown in FIG. 3 only two nozzle rings that are offset from each other so that viewed in plan view each nozzle of a nozzle ring exactly between two nozzles of the other nozzle ring lie. To better illustrate the different position of the nozzle rings, the two nozzle rings in FIG. 3 and the brine jets emerging from the respective nozzles are shown differently, namely once in solid lines and another time in dashed lines.
  • the particular advantage of the perpendicularly facing, radially oriented nozzle arrangement is the fact that a maximum turbulence of the injected brine is achieved.
  • the nozzle wreaths in FIG. 3 each have eight evenly spaced nozzles. Of course, more or less nozzles may be distributed around the circumference of the passage. However, with eight nozzles distributed over the circumference, it was possible to achieve a relatively uniform wetting of grit, in particular with a passage width of about 145 mm. The passage should not exceed a width of 200 mm and should not be less than 100 mm.
  • the nozzles 11 of the lower nozzle ring have a smaller passage diameter than the nozzles 11 of the upper nozzle ring.
  • Diameters between 1.5 mm and 10 mm are generally suitable. Good results have been obtained when the diameter of the nozzles of the upper nozzle ring was about twice as large as the diameter of the lower nozzle ring, in particular a diameter ratio of 6 mm to 3 mm.
  • the diameter of the nozzles of the intermediate nozzle ring does not necessarily have to be between these two values. Good results were obtained, for example, when the nozzles of the central nozzle ring had the same diameter of 6 mm as the nozzles of the upper nozzle ring.
  • a distance of the nozzle ring center planes between 10 mm and 50 mm, in particular 15 mm, has proved to be suitable.
  • the liquid is supplied to the passage 12 through two leads 10 in the radial direction, wherein the two leads 10 are diametrically opposite each other.
  • other supply lines can be provided, which are preferably distributed uniformly over the circumference of the passage 12.
  • the connection points of the leads 10 to the hollow chamber 9 of the moistening device 8 are chosen so that the liquid supplied against the inner housing wall 13 of the hollow chamber 9 between two nozzles 11 injected so that they can be evenly distributed in the hollow chamber 9 and not immediately by a the nozzles exit again.
  • the liquid is usually pumped with a pressure of 2 bar and a delivery volume between 0 and 100 liters / min in the hollow chamber 9, where it comes, however, essentially without pressure.
  • the cross section of the passage 12 need not be circular.
  • it can also have a square or rectangular or even oval cross-section.
  • the wall 13 of the passage 12 may also have a constriction, so that the passage 12 is also nozzle-shaped.

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  • Engineering & Computer Science (AREA)
  • Architecture (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Nozzles (AREA)
  • Polishing Bodies And Polishing Tools (AREA)
  • Coating Apparatus (AREA)
  • Special Spraying Apparatus (AREA)

Claims (19)

  1. Dispositif d'épandage de sel destiné à être utilisé pour le service d'hiver, comprenant un tube de descente (3) ou glissoir à travers lequel le matériau d'épandage est dirigeable en suivant la pesanteur, un distributeur (6) de matériau d'épandage pour la répartition du matériau d'épandage acheminé à travers le tube de descente (3), et un dispositif d'humidification du matériau d'épandage (8) qui comprend un couloir (12) destiné à y faire passer le matériau d'épandage, lequel couloir est respectivement relié au tube de descente (3) et au glissoir, et au moins une conduite d'amenée (10) destinée à l'amenée du liquide au couloir, le dispositif d'humidification du matériau d'épandage (8) comprenant au moins un groupe d'ouvertures (11), notamment de buses (11), réparties sur le pourtour du couloir (12) et reliées de telle manière à la au moins une conduite d'amenée (10) que du liquide amené par la au moins une conduite d'amenée (10) traverse les ouvertures (11), déferle dans le couloir (12) et humidifie le matériau d'épandage par plusieurs côtés en même temps lors du passage de ce dernier à travers le couloir (12), caractérisé en ce que le dispositif d'humidification du matériau d'épandage (8) est agencé dans la zone d'une extrémité supérieure (2) du tube de descente (3) ou glissoir.
  2. Dispositif selon la revendication 1, les buses (11) étant orientées de telle manière vers le centre du couloir (12) que des jets de buses distincts viennent se rencontrer à l'intérieur du couloir.
  3. Dispositif selon la revendication 1 ou 2, comprenant en outre une chambre creuse (9) agencée entre les ouvertures (11) et la au moins une conduite d'amenée (10), laquelle chambre creuse entoure au moins partiellement le couloir (12).
  4. Dispositif selon la revendication 3, les ouvertures (11) étant réalisées par des trous pratiqués dans une paroi de la carcasse (13) de la chambre creuse (9).
  5. Dispositif selon la revendication 4, les ouvertures de buses faisant saillie dans le couloir (12) à la manière de douilles.
  6. Dispositif selon une des revendications de 3 à 5, au moins deux points de branchement régulièrement répartis sur le pourtour de la chambre creuse (9) étant prévus pour les conduites d'amenée (10).
  7. Dispositif selon une des revendications de 4 à 6, le/les point(s) de branchement pour la au moins une conduite d'amenée (10) étant placé(s) de telle manière sur la chambre creuse (9) que du liquide amené à travers la au moins une conduite d'amenée (10) vient déferler de telle façon contre la paroi de carcasse (13) de la chambre creuse (9) présentant les ouvertures (11) que c'est entre les ouvertures (11) qu'il vient déferler.
  8. Dispositif selon la revendication 7, la au moins une conduite d'amenée (10) étant raccordée de telle manière à la chambre creuse (9) que le liquide peut être amené à la chambre creuse (9) dans un sens radial par rapport au sens d'acheminement du matériau d'épandage.
  9. Dispositif selon une des revendications de 1 à 8, respectivement deux ouvertures (11) étant agencées de manière opposée diamétralement l'une par rapport à l'autre.
  10. Dispositif selon une des revendications de 1 à 9, les ouvertures (11) étant agencées de manière régulière sur le pourtour du couloir (12).
  11. Dispositif selon une des revendications de 1 à 10, plusieurs groupes d'ouvertures (11) étant prévus, qui sont répartis de telle manière sur le pourtour du couloir (12) que chacun de ces plusieurs groupes d'ouvertures (11) constitue une couronne de buses.
  12. Dispositif selon la revendication 11, le diamètre de sortie des ouvertures (11) d'une première couronne de buses étant plus élevé que le diamètre de sortie des ouvertures (11) d'une deuxième couronne de buses.
  13. Dispositif selon la revendication 11 ou 12, les couronnes de buses étant espacées les unes des autres dans le sens de l'acheminement du matériau d'épandage.
  14. Dispositif selon la revendication 12, la première couronne de buses dont les ouvertures sont d'un diamètre plus élevé étant, dans le sens de l'acheminement du matériau d'épandage, agencée avant la deuxième couronne de buses dont les ouvertures sont d'un diamètre plus faible.
  15. Dispositif selon une des revendications de 11 à 14, chaque couronne de buses comprenant au moins trois, de préférence huit ouvertures (11).
  16. Dispositif selon une des revendications de 11 à 15, comportant trois couronnes de buses ou davantage.
  17. Dispositif selon la revendication 16, les ouvertures (11) possédant un diamètre situé entre 1,5 mm et 10 mm, notamment entre 3 mm et 6 mm.
  18. Dispositif selon une des revendications de 13 à 17, l'écart entre deux niveaux de couronnes de buses voisins se situant entre 10 mm et 50 mm, de préférence environ 15 mm.
  19. Dispositif selon une des revendications de 1 à 18, le couloir (12) présentant dans la zone des ouvertures (11) une diamètre intérieur situé entre 100 mm et 200 mm, notamment environ 145 mm.
EP03026873A 2002-11-26 2003-11-24 Dispositif d'épandage avec dispositif d'humidification du matériau épandable Expired - Lifetime EP1424449B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10255101 2002-11-26
DE10255101A DE10255101A1 (de) 2002-11-26 2002-11-26 Streuvorrichtung und Streustoffanfeuchtungsvorrichtung dafür

Publications (3)

Publication Number Publication Date
EP1424449A2 EP1424449A2 (fr) 2004-06-02
EP1424449A3 EP1424449A3 (fr) 2005-01-26
EP1424449B1 true EP1424449B1 (fr) 2010-08-18

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EP03026873A Expired - Lifetime EP1424449B1 (fr) 2002-11-26 2003-11-24 Dispositif d'épandage avec dispositif d'humidification du matériau épandable

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EP (1) EP1424449B1 (fr)
AT (1) ATE478199T1 (fr)
DE (2) DE10255101A1 (fr)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1775387B1 (fr) 2005-10-13 2016-12-07 Küpper-Weisser GmbH Véhicule d'épandage pour service d'hiver
DE102012012146B4 (de) * 2012-06-20 2017-07-13 Nutreon Engineering GmbH Mischen und/oder Dispergieren mithilfe eines Sprühteppichs aus einer fließfähigen Masse

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT360070B (de) 1975-12-15 1980-12-29 Kahlbacher Anton Vorrichtung zum bestreuen von verkehrsflaechen
US5419654A (en) * 1992-09-25 1995-05-30 Kleiger; Scott P. Vehicle for road repair and the like
DE19845083B4 (de) 1998-09-30 2004-01-29 Epoke A/S Alfred Thomsen Verfahren und Vorrichtung zur Verteilung von Taumitteln
DE10007926C2 (de) 2000-02-21 2002-10-02 Kuepper Weisser Gmbh Streuvorrichtung mit einem Zwischenbehälter zum Ausbringen von flüssigem Streugut

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Publication number Publication date
EP1424449A2 (fr) 2004-06-02
DE50312997D1 (de) 2010-09-30
EP1424449A3 (fr) 2005-01-26
ATE478199T1 (de) 2010-09-15
DE10255101A1 (de) 2004-06-03

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