EP0056732B1 - Apparatus for applying marking materials to surfaces - Google Patents

Apparatus for applying marking materials to surfaces Download PDF

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Publication number
EP0056732B1
EP0056732B1 EP82300274A EP82300274A EP0056732B1 EP 0056732 B1 EP0056732 B1 EP 0056732B1 EP 82300274 A EP82300274 A EP 82300274A EP 82300274 A EP82300274 A EP 82300274A EP 0056732 B1 EP0056732 B1 EP 0056732B1
Authority
EP
European Patent Office
Prior art keywords
container
marking
duct
marking material
burner
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
Application number
EP82300274A
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German (de)
French (fr)
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EP0056732A1 (en
Inventor
David Nicholas Kilner
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.)
REDLAND PRISMO Ltd
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REDLAND PRISMO Ltd
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Filing date
Publication date
Application filed by REDLAND PRISMO Ltd filed Critical REDLAND PRISMO Ltd
Priority to AT82300274T priority Critical patent/ATE13078T1/en
Publication of EP0056732A1 publication Critical patent/EP0056732A1/en
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Publication of EP0056732B1 publication Critical patent/EP0056732B1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/16Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas incorporating means for heating or cooling the material to be sprayed
    • B05B7/20Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas incorporating means for heating or cooling the material to be sprayed by flame or combustion
    • B05B7/201Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas incorporating means for heating or cooling the material to be sprayed by flame or combustion downstream of the nozzle
    • B05B7/205Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas incorporating means for heating or cooling the material to be sprayed by flame or combustion downstream of the nozzle the material to be sprayed being originally a particulate material
    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C23/00Auxiliary devices or arrangements for constructing, repairing, reconditioning, or taking-up road or like surfaces
    • E01C23/16Devices for marking-out, applying, or forming traffic or like markings on finished paving; Protecting fresh markings
    • E01C23/20Devices for marking-out, applying, or forming traffic or like markings on finished paving; Protecting fresh markings for forming markings in situ
    • E01C23/206Devices for marking-out, applying, or forming traffic or like markings on finished paving; Protecting fresh markings for forming markings in situ by applying fusible particulate material to the surface, e.g. by means of a gaseous stream

Definitions

  • the invention is concerned with improvements in or relating to apparatus for applying marking marterials to road surfaces.
  • Various apparatus for applying marking materials to road surfaces such as highways and airport runways are known. These include arrangements in which a supply of the marking material is preheated to melt a constituent of the material and is then applied to a surface to be marked by passing through insulated pipes to an applicator.
  • This method suffers the drawback that it involves a high capital outlay on the apparatus for heating the marking material in bulk and maintaining it at an appropriate temperature until it is applied. This is usually done by employing two vehicles one carrying the bulk supply of material and the other the applicator apparatus, although one large vehicle may suffice.
  • Devices for spraying particulate materials to form coatings on substrates are a19 0 known and include "flame" spray devices or apparatuses which are normally used to apply coatings of refactory material and the like.
  • "flame" spray devices for example as shown in British Patent 1109481 it is usual for the particulate material to be subjected to the direct effect of a flame.
  • This has the disadvantage that, where materials with low melt temperatures are subjected to the direct effect of the flame, great care has to be taken to ensure the accuracy of the residence time of such materials in the flame if charring of the materials is to be avoided.
  • high melt temperature materials are subjected to the heating effects of combustion gases there often has to be some additional heat supply in order to achieve the desired results.
  • pre-heating of the highway surface to between 65.6°C and 260°C is advocated.
  • French Patent 2155837 It is also known from French Patent 2155837 to provide in accordance with the first part of claim 1 an apparatus comprising means to burn a gaseous fuel under pressure to provide a supply of heated pressurized gas, duct means to direct the hot gas onto the road surface to be marked and means to inject a supply of marking material in unfused form into the hot gas stream within the duct means downstream of the burner means, thereby to cause the marking material to impinge on the surface.
  • the apparatus is generally T-shaped with the short arm of the T arranged vertically and the burner means in the longer arm arranged to direct the hot gas stream along that arm and down thp lower part of the shorter arm.
  • Both arms of the apparatus are cylindrical and the marking material is put into the hot gas stream through the upper part of the shorter arm of the apparatus so that it is entrained in the hot gas stream for a very short period or it falls to the surface.
  • the apparatus is described as a road marking apparatus it is wholly unsuitable for this purpose because the geometry of the apparatus does not ensure either a reasonable residence time for the marking material in the hot gas stream or any control over the stream of marking material applied to the surface.
  • the short cylindrical outlet duct of the apparatus could not produce satisfactory road markings.
  • the T-shaped arrangement with the material mixing with the hot gas stream as that stream is turned through 90° would result in wholly unsatisfactory distribution of material in the gas stream.
  • the present invention seeks to overcome these problems and provide an arrangement in which the marking material is directed onto the surface in a controlled manner and in such a way as to ensure satisfactory markings with clearly defined edges.
  • the duct means comprises a first elongate mixing chamber portion down which the hot gas is directed and into which the marking material is injected and a second elongate outlet duct portion co-axial with and downstream of the first portion, the outlet duct portion being of rectangular cross-section and having a ratio of length to maximum cross-sectional dimension of at least 4.75:1 so that the distance of the point of injection of the marking material from the road surface to be marked is such that at least some of the marking material is fused before the marking material impinges on the surface.
  • the outlet duct may be provided with baffle means whereby, when the apparatus is in use, oscillation of the material is prevented thereby obviating accretion of the material to inner walls of the duct.
  • the material is injected by feed means which may comprise at least one inlet port arranged so that material is injected into the hot gaseous jet upstream of the duct.
  • the material is injected into the hot gaseous jet upstream of the duct as aforesaid at an acute angle to the direction of the jet.
  • the acute angle may be up 70° but is preferably 35°.
  • the feed means may also include a fluidised bed arrangement for feeding material to the inlet ports.
  • the feed means may be controlled by means which may be manually operated or may be operated automatically in response to actuation of sensing means.
  • the burner is a flash back burner utilising liquefied propane gas as a fuel and in a preferred apparatus provided by the invention the burner may be connected to the duct through a swirl chamber for damping unwanted oscillations in the exhaust gases from the burner.
  • the ratio of the length of the outlet duct to its maximum cross-sectional dimension is preferably between 4.75:1 and 9:1 and may be approximately 6.5:1.
  • Apparatus used hitherto, for the application of markings, to highways or airport runways, etc., has not always resulted in a well defined durable marking at an acceptable speed of application or an acceptable cost per unit area covered by the marking.
  • the apparatus shown in the drawings enables a layer of a marking material to be sprayed onto a highway, airport runway or the like, with great economy in material usage, at low power consumption and with minimum interruption of traffic flow.
  • the apparatus comprises a bulk storage hopper 10 from which particulate marking material 11 may be fed via a screw elevator 12 to a fluidised bed feed device 14 and then via a line 16 to a mixing tube 18 where the material 11 is injected into a hot gaseous jet, created by a burner 20, before passing along a duct or flight tube 22 to be sprayed onto a highway 24, as shown at 26, to form a marking on the highway 24.
  • the material is injected into a reduced atmosphere.
  • the bulk storage hopper 10 is fed with compressed air from compressor 34 via a line 33 and control valve 31, so that the marking material 11 forms a fluidised bed.
  • the hopper 10 can usefully have a capacity of between one and six tonnes depending upon the size of vehicle on which the novel apparatus is to be used.
  • the screw elevator 12 ideally has a feed rate of between one and fifteen litres per minute and feeds the particulate marking material via a duct 13 to the feed device 14.
  • the feed device 14 has a capacity for 200 kilos of the particulate material fed thereto and comprises a container 30 fed with compressed air to form a fluidised bed. The compressed air is fed from compressor 34 via a line 33 and control valve 32 into the base of the container 30.
  • Material in the container 30 is ideally maintained at a level indicated by the dotted line 35.
  • a level switch 36 provided on a side wall 37 of the container 30, is connected to a motor 38 whereby rotation of the screw elevator 12 is effected in response to movement of a float member 39 forming part of the valve 36.
  • the feed device 14 also comprises a venturi valve 40 connected to the line 16 inside the container 30 which valve 40 is controlled by an actuator 41 whereby the rate of feed of particulate material through the valve 40 may be adjusted or shut-off as required.
  • the actuator 41 is in turn controlled pneumatically, via a solenoid controlled valve 42, from an appropriate control console 72 which may be mounted at any convenient location.
  • the disposition of the venturi valve 40 and the line 16 within the container 30 is consistent with obtaining a flow of the particulate material which is of an acceptable range of particle sizes, i.e. the particulate material will only show small diversities in size over a given period.
  • This is achieved by positioning the valve 40 and line 16 at an optimum level within the container. This occurs because the effect of the fluidised bed 11 is to stratify the particulate material in the container 30 according to the size of granule. Large granules will be more prevalent towards the top of the container and small granules towards the bottom. Thus, at an optimum level the ideal size range of granule can be expected.
  • a pigment feed hopper 44 On the outlet side of the line 16 between the container and the mixing tube 18 there is shown a pigment feed hopper 44 see Figure 3.
  • hoppers 44 there may be two or more hoppers 44 and switching of appropriate venturi valves located within the hoppers 44 enables the desired pigment to be fed into the flow of particulate material in the line 16.
  • the mixing tube 18, see Figure 3 is provided by a tubular chamber, 46 of circular cross section connected at an upper end portion 47, thereof to a combustion chamber 48.
  • the combustion chamber 48 is in turn connected to the outlet end 49 of the burner 20, see Figure 8.
  • the burner 20 may be a commercially available flash back burner using liquid propane gas and air mixture as fuel.
  • the air is supplied via a line 52 from the compressor 34 and the gas is supplied via lines 53 from liquid petroleum gas storage tanks 54, see Figure 3.
  • a spark generator 55 is provided to initially ignite this fuel mixture.
  • This combustion chamber consists of two coaxial cylindrical tubes 57 and 59.
  • the inner tube 57 has two rings of ports 58, which allow the air, fed via line 51 into the passage between tubes 57 and 59, to pass into tube 57 to react with any unreacted fuel.
  • These ports 58 are set at an angle, as shown, so as to introduce the air into tube 57 with a component of velocity in the direction of the general velocity of the gases already in the tube.
  • the mixing tube 18 is connected to the flight tube 22 by a suitable adaptor, not shown.
  • the length of the flight tube 22 is chosen so that the particulate material, which is admixed with the hot gaseous jet in the mixing chamber 18, will remain in the flight tube for a sufficient time for enabling sufficient heat transfer from the gaseous jet to a heat softenable portion of the particulate material to substantially liquefy said portion.
  • the ratio of the length of the tube 22 to its maximum cross-sectional dimension (width) is approximately 6.5:1.
  • flight tube 22 The actual dimensions of the flight tube 22 will be chosen to suit the application, the particulate material, the feed rate of particulate material and the capacity of the burner 20. Thus, in Figure 5 and 6 there are shown two further flight tubes 22a and 22b having length:width ratios of 9:1 and 4.75:1 respectively.
  • the flight tube 22 is also shaped to give a lamella flow of particulate material therefrom.
  • the tube 22a is rectangular in cross-section and of constant dimensions along its length while the tube 22b of Figure 6 is of variable cross-section along its length, being approximately square at its upper end and tapered in one dimension and flared in the other from that end to its lower end.
  • the rectangular shape of the outlet end of the flight tube helps to ensure that markings applied by the apparatus do not have blurred edges.
  • the flight tube 22 is of constant dimension along its length and no great difficulty is encountered in obtaining a true lamella flow of material from a nozzle end 25 thereof.
  • baffle plates may be provided down the centre of the flight tube 22 to split the tube in two length-wise. Indeed several baffles may be provided splitting the flight tube along its length into several parts. Tests on such arrangements have shown that the resultant markings are not impaired in any way while accretion of material to side walls of the flight tubes 22 is prevented.
  • Such alternative methods may include the use of annular inlet ducts for introducing hot gas to the tube 22 to augment the flow of the gaseous jet therethrough. Accretion is also prevented by lining the flight tube with a perforated lining plate, which also has the advantage of reducing the noise of the operation.
  • the apparatus may also include purging means for purging the apparatus of particulate material at the end of work shift.
  • This purging means may comprise a container for cleaning grit, sand, or the like material. This material may be fed into the feed device 14 via a venturi valve similar to valve 40.
  • air from the compressor will cause cleansing material to be fed to the mixing chambers 18 as aforesaid, via the valve 40 and line 16 to purge the mixing chamber 18 and flight tube 22 of any residual particulate material.
  • the purging means may also comprise a fluidised bed for agitating the sand in the container.
  • a material such as small glass beads onto the road 24 to form a top reflective layer of the marking 26.
  • These beads are held in a hopper 60, and may be agitated to form a fluidised bed.
  • To feed these beads to the road they are passed down a tube 61 and through a pneumatically controlled venturi valve 63 onto the road 24.
  • the apparatus described above may be adapted for mounting on a vehicle 80, see Figure 1 and 2, which vehicle is of much simpler design than known road marking vehicles.
  • FIG. 1 there is a laterally moving carriage 81.
  • This carriage includes a feed means 14, and a hopper 60 to hold glass beads and the like.
  • flight-tube there may only be one set of flight-tube, mixing chamber, feed line, combustion chamber and burner, all of which may be mounted as a boom to swing to either side of the vehicle.
  • This boom may be covered by a thermally insulating jacket to protect operative personnel from burns.
  • a gas deflector 86 may be attached to the lower end portion 25 of the flight tube 22. This arrangement is utilised to assist the adhesion and setting of the sprayed on marking 26.
  • the apparatus described above has several major advantages in determining suitable marking materials which it may utilise.
  • the binder resins In the conventional thermoplastic road marking materials, the binder resins must melt to a state of high fluidity to enable the overall composition to be sprayed or flowed (screeded or extruded) onto the road surface. This limits the types of resin, or polymer, which can be used, and also effectively limits the final performance of the road marking material. High fluidity results from relatively low molecular weight which in turn leads to low mechanical strength and toughness.
  • the materials capable of being used by the above apparatus do not have this limitation, in that it is apparently sufficient that individual- binder particles should melt in order to adhere .to the surrounding particles of filler, pigment, beads, etc.
  • binder polymers can be chosen of much higher molecular weight which give enhanced mechanical properties over existing thermoplastic compositions.
  • thermo-setting material is suitable not only for the use of thermoplastic materials, but also for thermo-setting materials.
  • a typical thermo-setting type would be an epoxy powder coating material which comprises an intimate blend of an expoxy compound and a reactant, which do not effectively react to give a polymer until a threshold temperature above 100°C is reached. If used in the above apparatus, such particles would melt to fuse into a coherent whole and a chemical reaction would occur to improve the mechanical properties still further.
  • a composition, particularly suitable for use in the apparatus described above to provide markings on highways or airport runways, etc., is one such as described in our Patent Specification GB-A-1344255 entitled “Improvements Relating to road marking.”
  • particulate material in other forms may also be used in the apparatus e.g. particulate materials in a liquid suspension are envisaged.
  • the vehicle 80 may incorporate any convenient sighting or sensing device for alignment of the flight tube 22 of the spraying apparatus over the portion of the highway 24 to be marked.
  • the vehicle 80 is driven along the highway 24 and a marking 26 applied thereto.
  • the thickness of the marking may be in the range 0.3-4.0 mm and is preferably in the range 0.5-1.5 mm.
  • the operation of the apparatus may be automatic in response of sensing of areas to be marked or the apparatus may be controlled manually from the console 42 by the vehicle driver. In either case the on-off cycle may be achieved by opening and closing the venturi valve 40 of the feed device 14 to interrupt the feed of the particulate material. In short line markings interruption of the burner operation is not necessary; however, in long line markings where long gaps are formed between the markings it is economical to shut off the burner 20.
  • the burner 20 creates a hot gaseous jet in a reducing atmosphere capable of raising the temperature of the particulate material without charring to above its melt temperature which, according to the heat softenable portion of the particulate material used, will be 100 to 400°C.
  • the heat generated by the burner 20 must therefore be in the order of 293 KW in order to provide sufficient latent heat in the hot gaseous jet to enable it to affect the particulate materials as aforesaid.
  • a flashback burner is used to create the gaseous jet.
  • a gas turbine or free piston gas generator may be used.
  • variable geometry flight tube as shown in Figure 9 might be employed rather than the fixed flight tubes described above in order to adjust the width of markings and form symbols such as arrows.
  • ingredients of the marking material need not all be injected into the flight tube at the same point and the aggregate, for example, could be injected upstream of the burner.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Architecture (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Road Repair (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Road Signs Or Road Markings (AREA)
  • Coating Apparatus (AREA)
  • Nozzles (AREA)

Abstract

A method and apparatus for marking road surfaces, runways etc. Marking material, normally a heat fusable solid in particulate form, is passed from a hopper (10) into a duct (18) where it is mixed with hot pressurised gas from a burner (20), the heat from the gas causing the marking material to partially melt. The marking material is then directed along a flight tube (22) from which it is expelled onto the surface (24) being marked. When the material cools the particles fuse together leaving a durable marking on the road surface. The apparatus is mounted on a vehicle in such a way that markings may be applied on either side of the vehicle. Control of the flow of marking material is by variable aperture venturi valves (40), as is control of flow of pigment and, when necessary, of purging material.

Description

  • The invention is concerned with improvements in or relating to apparatus for applying marking marterials to road surfaces.
  • Various apparatus for applying marking materials to road surfaces such as highways and airport runways are known. These include arrangements in which a supply of the marking material is preheated to melt a constituent of the material and is then applied to a surface to be marked by passing through insulated pipes to an applicator. This method suffers the drawback that it involves a high capital outlay on the apparatus for heating the marking material in bulk and maintaining it at an appropriate temperature until it is applied. This is usually done by employing two vehicles one carrying the bulk supply of material and the other the applicator apparatus, although one large vehicle may suffice.
  • Other arrangements are known, for example as described in British Patents 1087031 and 1234601 in which the surface to be marked is preheated and the marking material is then melted by contact with the surface. Some preheating of the material may take place but the melting of the material takes place by contact with the surface. This method again involves the use of complicated apparatus and is also limited in the materials which may be employed. The heat softenable constituent of the marking material must be chosen with a sufficiently low melting point to ensure that it is satisfactorily melted by contact with the preheated surface.
  • Devices for spraying particulate materials to form coatings on substrates are a190 known and include "flame" spray devices or apparatuses which are normally used to apply coatings of refactory material and the like. In such "flame" spray devices for example as shown in British Patent 1109481 it is usual for the particulate material to be subjected to the direct effect of a flame. This has the disadvantage that, where materials with low melt temperatures are subjected to the direct effect of the flame, great care has to be taken to ensure the accuracy of the residence time of such materials in the flame if charring of the materials is to be avoided. On the other hand, in arrangements where high melt temperature materials are subjected to the heating effects of combustion gases there often has to be some additional heat supply in order to achieve the desired results. For example, in United Kingdom Patent Specifications Nos. 1087031 and 1234601 pre-heating of the highway surface to between 65.6°C and 260°C is advocated.
  • It is also known from French Patent 2155837 to provide in accordance with the first part of claim 1 an apparatus comprising means to burn a gaseous fuel under pressure to provide a supply of heated pressurized gas, duct means to direct the hot gas onto the road surface to be marked and means to inject a supply of marking material in unfused form into the hot gas stream within the duct means downstream of the burner means, thereby to cause the marking material to impinge on the surface. In French Patent 2155837 the apparatus is generally T-shaped with the short arm of the T arranged vertically and the burner means in the longer arm arranged to direct the hot gas stream along that arm and down thp lower part of the shorter arm. Both arms of the apparatus are cylindrical and the marking material is put into the hot gas stream through the upper part of the shorter arm of the apparatus so that it is entrained in the hot gas stream for a very short period or it falls to the surface. Although the apparatus is described as a road marking apparatus it is wholly unsuitable for this purpose because the geometry of the apparatus does not ensure either a reasonable residence time for the marking material in the hot gas stream or any control over the stream of marking material applied to the surface. The short cylindrical outlet duct of the apparatus could not produce satisfactory road markings. Moreover the T-shaped arrangement with the material mixing with the hot gas stream as that stream is turned through 90° would result in wholly unsatisfactory distribution of material in the gas stream.
  • The present invention seeks to overcome these problems and provide an arrangement in which the marking material is directed onto the surface in a controlled manner and in such a way as to ensure satisfactory markings with clearly defined edges.
  • Accordingly the invention is characterized in that the duct means comprises a first elongate mixing chamber portion down which the hot gas is directed and into which the marking material is injected and a second elongate outlet duct portion co-axial with and downstream of the first portion, the outlet duct portion being of rectangular cross-section and having a ratio of length to maximum cross-sectional dimension of at least 4.75:1 so that the distance of the point of injection of the marking material from the road surface to be marked is such that at least some of the marking material is fused before the marking material impinges on the surface.
  • The outlet duct may be provided with baffle means whereby, when the apparatus is in use, oscillation of the material is prevented thereby obviating accretion of the material to inner walls of the duct. Conveniently the material is injected by feed means which may comprise at least one inlet port arranged so that material is injected into the hot gaseous jet upstream of the duct.
  • Preferably the material is injected into the hot gaseous jet upstream of the duct as aforesaid at an acute angle to the direction of the jet. Conveniently the acute angle may be up 70° but is preferably 35°.
  • In one preferred apparatus provided by the invention there are two inlet ports arranged as aforesaid for injecting material into the hot gaseous jet. The feed means may also include a fluidised bed arrangement for feeding material to the inlet ports. Conveniently the feed means may be controlled by means which may be manually operated or may be operated automatically in response to actuation of sensing means. There is preferably a burner to provide the supply of heated pressurised gas. Conveniently the burner is a flash back burner utilising liquefied propane gas as a fuel and in a preferred apparatus provided by the invention the burner may be connected to the duct through a swirl chamber for damping unwanted oscillations in the exhaust gases from the burner.
  • The ratio of the length of the outlet duct to its maximum cross-sectional dimension is preferably between 4.75:1 and 9:1 and may be approximately 6.5:1.
  • A preferred embodiment of the invention will now be described, by way of example, with reference to the accompanying drawings, in which:-
    • Figure 1 is a side view of a vehicle fitted with the apparatus for applying marking material of the present invention:
    • Figure 2 is a plan view of the vehicle and apparatus shown in Figure 1;
    • Figure 3 is a diagrammatic representation of the spraying apparatus;
    • Figure 4 is a diagrammatic representation of an alternative apparatus incorporating a gravity feed arrangement for feeding particulate material;
    • Figure 5 and 6 each show front and side views of alternative configurations of a flight tube for use in the apparatus of Figures 1 to 4,
    • Figure 7 shows two views, side and plan, of a gas deflector for attachment to a flight tube of the apparatus;
    • Figure 8 shows a burner and swirl chamber in section; and -
    • Figure 9 shows a further configuration of flight-tube with a variable geometry.
  • Apparatus used hitherto, for the application of markings, to highways or airport runways, etc., has not always resulted in a well defined durable marking at an acceptable speed of application or an acceptable cost per unit area covered by the marking.
  • The apparatus shown in the drawings enables a layer of a marking material to be sprayed onto a highway, airport runway or the like, with great economy in material usage, at low power consumption and with minimum interruption of traffic flow.
  • Referring first to Figure 3, the apparatus comprises a bulk storage hopper 10 from which particulate marking material 11 may be fed via a screw elevator 12 to a fluidised bed feed device 14 and then via a line 16 to a mixing tube 18 where the material 11 is injected into a hot gaseous jet, created by a burner 20, before passing along a duct or flight tube 22 to be sprayed onto a highway 24, as shown at 26, to form a marking on the highway 24. The material is injected into a reduced atmosphere. The bulk storage hopper 10 is fed with compressed air from compressor 34 via a line 33 and control valve 31, so that the marking material 11 forms a fluidised bed. The hopper 10 can usefully have a capacity of between one and six tonnes depending upon the size of vehicle on which the novel apparatus is to be used.
  • The screw elevator 12 ideally has a feed rate of between one and fifteen litres per minute and feeds the particulate marking material via a duct 13 to the feed device 14. The feed device 14 has a capacity for 200 kilos of the particulate material fed thereto and comprises a container 30 fed with compressed air to form a fluidised bed. The compressed air is fed from compressor 34 via a line 33 and control valve 32 into the base of the container 30.
  • Material in the container 30 is ideally maintained at a level indicated by the dotted line 35. A level switch 36, provided on a side wall 37 of the container 30, is connected to a motor 38 whereby rotation of the screw elevator 12 is effected in response to movement of a float member 39 forming part of the valve 36. The feed device 14 also comprises a venturi valve 40 connected to the line 16 inside the container 30 which valve 40 is controlled by an actuator 41 whereby the rate of feed of particulate material through the valve 40 may be adjusted or shut-off as required. The actuator 41 is in turn controlled pneumatically, via a solenoid controlled valve 42, from an appropriate control console 72 which may be mounted at any convenient location. The disposition of the venturi valve 40 and the line 16 within the container 30 is consistent with obtaining a flow of the particulate material which is of an acceptable range of particle sizes, i.e. the particulate material will only show small diversities in size over a given period. This is achieved by positioning the valve 40 and line 16 at an optimum level within the container. This occurs because the effect of the fluidised bed 11 is to stratify the particulate material in the container 30 according to the size of granule. Large granules will be more prevalent towards the top of the container and small granules towards the bottom. Thus, at an optimum level the ideal size range of granule can be expected.
  • On the outlet side of the line 16 between the container and the mixing tube 18 there is shown a pigment feed hopper 44 see Figure 3. In an alternative arrangement there may be two or more hoppers 44 and switching of appropriate venturi valves located within the hoppers 44 enables the desired pigment to be fed into the flow of particulate material in the line 16. There may be spaced along line 16 a number of annular passages for cooling the air.
  • The mixing tube 18, see Figure 3, is provided by a tubular chamber, 46 of circular cross section connected at an upper end portion 47, thereof to a combustion chamber 48. The combustion chamber 48 is in turn connected to the outlet end 49 of the burner 20, see Figure 8.
  • The burner 20 may be a commercially available flash back burner using liquid propane gas and air mixture as fuel. The air is supplied via a line 52 from the compressor 34 and the gas is supplied via lines 53 from liquid petroleum gas storage tanks 54, see Figure 3. A spark generator 55 is provided to initially ignite this fuel mixture.
  • The arrangement is such that a mixture of air and propane is combusted in the flash back burner 20 and the gases produced as a jet are prevented from oscillating unduly by passing the gaseous jet through the swirl chamber 48 as shown in Figure 8. This combustion chamber consists of two coaxial cylindrical tubes 57 and 59. The inner tube 57 has two rings of ports 58, which allow the air, fed via line 51 into the passage between tubes 57 and 59, to pass into tube 57 to react with any unreacted fuel. These ports 58 are set at an angle, as shown, so as to introduce the air into tube 57 with a component of velocity in the direction of the general velocity of the gases already in the tube.
  • At the lower end portion 56 thereof the mixing tube 18 is connected to the flight tube 22 by a suitable adaptor, not shown.
  • The length of the flight tube 22 is chosen so that the particulate material, which is admixed with the hot gaseous jet in the mixing chamber 18, will remain in the flight tube for a sufficient time for enabling sufficient heat transfer from the gaseous jet to a heat softenable portion of the particulate material to substantially liquefy said portion.
  • In the arrangement shown diagrammatically in Figure 3 the ratio of the length of the tube 22 to its maximum cross-sectional dimension (width) is approximately 6.5:1.
  • The actual dimensions of the flight tube 22 will be chosen to suit the application, the particulate material, the feed rate of particulate material and the capacity of the burner 20. Thus, in Figure 5 and 6 there are shown two further flight tubes 22a and 22b having length:width ratios of 9:1 and 4.75:1 respectively.
  • The flight tube 22 is also shaped to give a lamella flow of particulate material therefrom. Thus; as can clearly be seen from Figure 5 and the tube 22a is rectangular in cross-section and of constant dimensions along its length while the tube 22b of Figure 6 is of variable cross-section along its length, being approximately square at its upper end and tapered in one dimension and flared in the other from that end to its lower end. The rectangular shape of the outlet end of the flight tube helps to ensure that markings applied by the apparatus do not have blurred edges. In the arrangement shown in Figure 3 the flight tube 22 is of constant dimension along its length and no great difficulty is encountered in obtaining a true lamella flow of material from a nozzle end 25 thereof. However, with some lengths of tube conditions may arise in which the gaseous jet and admixed particulate material oscillate within the tube leading to accretion of the particulate material to the side walls of the flight tube 22. In order to prevent the occurrence of unwanted oscillations and the consequent accretion of the particulate material to the side walls of the flight tube 22, baffle plates may be provided down the centre of the flight tube 22 to split the tube in two length-wise. Indeed several baffles may be provided splitting the flight tube along its length into several parts. Tests on such arrangements have shown that the resultant markings are not impaired in any way while accretion of material to side walls of the flight tubes 22 is prevented.
  • It is also envisaged that use may be made of alternative methods of preventing unwanted oscillation of the material in the flight tube. Such alternative methods may include the use of annular inlet ducts for introducing hot gas to the tube 22 to augment the flow of the gaseous jet therethrough. Accretion is also prevented by lining the flight tube with a perforated lining plate, which also has the advantage of reducing the noise of the operation.
  • In the arrangement shown in Figure 3 only one line 16 is shown connecting with the mixing chamber 18; however two or more such lines may be connected to the chamber 18, see Figure 4. In addition it is envisaged that, while the lines 16 are arranged at an acute angle of 35° to a longitudinal axis of the mixing chamber 18, in the embodiments illustrated, any convenient angle of entry may be used. In addition the entry ports need not be diametrically opposite one another, as shown in Figure 4, but may be staggered along the length of the mxing chamber 18.
  • The apparatus may also include purging means for purging the apparatus of particulate material at the end of work shift. This purging means may comprise a container for cleaning grit, sand, or the like material. This material may be fed into the feed device 14 via a venturi valve similar to valve 40.
  • Thus, air from the compressor will cause cleansing material to be fed to the mixing chambers 18 as aforesaid, via the valve 40 and line 16 to purge the mixing chamber 18 and flight tube 22 of any residual particulate material.
  • The purging means may also comprise a fluidised bed for agitating the sand in the container.
  • It is often desired to spray a material such as small glass beads onto the road 24 to form a top reflective layer of the marking 26. These beads are held in a hopper 60, and may be agitated to form a fluidised bed. To feed these beads to the road they are passed down a tube 61 and through a pneumatically controlled venturi valve 63 onto the road 24.
  • The apparatus described above may be adapted for mounting on a vehicle 80, see Figure 1 and 2, which vehicle is of much simpler design than known road marking vehicles.
  • In the arrangement shown in Figures 1 and 2, there is a laterally moving carriage 81. This carriage includes a feed means 14, and a hopper 60 to hold glass beads and the like. There are also two sets of flight-tube 22, mixing chamber 18, feed line 16, combustion chamber 48 and burner 20 one set at each end of unit 81 and thus one set on either side of the vehicle 80. In addition there are two tubes 61 running from hopper 60, one tube disposed behind each flight-tube 22.
  • As an alternative, there may only be one set of flight-tube, mixing chamber, feed line, combustion chamber and burner, all of which may be mounted as a boom to swing to either side of the vehicle. This boom may be covered by a thermally insulating jacket to protect operative personnel from burns.
  • Although the apparatus described hitherto is provided with a fluidised bed feed means it may be useful in some applications to utilise a gravity feed arrangement as shown in Figure 4. The particulate material can thus be fed to the line 16 via a line 84 and a venturi valve 85 of known configuration.
  • In a further modified apparatus (see Figure 7) a gas deflector 86 may be attached to the lower end portion 25 of the flight tube 22. This arrangement is utilised to assist the adhesion and setting of the sprayed on marking 26.
  • The apparatus described above has several major advantages in determining suitable marking materials which it may utilise.
  • In the conventional thermoplastic road marking materials, the binder resins must melt to a state of high fluidity to enable the overall composition to be sprayed or flowed (screeded or extruded) onto the road surface. This limits the types of resin, or polymer, which can be used, and also effectively limits the final performance of the road marking material. High fluidity results from relatively low molecular weight which in turn leads to low mechanical strength and toughness. The materials capable of being used by the above apparatus do not have this limitation, in that it is apparently sufficient that individual- binder particles should melt in order to adhere .to the surrounding particles of filler, pigment, beads, etc. Thus binder polymers can be chosen of much higher molecular weight which give enhanced mechanical properties over existing thermoplastic compositions.
  • The individual components of the materials used do not need to be thoroughly compounded before application. Thus, a simple blend of polymer powder, pigment, aggregate and glass beads providing it is mixed uniformly before use, apparently gives an homogeneous coating to substrates.
  • The apparatus is suitable not only for the use of thermoplastic materials, but also for thermo-setting materials. A typical thermo-setting type would be an epoxy powder coating material which comprises an intimate blend of an expoxy compound and a reactant, which do not effectively react to give a polymer until a threshold temperature above 100°C is reached. If used in the above apparatus, such particles would melt to fuse into a coherent whole and a chemical reaction would occur to improve the mechanical properties still further.
  • A composition, particularly suitable for use in the apparatus described above to provide markings on highways or airport runways, etc., is one such as described in our Patent Specification GB-A-1344255 entitled "Improvements Relating to road marking."
  • Although such a material is described as particulate, material in other forms may also be used in the apparatus e.g. particulate materials in a liquid suspension are envisaged.
  • The vehicle 80, may incorporate any convenient sighting or sensing device for alignment of the flight tube 22 of the spraying apparatus over the portion of the highway 24 to be marked.
  • The vehicle 80 is driven along the highway 24 and a marking 26 applied thereto. The thickness of the marking may be in the range 0.3-4.0 mm and is preferably in the range 0.5-1.5 mm.
  • The operation of the apparatus may be automatic in response of sensing of areas to be marked or the apparatus may be controlled manually from the console 42 by the vehicle driver. In either case the on-off cycle may be achieved by opening and closing the venturi valve 40 of the feed device 14 to interrupt the feed of the particulate material. In short line markings interruption of the burner operation is not necessary; however, in long line markings where long gaps are formed between the markings it is economical to shut off the burner 20.
  • The end of line definition is remarkably clear and no ghosting in the gaps between markings is evident. The high impact velocity of the marking material on the road surface improves its adhesion.
  • In addition almost perfect resolution and material distribution is achieved with the spraying apparatus. In use, the burner 20 creates a hot gaseous jet in a reducing atmosphere capable of raising the temperature of the particulate material without charring to above its melt temperature which, according to the heat softenable portion of the particulate material used, will be 100 to 400°C. The heat generated by the burner 20 must therefore be in the order of 293 KW in order to provide sufficient latent heat in the hot gaseous jet to enable it to affect the particulate materials as aforesaid.
  • Other advantages of using the apparatus described above to carry out the method of spraying particulate material are:
    • (i) low cost compared with presently available line spraying equipment;
    • (ii) operation as a continuous process by one man using a single vehicle;
    • (iii) short warm up periods for operation conditions to be reached;
    • (iv) low pigment level requirement;
    • (v) instantaneous colour change where hoppers 44 and venturi valves are utilised;
    • (vi) lower fuel consumption compared with known arrangements;
    • (vii) less environmental pollution;
    • (viii) less hazard to operatives from easily shielded applicator assembly;
    • (ix) no hot materials to handle or maintain in liquefied condition;
    • (x) temperature sensitive materials may be used because of short duration at high temperature.
  • In the arrangement described a flashback burner is used to create the gaseous jet. In alternative arrangements a gas turbine or free piston gas generator may be used.
  • Further modifications may also be made to the apparatus within the scope of the invention. For example, a variable geometry flight tube as shown in Figure 9 might be employed rather than the fixed flight tubes described above in order to adjust the width of markings and form symbols such as arrows. Furthermore, the ingredients of the marking material need not all be injected into the flight tube at the same point and the aggregate, for example, could be injected upstream of the burner.

Claims (13)

1. Apparatus for applying to a road surface marking material which is fusible onto the surface, the apparatus comprising means (48) to burn a gaseous fuel in air under pressure to provide a supply of heated pressurised gas, duct means (18, 22) to direct the hot gas onto the road surface to be marked (24) and means to inject a supply of marking material in unfused form into the hot gas stream within the duct means downstream of the burner means, thereby to cause the marking material to impinge on the surface characterised in that the duct means comprises a first elongate mixing chamber portion (18) down which the hot gas is directed and into which the marking material is injected and a second elongate outlet duct portion (22) co-axial with and downstream of the first portion, the outlet duct portion being of rectangular cross-section and having a ratio of length to maximum cross-sectional dimension of at least 4.75:1 so that the distance of the point of injection of the marking material from the road surface to be marked is such that at least some of the marking material is fused before the marking material impinges on the surface.
2. Apparatus as claimed in claim 1 characterised in that the ratio of the length of the outlet duct portion (22) to its maximum cross-sectional dimension is between 4.75:1 and 9:1.
3. Apparatus as claimed in claim 1 characterised in that the ratio of the length of the outlet duct portion (22) to its maximum cross-section dimension is approximately 6.5:1.
4. Apparatus claimed in any one of claims 1 to 3 characterised in that the outlet duct portion (22) includes a baffle extending longitudinally of the duct.
5. An apparatus as claimed in any one of claims 1 to 4 characterized in that the injection means for the marking material comprises a container (30) for the material, at least one supply line (16) connecting the container to the mixing chamber portion (18) and means (34) for supplying compressed gas to the container to entrain the material and carry it through the supply line or lines.
6. An apparatus as claimed in claim 5, characterised in that the container (30) is a fluidised bed and includes at least one Venturi valve (40) for controlling the flow of material from the container.
7. An apparatus as claimed in claim 6, characterised in that it further comprises a hopper (10) for the marking material, a conveyor (12) for transferring material from the hopper to the container and a float valve (36) for determining the level of material in the container and controlling the conveyor in response thereto.
8. An apparatus as claimed in any one of claims 5 to 7 characterised in that it further comprises means for supplying purging material under pressure to the supply line (16) to clear the supply line and duct.
9. An apparatus as claimed in any one of claims 1 to 8, characterised in that the gaseous fuel is ignited in a flashback burner (20) and burns as it is passed through a combustion chamber (48), producing a resultant stream of hot gas.
10. An apparatus as claimed in any of claims 1 to 9 characterised in that the gaseous fuel is liquefied petroleum gas.
11. A road marking vehicle characterised by comprising a self-propelled chassis and apparatus as claimed in any one of claims 1 to 10.
12. A road marking vehicle as claimed in claim 11 characterised by having two duct means (18, 22) and associated with each duct means a burner (20) and a supply line (16), both supply lines feeding from a common container (30), characterised in that the supply lines, burners and duct means are rigidly mounted on the container such that one duct means faces the road surface (24) on each side of the container.
13. A road marking vehicle as claimed in claim 12 characterised in that the container is trans- versibly mounted on the vehicle.
EP82300274A 1981-01-21 1982-01-19 Apparatus for applying marking materials to surfaces Expired EP0056732B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82300274T ATE13078T1 (en) 1981-01-21 1982-01-19 DEVICE FOR APPLYING MARKING MATERIALS TO SURFACES.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8101848 1981-01-21
GB8101848 1981-01-21

Publications (2)

Publication Number Publication Date
EP0056732A1 EP0056732A1 (en) 1982-07-28
EP0056732B1 true EP0056732B1 (en) 1985-05-02

Family

ID=10519119

Family Applications (1)

Application Number Title Priority Date Filing Date
EP82300274A Expired EP0056732B1 (en) 1981-01-21 1982-01-19 Apparatus for applying marking materials to surfaces

Country Status (11)

Country Link
EP (1) EP0056732B1 (en)
JP (1) JPS57184461A (en)
AT (1) ATE13078T1 (en)
AU (1) AU543273B2 (en)
BR (1) BR8200271A (en)
DE (1) DE3263326D1 (en)
ES (1) ES8306818A1 (en)
GB (1) GB2091593B (en)
IE (1) IE52261B1 (en)
MX (1) MX156651A (en)
ZA (1) ZA82222B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008050184B4 (en) * 2008-10-01 2011-04-21 Technische Universität Chemnitz Method and apparatus for high velocity flame spraying
WO2016099410A1 (en) * 2014-12-17 2016-06-23 Altekma Diş Ticaret Boya Maki̇na Sanayi̇ Anoni̇m Şi̇rketi̇ Road marking machines
US10487463B2 (en) * 2017-08-28 2019-11-26 James P. Shea Thermoplastic kettle auxiliary single-pass oil bath heat exchanger system
DE202018101547U1 (en) 2018-03-20 2018-04-09 Heinz Tillack Snow and liquid barriers, especially in covered parking spaces such as garages

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE891852C (en) * 1951-08-21 1953-10-01 Richard Fischhoeder Method and device for applying marking lines to road surfaces
DE1094782B (en) * 1954-04-27 1960-12-15 Robert Ehrismann Method and device for applying markings on streets, parking lots and the like. like
US3393615A (en) * 1966-07-18 1968-07-23 Minnesota Mining & Mfg Apparatus and method for applying fusible organic particulate in a coalesced film condition to a surface
FR2155837A1 (en) * 1971-10-05 1973-05-25 Le Bruno Roland
BE807374A (en) * 1973-11-16 1974-03-15 Soudure Autogene Elect PROCESS FOR MARKING SURFACES BY PROJECTING PULVERULENT MATERIALS WITH A THERMAL TORCH

Also Published As

Publication number Publication date
EP0056732A1 (en) 1982-07-28
BR8200271A (en) 1982-11-23
AU543273B2 (en) 1985-04-18
GB2091593A (en) 1982-08-04
IE52261B1 (en) 1987-08-19
ZA82222B (en) 1983-08-31
IE820057L (en) 1982-07-21
JPS57184461A (en) 1982-11-13
ATE13078T1 (en) 1985-05-15
DE3263326D1 (en) 1985-06-05
AU7945982A (en) 1982-07-29
ES508894A0 (en) 1983-06-01
MX156651A (en) 1988-09-22
ES8306818A1 (en) 1983-06-01
GB2091593B (en) 1984-09-05

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