[0001] The invention is concerned with improvements in or relating to apparatus for applying
marking marterials to road surfaces.
[0002] 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.
[0003] 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.
[0004] 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. 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.
[0005] 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.
[0006] 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.
[0007] 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.
[0008] 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.
[0009] 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°.
[0010] 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.
[0011] 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.
[0012] 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.
[0013] 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.
[0014] 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.
[0015] 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.
[0016] 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.
[0017] 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.
[0018] 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.
[0019] 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.
[0020] 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.
[0021] 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.
[0022] At the lower end portion 56 thereof the mixing tube 18 is connected to the flight
tube 22 by a suitable adaptor, not shown.
[0023] 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.
[0024] 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.
[0025] 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.
[0026] 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.
[0027] 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.
[0028] 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.
[0029] 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.
[0030] 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.
[0031] The purging means may also comprise a fluidised bed for agitating the sand in the
container.
[0032] 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.
[0033] 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.
[0034] 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.
[0035] 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.
[0036] 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.
[0037] 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.
[0038] The apparatus described above has several major advantages in determining suitable
marking materials which it may utilise.
[0039] 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.
[0040] 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.
[0041] 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.
[0042] 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."
[0043] 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.
[0044] 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.
[0045] 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.
[0046] 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.
[0047] 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.
[0048] 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.
[0049] 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.
[0050] 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.
[0051] 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.
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.
1. Dispositif pour l'application d'un matériau de marquage sur une surface de route,
matériau qui fond sur la surface, le dispositif comportant un moyen (48) pour brûler
un combustible gazeux dans de l'air sous pression pour fournir un gaz chaud sous pression,
une conduite (18, 22) pour diriger le gaz chaud vers la surface de la route à marquer
(24) et un moyen pour injecter une alimentation en matériau de marquage à l'état non
fondu dans la veine de gaz chaud dans la conduite en aval du brûleur, pour que le
matériau de marquage frappe la surface, caractérisé en ce que la conduite se compose
d'une première chambre de mélange (18), allongée, dans laquelle descend la gaz chaud
et dans laquelle est injecté le matériau de marquage ainsi qu'une seconde partie de
conduite de sortie allongée (22) coaxiale à la première partie en aval de celle-ci,
la partie de conduite de sortie ayant une section rectangulaire et un rapport entre
la longueur et la dimension maximale de la section au moins égale à 4,75:1 de façon
que la distance entre le point d'injection du matériau de marquage et de la surface
de la route à marquer soit telle qu'au moins une partie du matériau de marquage fonde
avant que le matériau de marquage ne rencontre la surface.
2. Dispositif selon la revendication 1, caractérisé en ce que le rapport de la longueur
de la partie de conduite de sortie (22) à sa dimension maximale est compris entre
4,75:1 et 9:1.
3. Dispositif selon la revendication 1, caractérisé en ce que le rapport de la longueur
de la partie de conduite de sortie (22) à sa dimension maximale de sa section est
approximativement égal à 6,5:1.
4. Dispositif selon l'une quelconque des revendications 1 à 3, caractérisé en ce que
la partie de conduite de sortie (22) comporte une cloison s'étendant longitudinalement
par rapport à la partie de conduite.
5. Dispositif selon l'une quelconque des revendications 1 à 4, caractérisé en ce que
le moyen d'injection du matériau de marquage se compose d'un conteneur (30) pour le
matériau, au moins une conduite d'alimentation (16) reliant le conteneur à la partie
de la chambre de mélange (18) et un moyen (34) pour fournir du gaz comprimé au conteneur
et faire entrer le matériau et le transporter à travers la ou les conduites d'alimentation.
6. Dispositif selon la revendication 5, caractérisé en ce que le conteneur (30) est
un lit fluidisé et comporte au moins une vanne Venturi (40) pour régler le débit de
matériau fourni par le conteneur.
7. Dispositif selon la revendication 6, caractérisé en ce qu'il comporte en outre
une trémie (10) pour le matériau de marquage, un convoyeur (12) pour transférer le
matériau de la trémie vers le conteneur et une vanne à flotteur (36) pour déterminer
le niveau du matériau dans le conteneur et régler le convoyeur en réponse à cela.
8. Dispositif selon l'une quelconque des revendications 5 à 7, caractérisé en ce qu'il
comporte en outre un moyen pour fournir du matériau de purge sous pression à la conduite
d'alimentation (16) pour nettoyer la conduite d'alimentation et les conduites.
9. Dispositif selon l'une quelconque des revendications 1 à 8, caractérisé en ce qu'on
allume le combustible gazeux dans un brûleur instantané (20) et il brûle en traversant
une chambre de combustion (48) donnant une veine résultante de gaz chaud.
10. Dispositif selon l'une quelconque des revendications 1 à 9, caractérisé en ce
que le combustible gazeux est du gaz liquéfié de pétrole.
11. Véhicule de marquage de route caractérisé en ce qu'il comporte un châssis à moteur
et un dispositif selon l'une quelconque des revendications 1 à 10.
12. Véhicule de marquage de route selon la revendication 11, caractérisé en ce qu'il
comporte deux conduites (18, 22) et à chaque conduite est associé un brûleur (20)
et une conduite d'alimentation (16), les deux conduites d'alimentation venant d'un
conteneur commun, caractérisé en ce que les conduites d'alimentation, les brûleurs
et les conduites sont montés rigidement sur le conteneur de façon qu'une conduite
soit dirigée vers la surface de la route (24) de chaque côté du conteneur.
13. Véhicule de marquage de route selon la revendication 12, caractérisé en ce que
le conteneur est monté transversalement sur le vèhi- cule.
1. Einrichtung zum Auftragen von Markierungsmaterial auf eine Straßenoberfläche, wobei
das Material auf die Oberfläche aufschmelzbar ist und wobei die Einrichtung Mittel
(48) zum Verbrennen eines gasförmigen Brennstoffes in Druckluft zur Erzeugung eines
heißen Druckgases umfaßt, ferner Leitungskanäle (18, 22) zum Leiten des heißen Gases
auf die zu markierende Straßenoberfläche (24), sowie Mittel zum Einleiten von Markierungsmaterial
in ungeschmolzener Form in den heißen Gasstrom innerhalb der Leitungskanäle und stromabwärts
der Brennereinrichtung, wodurch das Markierungsmaterial zum Aufprallen auf die Straßenoberfläche
gebracht wird, dadurch gekennzeichnet, daß die Leitungskanäle einen ersten, langgestreckten
Mischkammer-Abschnitt (18) umfassen, in welchem das heiße Gas nach unten strömt und
in welchen das Markierungsmaterial eingeleitet wird, ferner einen zweiten, langgestreckten
Auslaßrohr-Abschnitt (22), welcher koaxial zum und stromabwärts vom ersten Abschnitt
angeordnet ist, wobei der Auslaßrohr-Abschnitt (22) einen rechteckigen Querschnitt
und ein Verhältnis von Länge zum größten Querschnittsmaß von wenigstens 4,75:1 aufweist,
so daß die Entfernung vom Einleit-Ort Markierungsmaterials zu der zu markierenden
Straßenoberfläche derartig ist, daß wenigstens ein Teil des Markierungsmaterials geschmolzen
wird, bevor das Markierungsmaterial auf der Straßenoberfläche auftrifft.
2. Einrichtung nach Anspruch 1, dadurch gekennzeichnet, daß das Verhältnis von Länge
des Auslaßrohr-Abschnittes (22) zum größten Querschnittsmaß zwischen 4,75:1 und 9:1
liegt.
3. Einrichtung nach Anspruch 1, dadurch gekennzeichnet, das das Verhältnis von Länge
des Auslaßrohr-Abschnittes (22) zum größten Querschnittsmaß etwa 6,5:1 ist.
4. Einrichtung nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, daß der Auslaßrohr-Abschnitt
(22) eine in Längsrichtung des rohres verlaufende Leiteinrichtung aufweist.
5. Einrichtung nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, das die Mittel
zum Einleiten des Markierungsmaterials einen Behälter (30) für dieses Material, wenigstens
eine Zuführungsleitung (16) zur Verbindung des Behälters (30) mit dem Mischkammer-Abschnitt
(18) sowie Mittel (34) zur Lieferung eines Druckgases zum Behälter umfassen, wobei
das Druckgas das Material mitreißt und durch die Zuführungsleitung oder -leitungen
transportiert.
6. Einrichtung nach Anspruch 5, dadurch gekennzeichnet, daß der Behälter (30) eine
Wirbelschicht-Kammer ist und wenigstens ein Venturi-Ventil (40) zur Regelung. des
aus dem Behälter abgeführten Materials umfaßt.
7. Einrichtung nach Anspruch 6, dadurch gekennzeichnet, daß ein Vorratsbehälter (10)
für das Markierungsmaterial vorgesehen ist, ferner ein Förderer (12) zum Fördern des
Materials vom Vorratsbehälter (10) zum Behälter (30) und ein Schwimmerventil (36)
zum Aufnehmen des Füllstandes des Materials im Behälter (30) und Steuern des Förderes
in Abhängigkeit vom Füllstand.
8. Einrichtung nach einem der Ansprüche 5 bis 7, dadurch gekennzeichnet, daß Mittel
zum Zuführen von Reinigungsmaterial unter Druck zur Zuführungsleitung (16) vorgesehen
sind, um damit die Zuführungsleitung und die Leitungskanäle zu reinigen.
9. Einrichtung nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, daß der gasförmige
Brennstoff in einem Rückschlag-Brenner (20) gezündet wird, bein Durchströmen einer
Brennkammer (48) verbrennt und so einen Heißgasstrom bildet.
10. Einrichtung nach einem der Ansprüche 1 bis 9, dadurch gekennzeichnet, daß der
gasförmige Brennstoff flüssiges Petroleumgas ist.
11. Straßenmarkierungsfahrzeug, dadurch gekennzeichnet, daß es ein selbstfahrendes
Chassis und eine Einrichtung gemäß einem der Ansprüche 1 bis 10 umfaßt.
12. Straßenmarkierungsfahrzeug nach Anspruch 11, mit zwei Leitungskanal-Anordnungen
(18, 22) sowie jeweils einer jeder Leitungskanal-Anordnung zugeordnet einen Brenner
(20) und eine Zuführungsleitung (16), wobei beide Zuführungsleitungen zur Entnahme
aus einem gemeinsamen Behälter (30) angeordnet sind, dadurch gekennzeichnet, daß die
Zuführungsleitungen, die Brenner (20) und Leitungskanal-Anordnungen (18, 22) jeweils
starr mit dem Behälter (30) verbunden sind derart, daß je eine Leitungskanal-Anordnung
an jeder Seite des Behälters der Straßenoberfläche (24) zugewandt ist.
13. Straßenmarkierungsfahrzeug nach Anspruch 12, dadurch gekennzeichnet, daß der Behälter
auf dem Fahrzeug in Querrichtung verschiebbar angeordnet ist.