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Manufacturing mastic asphalt
EP0140687A2
European Patent Office
- Other languages
German French - Inventor
Bryan Pope - Current Assignee
- PERMANITE ASPHALT Ltd
Description
translated from
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[0001] The present invention relates to a method and to an installation for producing mastic asphalt and to an improved mastic asphalt block. -
[0002] Mastic asphalt has been manufactured previously by methods in which the main constituents of the mastic asphalt, which generally include bitumen, limestone grit and a powdered limestone filler, are mixed and then heated together for further mixing. The resulting molten mixture is then poured into moulds and allowed to cool and solidify into blocks which are convenient for transporting to the sites on which the asphalt is to be used. -
[0003] A considerable amount of labour is involved in these existing methods and they are wasteful in terms of energy consumption. Consequently the asphalt produced using these methods is relatively expensive. -
[0004] Some attempts have already been made to overcome the disadvantages of these existing methods. -
[0005] For example, in order to mix bitumen with other materials it is necessary to keep it relatively warm so that it remains in a relatively fluid state otherwise it would simply be too viscous to handle efficiently at all. -
[0006] When the warm bitumen is added to the other cold constituent materials, its temperature drops and it must be re-heated before mixing is effected. This cooling and reheating of the bitumen used in manufacturing the asphalt increases the heat energy used in the manufacturing process. -
[0007] It has, therefore, been proposed that the energy consumed in the manufacture of mastic asphalt could be reduced by heating the grit before mixing it with the bitumen and grit so that the hot constituent materials can be mixed without supplying further heat to the mixer. This avoids reheating the already hot bitumen and saves considerable energy. -
[0008] Even this improved method, however, consumes a great deal of heat energy, and quite a large proportion of this energy is, in practice, simply lost into the atmosphere. The heat loss into the atmosphere is not only wasteful and expensive but also makes the the working area around the mixers very hot which is unpleasant for those persons working there. -
[0009] We have appreciated that it would be highly advantageous to recover at least some of the heat which has heretofore been dissipated in the atmosphere and to re-use it for heating the unmixed constituent materials. -
[0010] In one aspect, the apparatus of the invention is characterised in that it comprises means for heating at least some of the constituent materials from which the asphalt is formed prior to mixing, means for mixing the constituent materials, means for cooling the asphalt to a temperature suitable for discharging into a mould and a heat exchanger arrangment . associated with the cooling means
for recovering heat from the asphalt and returning it to the heating means for heating the constituent materials for asphalt to be produced subsequently. -
[0011] In one preferred arrangement it is proposed that heat should be recovered during the mixing of the constituent materials and used in heating the filler for asphalt mixed subsequently. -
[0012] In addition to considerably reducing the heat input required, this arrangement has a further advantage. Although mixing of the constituent materials is best carried out at a temperature of around 180°C, the asphalt is best poured into the moulds at a lower temperature, from around 1200C, the optimum temperature being about 150°C. Thus, if the heat exchange takes place in the latter stages of mixing, the asphalt can be cooled to a temperature ideal for moulding by the time the mixing is complete and the delays which have been necessary in the past while the asphalt is allowed to cool prior to moulding are avoided. -
[0013] Previously, once the hot asphalt has been poured into the moulds, it has been allowed to cool and solidify naturally. However, the asphalt blocks may take as long as four hours to solidify completely and this not only introduces a great deal of delay into the processing of the asphalt but also necessitates the provision of large areas of space in which the moulds can be stored during cooling. -
[0014] We have, therefore, proposed a method of cooling mastic asphalt characterised in that the asphalt is discharged into a plurality of moulds, and the moulds are conveyed through an array of spray nozzles arranged to spray water onto the moulds so that at least some of the water impinging on the moulds forms steam and thereby cools the asphalt; at least a portion of the path along which the moulds are conveyed extending between levels which are spaced from one another in a vertical direction. -
[0015] The entire cooling process may be effected by passing the filled moulds through an array of water spray nozzles in a vertical zig-zag path. In addition to enabling the moulds to travel along a relatively long path in quite a small ground area, this arrangement has the advantage that the use of water sprays in removing heat from the moulds is more efficient than immersing the moulds in water because water sprayed onto the surfaces of the moulds in the initial stages of cooling tends to form steam and so large quantities of heat are removed from the moulds as the latent heat needed to turn water into steam is much greater than the heat required to merely heat the water. -
[0016] As mentioned above, mastic asphalt is usually supplied to the contractors who use it in the form of solid blocks. These blocks generally have a nominal weight of 25kg as this amount can easily be melted in an ordinary bucket. In practice, the blocks vary considerably in weight, size and shape and are, therefore, difficult to stack and store. -
[0017] In a further aspect, the invention provides a method of discharging mastic asphalt into a plurality of moulds through a discharge outlet which can be selectively opened and closed, characterised in that a method of discharging mastic asphalt into a plurality of moulds through a discharge outlet which can be selectively opened and closed, the method being characterised in that the weight of each mould is measured after filling and the time for which the discharge outlet is opened to discharge asphalt into each mould is varied in response to the measured weight of preceding filled moulds so as to render the weight of asphalt discharged into successive moulds substantially uniform. -
[0018] The production of asphalt blocks of uniform size has the advantage that the resulting blocks can be formed into a self-supporting stack which is simply strapped for transporting and does not require a pallet or any other form of packing. This is only possible because the blocks are of uniform size. -
[0019] On site, it is often desirable to break up the blocks of asphalt to enable them to be melted more easily. Existing blocks are usually broken up by striking them with a hammer and it is quite common for the blocks to break into uneven-sized pieces or into a number of very small fragments which cannot be easily melted. We have appreciated that it would be desirable to split the block evenly into a number of suitabe, evenly sized pieces. -
[0020] In a further aspect, the invention provides a mastic asphalt block characterised in that it has formed in a surface thereof at least one groove for facilitating breaking of the block. When such block is gently tapped it will break, in a controlled manner, along the line of the groove or indentation. -
[0021] Thus the method of the invention in its various aspects enables an improved mastic asphalt block to be produced more quickly and cheaply than hitherto. -
[0022] An embodiment of the invention will now be described in detail with reference to the drawings, in which; - Fig. 1 is a schematic block diagram showing a mastic asphalt manufacturing plant in accordance with the invention;
- Fig. 2 is a front elevational view of the mixing arrangement of the plant of Fig. 1;
- Fig. 3 is a side elevational view of the secondary mixer of the plant of Fig. 1;
- Fig. 4 is a simplified plan view of the mixer of Fig. 3;
- Fig. 5 is a front elevational view of the cooling tower of the plant of Fig. 1;
- Fig. 6 is a side elevational view of the cooling tower of Fig. 5;
- Fig. 7 is a schematic block diagram of the mould filling station of the plant of Fig. I;
- Fig. 8 is a perspective view of a self-supporting stack of asphalt blocks; and
- Fig. 9 is a perspective view of a single asphalt block.
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[0023] The manufacturing plant shown in Figs. 1 and 2 enables mastic asphalt to be produced from the raw materials bitumen, limestone grit and powdered limestone filler by an almost completely automatic process. -
[0024] Bulk supplies of bitumen, grit and filler are held inseparate hoppers primary mixer 16 in the proportions necessary to produce the grade of asphalt required. Bitumen is delivered hot to the thehopper 10 and is kept warm at a temperature between 170°C and 200°C to render it sufficiently liquid to flow reasonably easily and is then carried directly to theprimary mixer 16 through apipeline 11. -
[0025] -
[0026] The filler is fed from thehopper 14 into twoheaters 18 where it is heated to a temperature of about 2000 C and then is carried downwards by gravity to theprimary mixer 16, either directly, as shown in Fig. 2 or via a weighinghopper 20 as shown in Fig. 1. The grit is not heated prior to mixing but is added to the other materials in theprimary mixer 16, again, either directly from thehopper 12 or via the weighinghopper 20. -
[0027] The heat retained in the bitumen and the filler is sufficient to permit the asphalt to be mixed without further heat input into themixer 16. Themixer 16 may be of the conventional "vertical" mixer type having a mixing vessel of, typically, 6 tonnes capacity with a central vertical rotating shaft carrying one or more sets of angled mixing blades or paddles which effect the mixing of the raw materials to form mastic asphalt. Themixer 16 is set to operate on a thirty-minute mixing cycle and once the mixing period is over, a gate is opened at the base of themixer 16 to allow its contents to be discharged by gravity through a steeply-angled shute 22 into asecondary mixer 24. -
[0028] Thesecondary mixer 24, which is shown in detail in Figs. 3 and 4, serves two purposes. Firstly, it subjects the asphalt to further mixing, so as to ensure that the raw materials are properly blended and the resulting asphalt is as homogeneous as possible, and, secondly, it acts to cool the asphalt, which not only permits heat to be recovered and re-used but also ensures that the asphalt is at the optimum temperature for moulding. -
[0029] Themixer 24 is, again of the vertical type consisting of amixing tank 26 enclosing a centralrotary spindle 28 which carries two sets ofangled mixing paddles 30. Hot asphalt from theprimary mixer 16 enters themixing tank 26 through anopening 32 at the top of thetank 26 and the cooled asphalt is discharged through an outlet valve (treacle valve) or opening at its base which is closed during mixing by a pneumatically-operatedgate 34. -
[0030] Thesecondary mixer 24 is also provided with anouter jacket 36 of insulating material which encloses a number ofvertical passages 38 for the flow of a heat exchange medium. Thepassages 38 are joined at their upper and lower ends byannular passages mixing tank 26 and heat is transferred from the asphalt to the oil. The hot oil then leaves thesecondary mixer 24 and passes through aheat exchanger 44 where the heat is removed and returned to theheaters 18 for use in heating filler for the next batch of asphalt. -
[0031] Combining thesecondary mixer 24 with a heat exchange arrangement in this way enables considerable savings in terms of heat energy to be made and, as mentioned above, has the advantage that once the secondary mixing cycle is complete, the asphalt has been cooled to a temperature of around 150oC, which is ideal for moulding. Furthermore, if thesecondary mixer 24 is made sufficiently large for example, of 13 tonnes capacity, the filling of the moulds can be entirely separated from the mixing process with thesecondary mixer 24 acting as a buffer between theprimary mixer 16 and the mould-filling equipment. It is also possible, if desired, to provide further primary mixers which discharge into the same secondary mixer. -
[0032] Once the asphalt has been poured into the moulds, which is preferably carried out as described in detail below, the moulds must be cooled so that the asphalt solidifies into fairly rigid blocks. -
[0033] Rapid cooling of the filled moulds is achieved by drawing the moulds through an array of water sprays. The filled moulds are carried from the filling point at the outlet of thesecondary mixer 24 by a suitable form of conveyor into acooling tower 50, which is shown in Figs. 5 and 6. -
[0034] Inside thecooling tower 50 themoulds 52 are coupled to achain conveyor 54. Theconveyor 54 runs in a zig-zag path up-and-down along the length of thetower 50 so as to fit as long a path as possible into a relatively small ground area. Each vertical span of the chain conveyor, may, for example, be about 30 feet (9 metres approximately) in length. -
[0035] Thechain conveyor 54 is surrounded along its sinuous zig-zag path by anarray 56 of nozzles which spray water onto themoulds 52. The water which initially contacts themoulds 52 and their contents is turned into steam, thus removing a relatively large quantity of heat from the asphalt in the form of the latent heat needed to turn the water into steam. Thereafter, heat is removed by merely heating the spray water. Typically, the water temperature rises from about 100C to about 160 C. -
[0036] Consequently, themoulds 52 and their contents are cooled rapidly in a relatively small space. -
[0037] At the end of thechain conveyor 54 remote from the mixers, themoulds 52 are uncoupled from theconveyor 54 and carried away for the asphalt blocks to be unmoulded and packaged prior to being transported to the sites where the asphalt is to be used. -
[0038] As mentioned above, mastic asphalt blocks produced in existing processes tend to vary a great deal in size and shape and are, therefore, difficult to package, because they cannot be stacked, and to transport. Frequently they are also difficult to break up into even-sized pieces. These disadvantages may be overcome in the following manner. -
[0039] In the installation of the invention, themoulds 52 in which the asphalt blocks are formed, are conveyed continuously around a closed-loop path which passes through a mould-fillingstation 53 and anunmoulding station 55. -
[0040] The filling of themoulds 52 is regulated by a control system incorporating a micro-processor 60 as shown in Fig. 7. -
[0041] Eachmould 52 is carried to the mould-fillingstation 53 which is directly below thedischarge gate 34 of thesecondary mixer 24. As mentioned above, thedischarge gate 34 is pneumatically-actuated and can be moved to open and close the discharge outlet at the base of themixer 24. When thegate 34 is open, asphalt falls vertically under gravity from the outlet into amould 52 which is positioned directly below it. The use of a vertical outlet arrangement avoids the problems due to drag and a build-up of asphalt in the shute which arise when an inclined outlet shute is used. -
[0042] Thepneumatic actuator 35 of thegate 34 is controlled by themicroprocessor 60. As eachmould 52 reaches the mould-fillingstation 53, themicroprocessor 60 causes theactuator 35 to open thegate 34. Thegate 34 remains open for the period required for a sufficient amount of asphalt to be discharged into themould 52 to fill it. Thegate 34 is then closed. -
[0043] The filledmould 52 is then conveyed through a weighingstation 64 and a signal representing the weight of the filled mould input into themicroprocessor 60. Themicroprocessor 60 then compares this signal to a stored value, which can either be a desired nominal weight or an average value or the weight of the next preceding mould. Themicroprocessor 60 then adjusts the time for which thedischarge gate 34 is opened to fill subsequent moulds so that the amount of asphalt discharged and, hence the size and weight of the blocks are as consistent as possible. -
[0044] Alternatively, where single moulds are used, each mould may in addition be weighed prior to being filled. The signal representing the weight of the empty mould can then be used by the microprocessor to provide a signal representative of the actual weight of asphalt in the mould which is then compared to a desired value. -
[0045] Themoulds 52 in which the blocks are formed are in the form of a generally rectangular tray consisting of four compartments, each rectangular, having a single integral side wall and a separate spring-biased loose bottom. Each compartment is preferably twice as long as it is wide, for reasons which will be explained in greater detail below, and has a capacity of 20kg of mastic asphalt. Typically, a 20kg block may be 0.5m (20 inches) long and 0.25m (10 inches) wide. To achieve the desired 20kg weight, a mould having these dimensions is filled with mastic asphalt to a depth of 9cm (3b inches). The side wall is not quite perpendicular to the bottom but tapers slightly towards it, typically at an angle of about 8° to the perpendicular, so that the asphalt blocks can more easily be removed from the mould. The use of a loose bottom in the mould allows the finished block to be simply pushed out of it by suitable unmoulding equipment at theunmoulding station 55. -
[0046] Prior to being filled, the inside of each mould is dusted with a little of the powdered limestone filler material to prevent the asphalt sticking to the mould. As a result, the finished blocks tend to have a surface layer of limestone filler which helps to prevent them sticking together. The empty moulds 52 are returned by means of aconveyor 57 to the mould-fillingstation 53 for re-use. -
[0047] Because the blocks produced by the installation of the invention are of a uniform size, they can easily be formed into a self-supportingstack 70, as shown in Fig. 8 of the drawings. For this reason, it is preferred to make the blocks of the rectangular shape described above, as such blocks can be stacked more easily using conventional stacking machinery than blocks of other shapes. -
[0048] Eachstack 70 is formed by a conventional stackingmachine 59 located downstream of theunmoulding station 55 and consists of, in this case, .eight layers of blocks arranged so that the blocks of each layer straddle the gaps between the blocks of the layer below. Thestack 70 is held together by means of four straps 72 which pass tightly around it to prevent the blocks moving apart. At the top and bottom of thestack 70, spaces are left between adjacent blocks to formchannels 74 into which the forks of a fork-lift truck can be inserted to move the stack. A stack formed in this way is entirely self-supporting and does not require a pallet or any other form of packing. -
[0049] Where such stacks are stored for some time before being transported, changes in ambient temperature may cause the blocks to contract and the straps 72 to loosen. It is therefore, preferred that each strap 72 should be left with an end free when initally placed on thestack 70 so that it can be pulled up and retightened immediately before moving thestack 70. -
[0050] The loose bottom plate of each compartment of themoulds 52 in which the blocks are formed is formed with two, as shown, or three equally-spaced transverse ribs of triangular cross-section which produce in the finished asphalt block correspondingly spaced, triangular cross-section grooves or indentations 80, as shown in Fig. 9. The ribs may either be formed integrally with the bottom plate of the mould or by positioning two pieces of angle iron on the base of the mould. -
[0051] The grooved blocks can be broken into even-sized pieces simply by tapping them sharply, thus causing the block to split cleanly in a controlled manner along the line of the grooves 80. Grooves 80 of various cross- sectional shapes may be used and provide satisfactory results. However, we have found that to enable the block to be broken cleanly, the groove depth should preferably be between one fifth and one third of the overall height of the block, the best results being obtained when the groove depth is about one quarter of the block height. So for a 0.5 metre long block of the dimensions described above, a groove depth of about 2.25cm (0.9 inch) is preferred. -
[0052] We have found that, for a 20kg block, the best results are obtained with grooves whose cross-section takes the form of a right-angled isosceles triangle, the sides of which are at least 1 to 16 inches (approximately 2.5-3.5cm) in length. Such grooves can easily be formed using suitably dimensional lengths of angle iron. Although it is possible to use, for example, a similarly-sized groove of equilateral triangle cross-section, blocks having such grooves are more difficult to release from their moulds than those having grooves of right-angled triangle cross-section. -
[0053] As will be seen from the above description, the method of the invention enables an improved mastic asphalt block to be manufactured more cheaply by making savings in both the energy consumed and the manufacturing time. Furthermore, the plant described above is almost completely automatic and can be operated by as few as two men who may be housed in a small air-conditionedcontrol cabin 90, shown in Fig. 2, thus avoiding the need for personnel to work in the unpleasantly hot areas around the heaters and mixers. In addition, the plant is very compact and, consequently, occupies relatively little space and it is envisaged that it could be erected on site in instances where large quantities of mastic asphalt will be needed.
Claims (36)
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at least some of the heat removed from the asphalt during cooling being recovered and re-used in heating the constituent materials of asphalt manufactured subsequently.