METHOD AND APPARATUS FOR THE MANUFACTURE OF CEMENTITIOUS SLAB PRODUCTS AND THE RESULTING PRODUCTS

Abstract: Cementitious products in form of either single-layer tiles or slabs or of blocks to be subsequently sawed in form of said slabs are prepared from a mixture of a granulated stone material having a selected particle size, and from a binding mix formed by cement, a quantity of between 0.25 and 0.36 parts by weight of water relative to the weight of cement, and a plasticizer for cementitious slurries, in which the quantity of binding mix added is slightly in excess of the quantity corresponding to the void fraction of the granulated material, by a method and apparatus which provide for the forming mould, containing a layer of predetermined thickness of the mixture, to be subjected to a first very short deaeration step under the effect of a very high vacuum and to a subsequent vibration step under a lower vacuum, after which the mould goes on to setting and hardening steps.

Description: "Method and apparatus for the manufacture of cementitious slab products and the resulting products" The present invention relates to artificial stone products in form of slabs or blocks consisting of a granulated stone material bound by means of a cementitious binding, useful for pavings and wall coverings. The invention also relates to a method and apparatus for their production. It is known that, for many centuries, natural stone materials such as marble, granite, etc. have been used in the form of slabs and panels both for pavings and for wall claddings. Natural stone materials are extracted from quarries in the form of blocks and the blocks are subjected to an operative cycle which provides for many operations and processes such as, for example, sawing, facing, polishing, etc. Alongside their unquestionable aesthetic properties and their equally undeniable mechanical properties, however, natural stone materials have some problems and disadvantages. In the first place every block extracted from a quarry differs, sometimes slightly, but also sometimes considerably from blocks extracted from the same quarry, so that it is not possible to produce floors or cracklings with large surface areas which do not have considerable aesthetic and/or colour differences. In the second place, even at the stage of the extraction of blocks from quarries, a considerable portion of the material excavated or extracted, for example, by blasting, remains unused or becomes unusable in the course of processing. By way of example, it may be mentioned that the percentage of the stone material excavated from quarries which is used, that is, which is sent in the form of blocks for subsequent processing does not exceed 20-30%, with obvious wastage which is not only disadvantageous from an industrial point of view but also constitutes a factor in environmental pollution and in the disfiguring of the landscape in the regions surrounding quarries. Attempts have been made in the past and are still being made today to use this resulting stone material (that is, the aforementioned 70% which is not used directly) in the manufacture of artificial stone products. In order to solve this problem several solutions have been proposed and practiced, which can be classified in two main groups or approaches. A first approach consists in the manufacture of so-called "terrazzo" cementitious products or tiles which are constituted essentially by granulated natural stone material dispersed in a cementitious matrix. The p-trticular method used for this product produces tiles which are very thick (particularly relative to the dimensions of the individual tiles) and consequently also heavy which, naturally, is disadvantageous with regard to their subsequent handling, particularly at the stage when the tiles are laid. 2 A "terrazzo" tile generally has dimensions of 40x40 cm (wαth thicknesses of no less than 3 5 cm) or 30x30 cm (with thickness of 2 7 cm) or other less commonly-used dimensions Moreover, their mechanical properties are relativeK poor In fact, the flexural strength (9 5-10 N/sq mm) and the abrasion resistance (560-580 cu mm ) values are certainly not high, whilst water absorbtion reaches 9-10% by weight A further disadvantage of this cementitious product lies in its appearance which reveals the presence of the cementiϋous binding in which the granulated mateπal is incorporated so that, from an aesthetic point of view, "terrazzo" tiles have never been held in great esteem and their widespread use is due mainly to their cheapness Each tile is produced individually by a method which provides for the followmg steps (1) a layer of a starting mixture or mix, constituted by (a) the inert granulated material reduced to the desired particle size beforehand, and (b) a cementitious binding formed by cement and water in which the percentage of water is decidedly m excess of the quantity normally necessary to achieve the binding effect, is spread on the base of a mould and subjected to slight vibration for several seconds, (2) a second layer of very lean cementitious binding barely moistened with water is placed on top of this first layer (which is intended to form the so-called visible face of the tile), (3) a pressure is applied over this second layer so as to force the excess water present in the first layer to be transferred into the overlying layer to make up its water percentage to values suitable for bnnging about the subsequent setting and hardening steps, (4) the product is extracted from the mould and is allowed to rest for the time necessary for setting to take place on tables or shelving where it is also left for the time necessary to complete the hardening step (usually about 25 days) With reference to the manufacturing of tiles or slabs, m more recent years, industrial investigations and developments have been carried out in relation to industrial methods in which a granular filler of stone material, usually the waste from the excavation of natural stone matenals, brought to a suitable particle size beforehand, is mixed in suitable proportions with a binding either of a cemenuuous nature or constituted by a setting synthetic resin The resulting mixture is subjected to a first forming step, for example, by the filling of suitable moulds or similar forming devices so as to form a layer of the desired thickness The mould or forming device is then subjected to a mechanical compaction operation (preferably by the action of a plate press) with the simultaneous apphcation of a vibratory motion, the mould being kept under vacuum Upon completion of this step, which lasts for a few minutes, a hardening step takes place in a manner which depends upon the nature of the binding More specifically, in the case of the cementitious binding, this is a conventional setting and subsequent hardening step for which the product is left to rest for the necessary time In the case of a binding constituted by synthetic resin, however, hardening takes place in a short time in the presence of a catalyst with the apphcation of heat, or cold by the joint action of a catalyst and a promoter This method is advantageous, not only because of its compatibility wαth modern industrial production standards but also, and above all. because it leads to decidedly more advantageous products Amongst the advantages it should be pointed out, in the first place, that it is possible to manufacture slabs of truly considerable dimensions much larger than those of "terrazzo" tiles and also larger than tiles or products made of natural stone materials In the second place, the resulting product has a completely homogeneous appearance so that it is possible to produce very large floors or external claddings for buildings In the third place, the mechanical charactenstics of the resultmg slabs are decidedly better than those of "terrazzo" tiles The second approach is that of the manufacturing of blocks having size comparable with that of the blocks obtained by excavauon from quarries, to be later sawed mto slabs In the common practice the manufacturing of blocks of stone materials has been and is practiced bj prevailingly usmg calcareous stone materials (since these materials, differently from siliceous matcnals like granite, can be easιl> sawed by means of tools bearing diamond insert segments) and Portland cement or more generally hydraulic bindings having a cementing function Unfortunately these blocks show the same disadvantageous features of the already mentioned cementitious products, smce in their production cement slurnes must be used containing water excess owing to the need of using fluid mixtures capable of readily filling the mterstices between the particles of granulated natural stone By the way the water excess with respect to the cement causes the mechanical properties of the products to be heavily lowered and moreover the slabs obtained from the blocks undergo diffused fissures caused by the alternated shrinkage and dilatation of the product, these phoenomena being increased by the excessive porosity of the product onginated by the evaporation of the too much excess water and by the reduced mechanical resistance of the product deπving from such an excess The filled m forms are subjected to vibrations applied to the base and or to the walls of the forms, in order to compact the slurry likewise a concrete casting The excess water causes the "bleeding" effect, namely the separation of water from cement, with a surface floating and (which is even more seπous) such a separation takes also place within the single mterstices wherein the interface between the binding mix and the surface of the particle of stone material sometimes consists of water only The use of plasticizing additives m this type of process is not much useful since the slum', although being more fluid, gams a plastic state hindering the deaeration of the mixture needed before the setting As a consequence products are obtamed filled with air bubbles which appear onto the surface of the slabs obtained by sawαng m form of holes haΛαng diameters vaπable from few thousandts of millimeter to some millimeters In the technical panorama relating to the manufacturing of blocks of stone mateπal. besides the above process, the US Patent 4,698,010 can be cited (wherein moreover other patents are summaπzed being part of the pπor art), therein a process is descπbed for the manufactuπng of blocks startmg from stone material of various particle size and from a binding, compnsing an initial mixing step in which stone mateπal, in form of powder and/or granulated, and a binding are mixed under vacuum, thereafter the mixture is transferred mto a form which is gι%'en an alternated motion to obtain an uniform and homogeneous distribution of the mixture wαthm the form,the latter, still remaining under vacuum, is then transferred into a chamber, also kept under vacuum, in which it is subjected to the action of a compacting press in combination with a vibratory motion of predetermined frequency The subsequent and final phase which is that of the setting and hardening, depends also in this case on the nature of the binding, namely on whether it is a hardenable resin or a cementitious binding, whereby the considerations already made with respect to these two types of binding still hold true, wαth the self evident differences determined by the size of the blocks Thus the mam subject of the present mvention is the production of products in which natural stone materials in granulated form and a cementitious binding are used, and which are not subject to problems of excessive unit weight or too great a thickness, or to the aesthetic disadvantages described briefly above with reference to known solutions In the production of the products constituting the subject set out above, the mam problem which has not been solved satisfactoπly up to now is that of the filling of the voids, that is, the empty spaces, which are created or remain between the particles of a granulated mateπal when it occupies a certain closed space or volume In fact, the greater the degree of filling, the closer the properties and also the appearance of the resulting cementitious product comes to a natural stone mateπal Now, if one takes the aforementioned closed volume or space containing a certain quantity of granulated mateπal, the nature, particularly the dimensions, of the voids or mterstices between the particles naturally depends upon the size of the particles, so that the void fraction, and hence the volume of the mterstices to be filled with the cementitious binding, also depends upon the particle size The cementitious binding in turn consists basically of cement powder and water There is a known quantity of water which is necessary so that the reactions which characteπze the settmg and hardening of a cement can take place However, this quantity of water is not sufficient to confer on the cement and water slurry even a minimal workability or fluidity so that, in normal techniques for the manufacture of cement products, the quantity of water added in the preparation of the slurry is m excess of that necessary for the hydration of the cement This excess in turn has to be the smallest possible excess consistent with the workability the mix since, in the final analysis, the excess water detracts from the compactness, and hence from the mechanical properties of the final cementitious product, the porosity of which is increased. With reference once more to the preparation of the product made of stone mateπal in granular form and cementiuous binding to which the present invention relates, if a cement and water slurry contauiing the quantity of water sufficient for the hydration of the cement were used to fill the voids, this slurry would be very dense and would have insufficient workability or fluidity to fill the interstices between the granules of inert stone mateπal by flowing. If, on the other hand, the optimal degree of filling were to be obtained, the initial water and cement slurry would have to contain an excess percentage of water, as mentioned above, to the detriment of the mechanical properties of the cementitious matrix of the final product and hence of the product itself In order to have a more precise idea of the values involved, it suffices to consider that a slurry which is almost ideal for producing a cement product having satisfactory characteristics and properties would have to have a water content of less than 0.315 parts by weight relative to the weight of cement, whereas the percentage of water in order to achieve satisfactory fluidity of the slurry such as to ensure a satisfactory degree of filling of the interstices of a granulated material would generally have to be greater than 0.55 parts by weight again relative to the weight of cement and, in this case, the mechanical properties of the final product would undoubtedly be poor It is precisely the contradictor}' nature of these two situations which led, in the pπor solutions mvestigated and implemented, in the case of "terrazzo" tiles, to the use of a mixture with a large excess of water in the cementitious slurry filling the voids of the granulated mateπal, with subsequent recourse to the measure of a second layer of a mixture lacking m water so as to balance the water content of the cementitious binding as a whole However, although this measure achieves an adequate degree of filling of the voids of the initial granulated mateπal, it is impossible to prevent the final product from having a very great thickness and weight relative to its dimensions and, moreover, from having at least mediocre mechanical properties Thus, before the present mvention, an industrially satisfactory solution to the problem had not been found Moreover, recent years, water reducing or plasUcizmg additives have come mto use for cementitious slurπes. with the purpose of conferring greater fluidity on slurries containing cement and water m the optimal ratio, s ce otherwise they are pasty and therefore not fluid With the present mvention, however, the optimal solution has been found for the production of cementitious products compπsmg a granulated natural stone matenal and a cementitious matπx filling the voids and the interstices of the granulated mateπal, the products having (1) in the case of slab product, thicknesses much less than those of directly comparable products of die pπor art havmg the same composition, and the case of blocks, the possibility of bemg sawed in form of big size slabs of thickness definitely less than that of the slabs which can be obtained by sawing from blocks produced according to the known art and directly comparable as havmg analogous composition, (n) excellent physical and mechanical properties, particularly porosity and flexural strength, of the same order as those obtainable by the most recent methods based on the vibratory compaction of mixtures of granulated material and cementitious binding under vacuum, (in) an appearance very similar to that of the natural stone mateπal from which the starting granulated material is formed, and (iv) dimensions also definitely larger than those of conventional Ules, for example of the "terrazzo" type In order to produce the product wαth the charactenstics mentioned above, the present invention consists of a method which provides for the followmg steps a) provision of a granulated matenal having a predetermined and controlled particle size and calculation of its void ratio or fraction, b) preparation of a water and cement binding mix havmg a water content of between 0 25 and 0 36 parts by weight relative to the weight of cement, preferably between 0 28 and 0 32 parts by weight, the binding mix bemg supplemented with a quantity of a known plasticizing additive for cementitious slurπes such that, when the mix is poured onto a surface in order to carry out the "mini slump test", it has a fluidity such that it is arranged in a very thin layer with a roundish shape having a diameter of about 20 cm and there is no apparent separation between the water and the cement with the deposition of the cement in the bottom of the mould and the appearance of the water on the surface, c) intimate mixing of the granulated mateπal and of a quantity of cementitious binding mix such as to be slightly in excess of the void fraction of the granulated mateπal, said mixing bemg earned out under vacuum when the product to be obtamed has a thickness not less than 5 cm, d) spreading of the resulting mixture in a mould or similar forming device to form a layer of the desired thickness, said spreading being effected under vacuum if the mixing has taken place under vacuum, e) application of a very high vacuum to the mixture contained m the mould for a peπod which is very short but long enough to bring about substantially complete deaeration of the mterstices and to remove all of any air rernaining incorporated in the startmg mixture, f) application for few minutes of a vibratory motion wαth a frequency of between 2000 and 4800 cycles/mm to the deaerated layer under a vacuum lower than that of previous step said vacuum bemg not lower than 80 mm Hg and tn the case of slabs having thickness not higher than 5 cm the application of the vibratory motion taking place for a peπod of at least 60 seconds, g) transfer of the mould to a settmg and initial hardening section, and h) removal of the product from die mould and keepmg of the product on shelves for final hardening In the case of products having thickness greater than 5 cm and more specifically of blocks said step (g) includes the permanence in said setting and initial hardening section for at least 8 hours and said step (h) compnses a first phase (hi) of initial hardening having a duration of about 7 days, in which the product is protected to avoid the water evaporation, and a second phase (h2) for the completion of the hardening for the necessary number of days, said hardening bemg earned out either on the block as such or on the slabs obtained from the block sawing at the end of the initial hardening phase (hi) In the foregoing definition, the expression "mini slump test" means the simplified form of the slump test according to the method defined by the UNI 9418 standards By way of illustration, it can be shown that if equal volumes of water and cement are mixed, a mixture or binding mix containing 0 32 parts by weight of water relative to the weight of cement is obtamed If one takes a granulated mateπal resultmg, for example, from the nulling of marble, wαth a particle size of between 0 1 and 6 mm, it has a void fraction of 26% by volume, so that this is the theoretical quantity of cementitious binding mix to be added The actual quantity of binding mix to be added in this case is mcreased to about 29% by volume Should it be desired to increase the quantity of cement binding mix for filling the mterstices, for example, if the void fraction were to increase, so that the quantity of mix would increase correspondingly, the possible use of inert mateπals in finely nulled form (for example, calcium carbonate) is foreseen, in order to keep the quantity of cement sufficiently low by replacmg some of it with an inert matenal Finally, it should be pointed out that other additives, for example, the usual cement dyes, may also be added to the cement and water binding mix, for example, when particular colour or decorative effects are sought With regard to the water reducing or plasticizing additive which improves the workability and hence the fluidity of the cementitious binding mix to be mixed wαth the granulated mateπal, these additives are well known in the art Examples of these additives are the so-called super plasticizers based on naphthalene sulphonic compounds, based on melairune. or based on acrylic polymers Among them there can be cited those obtained through copolvmeπzation of acrylic acid such as ' ERAFLUID 001"of the Italian company Breton Spa. "MAPEI FLUID X P404" of the Italian company Mapei Spa, "CHUUPOL APIO" of the Japanese company Takemoto or those havmg naphtalensulfomc base such as "REBUILD 2000" of this Swαss company Mac-Master, or lastly those havmg melamine basis such as "MELMENT 1 30" of the German Company SKW With regard, more specifically, to the individual steps of the method of the mvention as defined above, the first aspect which is worthy of more specific comment is that of the selection of the startmg granulated mateπal As already mentioned, one of the advantageous aspects of the present invention lies in the fact that waste stone mateπal such as that resultmg from operations to excavate blocks of natural stone matenal is fully reused If the starting granulated matenal is homogeneous and thus resulting from the same startmg stone mateπal, the optimal condition consists m the crushing and milling of the stone material to a maximum particle size no greater than 6 mm (although, in some cases, this maximum size may reach 8 mm) and the subsequent use of the granulated mateπal resultmg from the milling as it is (run of null) If, on the other hand, the starting granulated mateπal is not homogeneous, or if it is desired, for example, ra order to achieve particular colour or aesthetic effects, to mix stone mateπals of different oπgms and provenance, in this case, the composition of the starting granulated mateπal may be pre-arranged by the application of one of the usual formulae for calculating the composition and particle-size distnbution used in the field of cementitious products with reference to the inert component Examples of these formulae are Fuller and Thompson's formulae, or Bolomey's formula which are discussed, for example, in M Collepardi. Scienza e tecnologia del calcestruzzo, (Science and technology of concrete) pp 292-303, editor Hoeph Once the starting granulated matenal and its composition and particle-size distnbution have been identified, its avoid fraction can be calculated, for example, by formula 7 12 of the text indicated above The quantity of cementitious binding mix which is theoretically sufficient to fill the voids and mterstices can be identified upon the basis of this void fraction As already stressed in the definition of the method of the present mvention, the quantity of binding mix actually used wall be slightly in excess of this theoretical quantity, but this excess does not have to be such as to lead, upon completion of the method, to the formation of an independent layer constituted by cement alone on one of the two faces of the product In practice, the excess is normally of the order of 10% of the initial volume of cementitious binding mix related to the total volume of the mixture of granulated matenal and cementitious binding mix With regard now to the other steps of the method, these in the case of the direct manufactuπng of slabs provide, in the first place, for the pouring and/or spreading of a layer of the mixture of granulated mateπal and binding mix onto the base of a mould which may, for example, consist of a tray havmg the desired dimensions of the final slab This layer is spread m a thickness substantiall} corresponding to that of the final slab or product, m the prefened embodiment, this thickness will be of the order of 15- 20 mm, most preferably 17mm Once the mixture has been poured mto the mould, it is subjected to a forced deaeration step by the mtroduction of the mould into an environment under vacuum in which a high vacuum which should be no less than 40 mm Hg is formed This deaeration step should be very short and, in experimental tests it was found that it should preferably last no longer than 20 seconds Tins short duration is necessary owαng to the requirement to prevent the water from boiling wαth the formation of steam bubbles causmg imperfect compaction to the detnment of the final compactness and mechanical properties of the product Upon completion of the step of deaeration under a high vacuum, the mould contaimng the layer of mixture, now deaerated, is subjected to vibration at a predetermined frequency, with the mould still kept under a vacuum lower than that of the deaeration step and preferably of the order of 70-80 mm Hg. to prevent the water of the mix from boiling The duration of the vibration treatment under vacuum is of the order of a few tens of seconds, preferabl} about three minutes Although this remark should not be understood m a limiting sense, it seems plausible to consider that the apphcation of the vibration under vacuum to the deaerated mixture leads to a relative settling of the particles of granulated mateπal and to better copenetration or surface "closing" thereof ("closing" meaning that the surface of the product or slab has very small regions of cementitious binding in view) since the particles can perform microscopic movements without being obstructed by the friction which would obstruct the same settling thereof m the absence of the cementitious binding mix which thus also acts so as substantially to reduce friction, naturally as well as constituting the filling of the mterstices of the granulated matenal With regard to the method defined above, another aspect is worth noting, and that is the fact that setting and initial hardening occurs about 8 hours after the start of this step and complete hardening to an extent sufficient for the mechanical removal of the product from the mould generally occurs withm 24 hours In the case of the manufactuπng of products havmg thickness greater than 5 cm and particularly of blocks, the mixing takes place under a controlled vacuum so as to prevent in this phase the mixture, which subsequently fills the form, from contaimng air the removal of which, owing to the dimensions of the block and thus of the form, is very problematic and almost impossible with the known methods Moreover, wαth respect to the setting or hardenmg phase, it is to be observed that it includes first of all the maintaining at rest of the block, upon bemg extracted from the form, preferably m a wav to have it protected by an envelope of waterproof material such as to prevent the evaporation of water from the block to the surrounding atmosphere This phase has preferably a duration of at least 7 days and at this step it becomes possible to carry out the block sawαng the hardenmg bemg possibly continued on the thus obtained raw slabs, and possibh carrying out the other finishing operations With reference now to the apparatus for implementing the method of the present mvention, it compπses, as essential components (a) a raw mateπal stocking and supply section compπsmg a number of silos and hoppers for the stocking of the raw mateπals for the preparation of the starting mixture and corresponding devices tor the dosage of the single ingredients to a weighing equipment, (b) a mixing section compπsmg a mixer in which the ingredients coming from said weighing equipment together with water, water reducing or plasticizing additive and other possible additives are throughly mixed, (c) a section for the dosed and homogeneously uniform filling of at least one mould with the mixture formed in said mixer, (d) a combined section for the deaeration and settling of the mixture present m said at least one forming mould, compnsing first vacuum generating means adapted to have the surface of the mixture contained in said at least one mould subjected to a predetermined vacuum, means for controlling and regulating the vacuum acting onto said surface and vibration generating means adapted to apply to said mixture contained m said at least one mould a vibratory motion, havmg a frequency of between 2000 and 4800 cycles/nun , preferably 3000 cycles/mm and for a short time, preferably of the order of 4-5 nun , (e) a setting and imtial hardenmg section for the setting and initial hardenmg of the product contained in said at least one mold, said settmg and imtial hardenmg takmg preferably place at a temperature of between 25°C and 35°C, (f) a section for the removal of the product from said at least one mould and for maintaining at rest the product for the hardenmg phase According to the first embodiment of the above defined plant with reference to the manufacturing of slab products havmg thickness not greater than 5 cm and preferablv of the order of 13-20 mm, said at least one mould consists of a tray or preferably of a number of travs and said first vacuum generating means in said deaeration and settling combmed section compπse a vacuum bell shaped tank which can engage the entire surface of the tray or trays contaimng said mixture, and said control and regulating means for the vacuum generated in said bell shaped tank are adapted to generate firstly said high vacuum of a value not less than 40 mm Hg before said vibratory motion is applied and then said vacuum less high than the previous one, of the order of 70 to 80 mm Hg, duπng the phase of vibratory motion application According to the second embodiment of the above defined plant, and thus wαth respect to the manufactuπng of products having thickness higher than 5 cm and particularly of blocks, there are provided (bl) m said mixmg section second vacuum generating means owing to which said mixmg takes place under a controlled and regulated vacuum so as to prevent the water contained m the mixture from boiling, (cl) said filling section consists of a forming chamber communicating through valve means with the discharge of said mixer, said chamber bemg adapted to temporarily receive a form and being provided with means to render uniform and homogeneous the distnbution of said mixture m said form. (fl) m said removal and maintaining section means are provided for the protection, duπng a first peπod of the block bemg hardened against the evaporation of the water towards the surrounding atmosphere As regards the mixer, this is preferably of the type havmg parallel horizontal shafts bearmg radial arms. or it is of the orbital type with vertical shafts According to the preferred embodiment moreover, said mixer is fixed to the upper part of the forming chamber whicht, in turn, is preferably maintained under vacuum both duπng the transfer of the mixture from the mixer to the form and duπng the phase of vibratory motion application In turn the form is supported onto a saddle movable with an alternated translation motion, whereby the mouth of the form is alternatively moved m hoπzontal direction wαth respect to the above discharge orjening of the mixer and in this manner an uniform distnbution of the mixture withm the form is ensured As regards specifically the phase of application of the vibratory motion, according to a first embodiment of the plant of the mvention, the vibratory motion can be applied to die form supporting saddle withm the filling chamber Alternatively this step is effected in a second chamber, which is external with respect to the vacuum chamber in which the form is filled wαth the mixture prepared in the cited mixer, and m that case in said second chamber which is into commumcation with the first one through a vacuum tight door and is too maintained under a predetermined vacuum not higher than 70 mm Hg, the form is supported onto a plane havmg connected thereto means for the generation of vibratory motion of the desired frequency In the enclosed drawings the plant according to the present invention is partly shown m schematic view More specifically • fig 1 shows the plant scheme for the manufacturing of slab products, • fig 2 schematically shows the plant for the manufacturmg of block products accordmg to a first embodiment thereof, • fig 3 schematically shows a plant alternative to that of fig 2 and relating to a second embodimen,, • figs 4 and 5 specifically show the mixer for the mixture preparation Considering firstly fig 1 a general plant layout is shown, relating to the manufactuπng of slab products, compnsmg a section A for the stockmg and dosmg of the raw materials comprismg four silos. respectively A 1. A2, A3 and A4 , the first two of which are used respectively for the stocking of the granulated natural stone (0 1-0 3 mm) and of the powder of the same natural stone, whereas the silos A3 and A4 are used for the stockmg of white and grey cement (depending on the production requirements) References A 10, A 12 and A 14 indicate three hoppers, which are fed by means of a loading shovel A weighing and conveying band is fed from the silos Al and A2 as well as from the three hoppers whereas a dosmg and weighing unit A 16 is m direct communication wαth the cement stockmg silos A3 and A4 Al! the ingredients of the cementitious mixture, and therefor together with water and the other additives, among which mainlv the plasticizer additive, are fed to an epicycloidal mixer A 18 having a discharge channel A20 to convey the mixture coming out of the mixer to a section for the mould filling, geneπcally indicated by the reference B In the case of the manufactuπng of slabs and thus of products having thickness lower than 5 cm . by mould there is meant a tray havmg the desired depth which is filled wαth a dosed, uniformly distπbuted amount of mixture, and thereafter the trays are transferred to the section C m which the phases of deaeration and application of vibratory motion under vacuum are earned out To this end each tray is brought under a vacuum bell m which m a first phase a high vacuum is applied under the above mentioned conditions (at least 40 mmHg) and m the next step a vibration generating device is operated, the tray or mould bemg still maintained under a vacuum which however is less high than that of the first phase From section C the trays are transferred to a settmg and first hardenmg section D consisting of a number of chambers in which the trays are maintained at rest for a time of the order of 24 hours Preferably in the chambers of setting and first hardening an atmosphere heated to about 35°C is created. and more preferably these chambers are fed wαth steam so as to saturate the intemal environnment From the section D the trays containing the slab products are transferred to a unit E m which the slabs are removed from the trays and transfeπed to a hardenmg section F havmg a duration (as alreadv mentioned) of several days At the end of this phase the raw slabs are transferred to the standard operations of calibration, polishing and the like The trays from which the slabs have been removed are passed to a line for their cleaning, drying and spraying with a release agent, indicated on the whole by the reference G Turning now to fig 2 the part of the plant therein shown (the remaining parts being per se known) compπses a mixer 10 and a vacuum chamber 12. in which a form 14 is introduced, bemg supported onto the saddle 16. The saddle 16 is mounted on wheels 18, which are motor driven so that the saddle and therewαth the form 14 is alternatively moved in the direction of the arrows F, and Fj . In this manner, as clearly seen from the figure, the upper mouth of the form 14 is alternatively displaced between a first end position showτi in fig. 2 by full lines, and a second end position shown in fig. 2 by dashed lines. The chamber 12 is defined by a casing 20 which not only defines and encompasses the chamber 12, but is also provided wαth side openings, for the entry and exit of the forms, in a per se known manner, these openings being obviously provided wαth suitable tight closing means owing to the fact that a substantial vacuum must be established in the chamber 12 as already mentioned The mixer 10 too is maintained in a per se known manner under the same vacuum generated in the chamber 12 and preferably by connecting both the mixer and the chamber to the same vacuum source (net showαi). The mixer 10 is provided wαth a discharge channel 22 having check valve means for instance of the lock type, so as to control the discharge of mixture from the mixer within the form. In this embodiment the saddle 16 has connected thereto means for the vibratory motion generation, schematically represented by the reference 24, which are adapted to give to the plane 28 of the saddle 16 a vibratory motion and thus, through the form 14 abutting onto the saddle, to die mixture contained within the form. It is evident that the mixing action taking place in the mixer 10, owing to the fact that is is effected under vacuum, has also the function of deaerating the resulting mixture or, to say it better, to preλ'ent the mixture from incorporating air. As a matter of fact the size of the form and thus of the mixture therein contained would almost totally hinder the removal of the air as determined by the vibratory motion applied to die mixture. In the figures 4 and 5 an embodiment of the mixer 10 is shown, comprising two horizontal and parallel shafts 26 from which arms 30 radially protrude. Each shaft 26 rotates in the direction indicated by the arrows F 3 and F 4 respectively, the two shafts being driven by only one motor 33, by means of two reduction gears 32. Coming now to fig. 3 in which parts corresponding to those of fig. 2 are indicated by the same references, the form 14, once it has been homogeneously filled wαthin the vacuum chamber 12, is transferred to another vacuum chamber 34, in which the form is abutted onto a plane 36 rigidly connected to a vibratory motion generator 38. In this case too the vacuum acting in the chamber 34 is suitably controlled and regulated by connecting the chamber 34 to the same vacuum source operating for the chamber 12 and the mixer 10. Corning back to the manufacturing of slabs of a thickness less than 5 cm by the method and the apparatus according to the present invention it is possible to manufacture single-layer tiles (that is without a base layer) of marble-cement, granite-cement and other natural stone materials. The use of granulated mateπals resulting from the milling of artificial products such as ceramic mateπal can also be envisaged The resultmg tiles have a small thickness of the order of 13-20 mm, although thicknesses up to 40 mm can be achieved for certain requirements, and dimensions which may reach 600x600 mm or more The degree of fimshing of the resulting products is comparable to that of natural stone slabs and tiles since the usual sizing, grinding, chamfeπng and polishing treatments can be earned on the finished slabs Moreover, a suitable selection of the particle size of the startmg granulated matenal, enables the resulting aestlietic effect to be vaned Furthermore, an examination of a cross-section of a slab produced bv the method of the present mvention shows that the granulated mateπal is distπbuted homogenously throughout the thickness so that the slab is also characterized bv completely isotropic properties throughout its thickness as well as throughout its area With regard to the mechanical properties, the values given m the following table have been measured experimentally BINDING PORTLAND CEMENT PORTLAND CEMENT STANDARD White 525 Grey 450 Used AGGREGATE BOTTICINO MARBLE BOTTICINO MARBLE MAX DIM PARTICLE SIZE (mm) 6 45 6 45 SPECIFIC WEIGHT (kg/dm2) 250 250 2 50 250 UNI - 10444 FLEXURAL STRENGTH <N/mm2) 1450 1750 140 170 UNI - 10443 ABRASION RESISTANCE (mm2) 440 460 440 460 EN - 102 WATER ABSORPTION (% by weight) 250 250 250 250 UNI - 10444 After curing for 28 days The following examples descπbe the production of the cementitious products accordmg to the present mvention in non-limiting manner With regard to the additives added to the binding mixes, these are normal additives for cementitious slurπes for the functions indicated and the respective concentration ranges are given below dye 0-4% of the weight of the cement, plasticizer (active substance) 1 5-2 0% of the weight of the cement, deaeratmg agent (active substance) 04-0 6% of the weight of the cement, retardcr (active substance) 0 4-0 6% of the weight of the cement Example 1 Marble was milled producing "run of null" granulated matenal having the followmg particle-size composition 0 - 0 6 mm 8 2% by volume 0 6 - 1 2 mm 9 6% by volume 1 2 - 2 5 mm 17 5% by volume 2 5 - 4 0 mm 21 7% by volume 4 0 - 6 0 mm 15 5% by volume Water and white Portland cement were loaded mto a cement mixer in a manner such that the quantity of cement was equal to 13 7% by volume relative to the total volume of the final mixture and the water was equal to 13 85 by volume After the water and the cement had been mixed intimately, the granulated marble filler was added and the additives mentioned above were also added Sample slabs havmg dimensions of 40x40 cm and a thickness of 1 7 cm were then moulded, set and hardened under the conditions radicated above Example 2 The method of Example 1 was repeated with the use of a granulated marble havmg the followmg particle- size composition, calculated by the application of Bolomey's formula 0 - 0 045 mm (marble powder) 2 0% by volume 0 1 - 0 3 mm 8 0% by volume 1 2 - 2 5 mm 28 8% by volume 2 5 - 4 5 mm 32 50% by volume The mixture was prepared by the mixmg of the granulated mateπal of the aforementioned composition with a bmding mix of water and cement to mclude 14 3% by volume of white or grey Portland cement and 14 4% by volume of water, total, naturally as well as the additives already mentioned Example 3 The method of Example 1 was repeated with the use of granulated marble mateπal havmg the followmg particle-size composition 0 - 0 045 mm (marble powder) 2 0% by volume 0 1 - 0 3 mm 6 3% by volume 1 2 - 2 5 mm 8 6% by volume 4 0 - 6 0 mm 57 0% by volume The cement and water slurry was constituted by 13 0% by volume of white or grey Portland cement and by 13 1% by volume of water (total) In this case the particle-size selected clearly included a "jump" in particle-size Example 4 The method of Example 1 was repeated with granulated "run of mill" granite produced by the nulling of natural granite and having the followmg particle-size composition 0 2 - 0 6 mm 8 6% by volume 0 6 - 1 2 mm 12 5% by volume 1 2 - 2 5 mm 22 3% bv volume 2 5 - 4 mm 25 9% by volume 2 0% by volume of marble powder with a particle-size of 0 - 0,045 mm was added to this granulated mateπal The cementitious bradmg mix to which the granulated gramte was added compnscd 14 3% by volume of white or grey Portland cement and 14 4% by volume of water, total Example 5 Example 1 was repeated wαth granulated granite havmg a particle-size jump and having the followmg particle-size distribution 0 1 - 0 3 mm 6 0% by volume 1 2 - 2 5 mm 8 0% by volume 4 0 - 6 0 mm 56% by volume In this case also the granulated matenal was supplemented with 2 0% by volume of marble powder with a particle-size of up to 0 045 mm The water and cement mixture m turn compπsed 14 0% by volume of white or grey Portland cement and 14 0% by volume of water, total The physical and mechanical properties and charactenstics of the slabs manufactured m accordance with the examples given above were determined producmg the data given m Table 1 below, these data relating to slabs subjected to the customary 28 days curing TABLE l Type of formulation Specific weight Flexural streπght Abrasion resistance Water Absorption (kg.dm J ) UNI-104 4 (N mm 2 ) UNI-10443 (mm ^ EN-IO. (% by weight) UNI-10444 Example No 1 2 50 14 5 440 2 5 Example No 2 2 50 17 5 460 2 5 Example No 3 2 50 16 5 430 2 6 Example no 4 2 45 14 6 320 3 1 Example No 5 2 45 13 5 290 H 1 Block products, wluch afterwArds were sawed in form of slabs have been manufactured, by the process of the present invention and the related plant as illustrated by in non-limiting manner the followmg examples With regards to the additives, added to the bmding mixes these are again normal additives for cementitious slurnes for the functions radicated and the respective concentration raNges are the same given beforehand Example 6 Marble was milled producmg "run of null" granulated mateπal having the followmg particle-size composition 0 - 0 6 mm 8 4% by volume 0 6 - 1 2 mm 10 0% by volume 1 2 - 2 5 mm 17 5% by volume 2 5 - 4 0 mm 22 0% by volume 4 0 - 6 0 mm 15 5% by volume Water and white Portland cement were loaded into a cement mixer m a manner such that the quantity of cement was equal to 13 7% by volume relative to the total volume of the final mixture and the water was equal to 12 90% by volume After the water and the cement had been mixed intimately, the granulated marble filler was added and the additives mentioned above were also added The operations for the forming of blocks of the size 250x125 100 cm have been then earned out The blocks were sawed ra form of slabs 17 mm thick, which have been examined, both to detected possible porosity, both macroscopical and microscopical, and to determine the mechamcal properties of mterest for the final destination of the slabs Example 7 The method of Example 6 was repeated with the use of a granulated marble havmg the followmg particle- size composition, calculated by the apphcation of Bolomey's formula 0 - 0 045 mm (marble powder) 2 0% by volume 0 I - 0 3 mm 8 6% bv volume 1 2 - 2 5 mm 28 8% by volume 2 5 - 4 5 mm 31 9% by volume The mixture was prepared by the mixmg of the granulated mateπal of the aforementioned composition with a binding mix of water and cement to mclude 14 3% by volume of white or grey Portland cement and 14 4% by volume of water, total, naturally as well as the additives already mentioned Example 8 The method of Example 6 was repeated with the use of granulated marble mateπal havmg the followmg particle-size composition 0 - 0 045 mm (marble powder) 2 0% by volume 0 1 - 0 3 mm 6 3% by volume 1 2 - 2 5 mm 8 6% by volume 4 0 - 6 0 mm 57 0% by volume The cement and water binding mix was constituted bv 13 0% by volume of white or grey Portland cement and by 13 1% by volume of water (total) In this case the particle-size selected clearlv mcluded a "lump" ra particle-size Example 9 The method of Example 6 was repeated with granulated "run of null" granite produced by the millmg of natural granite and having the following particle-size composition 0 2 - 0 6 mm 8 6% by volume 0 6 - 1 2 mm 12 5% by volume 1 2 - 2 5 nun 22 3% by volume 2 5 - 4 5 mm 25 9% by volume 2 0% by volume of marble powder with a particle-size of 0 - 0,045 mm was added to this granulated mateπal The cementitious binding mix to which the granulated granite was added compnsed 14 3% by volume of white or grey Portland cement and 14 4% by volume of water, total Example 10 Example 6 was repeated with granulated gramte havmg a particle-size jump and having the followmg particle-size distribution 0 1 - 0 3 mm 6 0% by volume 1 2 - 2 5 mm 7 0% by volume 4 0 - 6 0 mm 56,3% by volume In this case also the granulated mateπal was supplemented with 2 0% by volume of marble powder with a particle-size of up to 0 045 mm The water and cement bmding mix ra turn compnsed 14 0% by volume of white or grey Portland cement and 14 0% by volume of water, total By detemung the physical and mechanical properties and charactenstics of the slabs manufactured from block produced according to the preceeding examples 6 to 10, data substantially comcident with those already reported in the previous table 2 are obtained It is worth to notice that this substantial coincidence is obtained when the slabs arc manufactured both from blocks undergoing the usual 28 days hardenmg and from blocks for which the hardening is earned out in a first phase wαth the block encompassed withm an envelope of water proof plastic material and in the next phase, after sawing by maintaining the slabs for 23 days ra a wet atmosphere From the above it is clear that the products of the present mvention, ra form both of slabs and of blocks, are therefore distinct from known cementitious products m composition, mechamcal properties and aesthetic properties

Claims: CLAIMS 1 Method of manufactuπng cementitious products compπsmg a granulated natural stone matenal and a cementitious matnx filling the voids and interstices of the granulated mateπal, providmg for the followmg steps a) the provision of a granulated matenal having a predetermined and controlled particle size and calculation of its void fraction, b) preparation of a water and cement binding mix having a water content of between 0 25 and 0 36 parts by weight relative to the weight of cement, thebmding mix being supplemented with a quantity of a known plasticizing additive for cementitious slurπes such that, when the slurry is subjected to the "mini slump" test it has a fluidity such that it is arranged in a very thin layer with a rounded shape havrag a diameter of about 20 cm, c) ratimate mixmg of the granulated matenal and of a quantity of cementitious slurrv such as to be slightly in excess of the void fraction of the granulated matenal, said mixmg bemg carried out under vacuum when the said cementitious product to be obtained has a thickness not less than 5 cm , d) spreading of the resulting mixture ra a mould or similar forming device to form a layer of the desired thickness, said spreading being effected under vacuum if the mixing has taken place under vacuum, e) application of a very high vacuum to the mixture contained ra the mould for a period which is very short but long enough to bring about substantially complete deaeration of the mterstices and to remove all of any air remaining incorporated ra the startmg mixture, f) application of a vibratory motion with a frequency of between 2000 and 4800 cycles per minute to the deaerated layer under a vacuum lower than that of step (e), saud vacuum bemg no lower than 80 mm Hg and in the case of cementitious products having a thickness not higher than 5 cm the apphcation of the vibratory motion taking place for a peπod of at least 60 seconds, g) transfer of the mould to a setting and imtial hardening section, and h) removal the product from the mould and keeping of the product on shelves for final hardening 2 Method according to Claim 1, characteπzed ra that the starting granulated mateπal is the product resultmg directly from the milling and granulation of natural stone matenal 3 Method according to Claim 1, characteπzed in that the starting granulated mateπal has a particle-size composition calculated according to the Fuller-Thompson formula or to Bolomey's formula 4 Method according to any one of Claims 1-4, characterized in that the starting granulated mateπal has a particle size of between 0 1 and 6 mm 5 Method according to Claim 1, characteπzed in that the water and cement bmding mix has a water content of between 0 25 and 0 36 parts by weight 6 Method according to Claim 1 , characteπzed ra that the excess of cementitious bradmg mix added to the granulated material in step (c) is 10%. 7. Method according to Claim 1, characterized in that the de-aeration by the application of a high vacuum is carried out with a vacuum of 40 mm Hg and for a period of 20 seconds. 8. Method according to Claim I, characterized in that the vibration step is carried out by the application of vibration at a frequency of 3000 cycles per minute and for a period of 4 - 5 minutes. 9. Method according to Claim 1 , characterized in that the starting granulated material is selected from granulated marble, gramte and ceramic material, milled to the desired particle size. 10. Method according to claim 1, characterized in that for the manufacturing of cementitious products having thickness higher than 5 cm. said mixrag step takes place under a controlled vacuum such as to prevent the water contained in the mixture from boiling. 11. Method according to claim 10, characterized in that said vacuum is not higher than 70 mm Hg. 12. Method according to claim 10, characterized in that said final hardening step (h) takes place in two phases, the first one (hi) of which has a duration of at least 7 days and takes place by maintaining the cementitious product being hardened in a condition protected from the evaporation of the water towards the surrounding atmosphere, whereas the second phase (tι2) takes place for the number of days necessary for the hardening completion. 13. Method according to claim 1, characterized in that said binding mix is added with inert material in finely milled form. 14. Method according to claim 13, characterized in that said inert material is added in substitution for part of the cement ingredient of said binding mix. 15. Method according to claim 13, characteπzed in that said inert material is calcium carbonate. 16. Plant for the manufacture of cementitious slab products from a mixture of a granulated stone material and of a binding mix of cement, water and a plasticizer for cementitious slurries, characterized in that it comprises: (a) a raw material stocking and supply section comprising a number of silos and hoppers for the stocking of the raw materials for the preparation of the starting mixture and corresponding devices for the dosage of the single ingredients to a weighing equipment; (b) a mixrag section comprising a mixer in which the ingredients coming from said wighing equipment together with water, water reducing or plasticizing additive and other possible additives are thoroughly mixed; (c) a section for the dosed and homogeneously uniform filling of at least one mould with the mixture formed in said mixer; (d) a combined section for the dearation and settling of the mixture present in said at least one forming mould, comprising first vacuum generating means adapted to have the surface of the mixture contained in said at least one mould subjected to a predetermmed vacuum, means for controlling and regulating the vacuum acting onto said surface and vibration generating means adapted to apply to said mixture contamed m said at least one mould a vibratory motion, having a frequency of between 2000 and 4800 cycles/minand for a short time, (e) a settmg and imtial hardening section for the settmg and initial hardenmg of the product contamed m said at least one mold, (f) a section for the removal of the product from said at least one mould and for maintaining at rest the product for the hardening phase 17 Plant according to claim 16, characterized m that in said section (d) said vibratory motion generating means generate a vibratory motion at a frequency of 3000 cycles per minute 18 Plant according to claim 16, characterized m that ra said section (e) said setting and initial hardenmg takes preferably place at a temperature of between 25°C and 35°C 19 Plant according to claim 16, characterized ra that for the manufactuπng of cementitious products having a thickness not greater than 5 cm said at least one mould consists of a tray and said first vacuum generating means ra said dearation and settling combined section compπse a vacuum bell shaped tank which can engage the entire surface of the tray or trays containing said mixture, and said control and regulating means for the vacuum generated in said bell shaped tank are adapted to generate firstly a vacuum not less than 40 mm Hg before said vibratory motion is applied and then said vacuum less high than the previous one, of the order of 70 to 80 mm Hg, dunng the phase of vibratory motion application 20 Plant accordrag to claim 19, characteπzed in that said at least one mould consists of a number of trays 21 Plant accordrag to claim 20, characteπzed m that said bell shaped tank is shaped so as to fully encompass the whole upper surface of said tray shaped mould 22 Plant according to claim 16, characterized m that said settmg and first hardenmg section compπses a number of chambers wherein said trays are maintained at rest for a time of the order of 24 hours 23 Plant accordmg to claim 22, characteπzed m that said chambers are fed with steam to saturate their intemal atmosphere 24 Plant according to claim 16, characteπzed ra that for the manufacturmg of cementitious products havrag thickness higher than 5 cm and particularly of blocks m said mixing section second vacuum generating means are provided whereby said mixing takes place under a controlled and regulated vacuum preventing the water contained ra the mixture bemg prepared from boiling 25 Plant according to claim 24, characteπzed m that said at least one mould is a form for the casting of cementitious products, said filling section consists of a forming chamber communicating through valve means with the discharge of said mixer and adapted to temporaπly receive said form 26 Plant according to claim 25, characteπzed said form in said filling section is supported onto a saddle movable with an alternated horizontal translation motion, whereby the mouth of the form is alternatively moved with respect to the discharge opening of said mixer between two end positions thus ensunng the uniform distnbution of said mixture withm said form 27 Plant according to claim 26, characteπzed m that said vibration generating means are connected to said form supporting saddle whereby said vibratory motion is applied to said saddle within said forming chamber provided in said filling section 28 Plant accordmg to claim 26, characteπzed m that a second foπn receiving vacuum chamber is provided after that provided ra said filling section, said second vacuum chamber bemg housed in said combined deaeration and settling section wherem said vibratory motion is applied to said form supporting means, the vacuum in said second chamber bemg controlled and regulated 29 Plant accordrag to claim 28. characterized in that said second vacuum chamber is connected to the same vacuum source operating for the said first vacuum chamber and for said nuxer 30 Slab product formed from a granulated stone mateπal and from a cementitious bmding phase, in the form of a single-layer tile and/or slab with a thickness of between 13 and 40 mm and havmg a homogeneous distribution of the granulated mateπal and of the bradmg phase, as produced by the method accordrag to any one of Claims 1-23

Inventors: TONCELLI MARCELLO, TONCELLI, MARCELLO
Applicants: TONCELLI MARCELLO, TONCELLI, MARCELLO
Application year: 1997
Main classification: B28B23
IPC codes: B28B1, B28B7, B28B23, B28C5, C04B28, C04B40