Patent Description:
It is well known that the production of ceramic products begins with the choice of raw materials, which generally include clay components of various mineralogical constitution to which inert materials and/or melting materials, such as quartz sand and feldspars, may eventually be added.

These ceramic raw materials are then subjected to a series of mechanical operations aimed at reducing their initial dimensions, in order to obtain a ceramic granulate with a determined average particle diameter and a particle size suitable for the product to be obtained.

The granulate thus obtained is then subjected to a forming step, for example by pressing, extrusion, casting or other processes, which makes it possible to obtain a semi-finished product having a certain geometric shape.

After possible decoration steps, this semi-finished product undergoes a firing step that transforms the raw materials of the granulate into new crystalline and/or glassy compounds, giving the product thus obtained particular chemical/physical properties, including the solidity and mechanical resistance necessary to maintain its shape.

As part of this general system, one of the most widespread techniques currently used to prepare ceramic granulate is the one involving wet grinding of the raw materials and subsequent spray drying thereof (atomization).

In particular, this technique requires that the raw materials are wet ground in special rotary mills until a liquid and viscous mixture is obtained, commonly called slip. The slip produced in this way is then introduced in special spray dryers, called atomizers, which are able to produce a homogeneous powder with constant humidity, called atomized, ready for the subsequent processing steps.

Another technique that is commonly used for preparing ceramic granulate is the one that includes a dry grinding of the raw materials and their subsequent agglomeration.

In particular, this technique provides that the raw materials are dry ground in special mills, possibly by successive reduction stages, until a micronized powder having an almost negligible degree of humidity is obtained. This ceramic powder is then subjected to an agglomeration step, for example through a wet granulation process, whereby the ceramic powder particles are made to adhere to each other to obtain larger particles or granules.

Specifically, the wet granulation process involves wetting the ceramic powder, previously obtained by dry micronization, and subsequent drying of the granulate thus obtained, in order to reach a predefined level of humidity suitable for the subsequent forming steps.

As an alternative to wet granulation with drying, suitable granulators have been devised which, thanks to extremely accurate systems for dosing the incoming micronized powder and for measuring the humidity level, are able to mix the particles of said micronized powder with a homogeneous and constant quantity of water and possibly water-soluble binders and/or additives, producing granules with a morphology similar to an agglomerate of fine particles, such as to increase the apparent density of the micronized powders and to facilitate the subsequent processing steps.

Compared to the wet grinding technique with slip atomization, the agglomeration of the micronized powder obtained by dry grinding has several advantages, including a marked reduction in electrical and thermal consumption, reduced greenhouse gas emissions, marginal water consumption and a strong reduction in the chemical additives normally used in the processing steps (e.g. deflocculants, tenacifiers or others). On the other hand, it is well known that agglomerated ceramic powders generally contain a higher percentage of air than an atomized one, which in many cases leads to greater difficulties in pressing both in terms of production and quality.

For example, the greater quantity of air can lead to: lower press output, higher raw waste, difficulty in obtaining large dimensions due to non-uniform distribution of the powder inside the mould cavity, surface defects caused by the presence of fine powder not properly agglomerated and with lower humidity than expected.

In an attempt to overcome these drawbacks, patent application <CIT> describes a process for granulating ceramic powder previously obtained by dry micronization, the objective of which is to produce a granulate with a reduced air presence, high fluidity and a reduced percentage of fine particles lower than <NUM> micrometres.

More specifically, this is a dry granulation process comprising a step of preparing the micronized ceramic powder, a step of compacting the micronized powder to obtain at least one compacted element, and finally a step of crushing the compacted element, to obtain a granulated material having a predefined particle size.

In particular, the process described in <CIT> envisages that the step of compacting the micronized ceramic powder is performed using only a compression action, during which the ceramic powder is subjected to a pressure value not lower than <NUM>/cm<NUM>.

However, the pressure value to which the micronized ceramic powder must be subjected, in order to ensure an adequate level of quality and effectiveness of the compaction step, is not a constant but depends on many characteristics of the powder, including particle size, apparent density and the degree of cohesion of the specific raw materials that make it up.

In several cases it may therefore happen that the above mentioned peculiar characteristics imply the need to exert a very high compaction pressure, higher than <NUM>/cm<NUM>, which drastically reduces the production capacity and efficiency of the compaction step, increasing at the same time the quantity of waste product that is not properly compacted. <CIT> discloses a process for preparing a ceramic granulate.

An object of the present invention is to overcome or at least significantly reduce the aforementioned drawback of the prior art, by making available a solution that allows efficient granulation of dry ground ceramic powders, while using lower compaction pressures than those required to implement the method described in <CIT>.

A further object of the present invention is to achieve the above-mentioned objective within the scope of a simple, rational and relatively low cost solution, which can also be flexible and adaptable to the various peculiar characteristics that micronized ceramic powders may present depending on a different composition of the raw materials. These and other objects are reached thanks to the characteristics of the invention as set forth in the independent claims. The dependent claims outline preferred and/or particularly advantageous aspects of the invention but not strictly necessary for the implementation thereof.

The invention makes available a process for preparing a ceramic granulate according to claim <NUM>.

Thanks to the aforementioned wetting step, it is advantageously possible to increase the humidity and density of the dry ground ceramic powder, obtaining an agglomerated product which can be effectively compacted using a comparably lower compaction pressure than the one that would be required to compact the same ceramic powder under a dry condition.

As a result, the wetting step significantly increases the production capacity and the efficiency of the compaction step, at the same time decreasing the quantity of waste product that would otherwise not be adequately compacted.

The introduction of this wetting step therefore allows the process according to the invention to obtain a ceramic granulate with reduced presence of air and high flowability as part of a more efficient and productive solution than the prior art represented by patent application <CIT>.

According to an aspect of the present invention, the ceramic raw materials from which the starting ceramic powder is obtained may comprise at least one clay component or a plurality of clay components having a different mineralogical constitution.

In this way, by varying the number, type and/or percentage quantities of each clay component, it is advantageously possible to produce ceramic granulates with different characteristics, for example according to the specific ceramic product to be made. According to another aspect of the invention, the ceramic powder obtained from the grinding step may possess one or more of the following characteristics:.

Each of these features has the advantage of making the subsequent processing steps more effective, allowing to obtain a ceramic granulate characterized by a further reduced presence of air and optimal flowability.

In addition, the particle size spectrum indicated above also has the advantage of favouring sintering processes during the firing step of ceramic products.

Of course, within the ranges provided, the values of the various characteristics may vary.

For example, the particle size spectrum may vary depending on the characteristics of the raw materials, the characteristics of the subsequent processing steps and the type of product to be made.

The apparent density may similarly vary depending on the characteristics of the raw materials and the desired particle size.

According to another aspect of the invention, the liquid substance used in the wetting step may include water and possibly water-soluble binders and/or additives (e.g. CMC, starch, lignite, boric acid, SIL60, etc.), which are preferably in quantities lower than <NUM>% of the total weight of the solution.

The use of a water-based solution has the advantage of increasing the cohesion of the ceramic powders, while limiting the environmental impact of the process.

Another aspect of the invention provides that the agglomerated product obtained by the wetting step may possess one or more of the following characteristics:.

Each of these features has the advantage of making the subsequent compaction step, and therefore the entire process, more effective and productive.

According to one aspect of the present invention, the compaction pressure that is applied to the agglomerated product during the compaction step may be lower than or equal to <NUM>/cm<NUM>, for example comprised between <NUM> and <NUM>/cm<NUM> (extremes included).

In this way, the compaction step can be carried out by means of technical equipment and in a relatively simple way, which makes it particularly efficient and productive. According to a preferred aspect of the invention, the process may further comprise at least a step of sieving the ceramic granulate in order to separate from the same the coarse particles, i.e. particles having a maximum dimension (e.g. diameter) greater than a predetermined value, for example greater than <NUM> micrometres.

Thanks to this solution, it is advantageously possible to supply a ceramic granulate having a relatively narrow particle size spectrum and few coarse particles.

In this context, one aspect of the invention provides that the process may further comprise a step of reconveying said coarse particles to the crushing step.

In this way, coarse particles that do not meet the required specifications can be efficiently returned to the production cycle, reducing production waste.

According to the invention, the process also comprises a step of inertial separation of the ceramic granulate in order to separate from the same the fine particles, i.e. particles having maximum dimensions (e.g. diameter) lower than a predetermined value, for example lower than <NUM> micrometres.

Thanks to this solution it is advantageously possible to supply a ceramic granulate with a low presence of fine particles.

In this case, one aspect of the invention provides that the process may further comprise a step of reconveying said fine particles to the wetting step, for example by first combining them with ceramic powder.

In this way, fine particles that do not meet the required specifications can be efficiently returned to the production cycle, reducing production waste.

In general terms, one aspect of the present invention provides that the ceramic granulate obtained by the process outlined above may possess one or more of the following characteristics:.

Each of these characteristics has the advantage of making ceramic granulate particularly suitable for use in the production of ceramic products, mainly through the usual forming (e.g. pressing, extrusion, casting, etc.) and firing steps.

Another embodiment of the present invention finally makes available a plant for preparing a ceramic granulate, which comprises:.

This embodiment achieves essentially the same advantages as the corresponding process, in particular that of increasing the efficiency of the compaction step and consequently the productivity of the entire system.

All ancillary aspects of the invention, which have already been outlined in relation to the process, are of course also applicable mutatis mutandis to the corresponding plant.

In particular, the plant may comprise means for sieving the ceramic granulate, placed downstream of the crushing means, to separate the coarse particles from the ceramic granulate, i.e. particles having a maximum dimension (e.g. diameter) greater than a predetermined value, for example greater than <NUM> micrometres, as well as possible means for reconveying said coarse particles back to the crushing step.

The plant may also comprise means for inertial separation of the ceramic granulate, placed downstream of the crushing means and possibly of the sieving means, to separate from the ceramic granulate the fine particles, that is particles having maximum dimensions (e.g. diameter) lower than a predetermined value, for example lower than <NUM> micrometres, as well as possible means for reconveying said fine particles to the wetting step, for example by previously combining them to the ceramic powder.

Further features and advantages of the present invention will become more apparent from the description of a preferred, but not exclusive, embodiment of a process and a plant, illustrated only by way of non-limiting example in the accompanying drawings, in which:.

With particular reference to the aforementioned figures, a process for preparing a ceramic granulate particularly suitable for preparing ceramic products such as slabs and/or wall and floor tiles, as well as a plant <NUM> especially suitable for implementing the aforementioned process are described below.

In this regard, however, it should be specified that the process could also be implemented with plants <NUM> different from those illustrated in the figures.

The process first involves preparing a mix of ceramic raw materials.

This mix of ceramic raw materials may comprise at least one clay component or a plurality of clay components having a different mineralogical constitution.

For example, each of these clay components may be chosen from the arrangement consisting of: kaolinite clay, illite clay, montmorillonite clay and chlorite clay.

By varying the number, type and/or percentage quantities of each clay component, it is advantageously possible to produce a ceramic granulate with different characteristics, for example according to the specific product to be made.

In general, the percentage by weight of the clay component in the raw material mix can vary in the range comprised between <NUM>% and <NUM>% (extremes included), for example by taking into account the characteristics of the subsequent processing steps and the type of ceramic product to be made.

The mix of ceramic raw materials may possibly also include inert materials and/or melting materials, such as quartz sand and feldspars.

This does not exclude the recovery of secondary raw materials (processing waste and powder recovery from the filtering systems), the presence of which can vary in the range comprised between <NUM>% and <NUM>% (extremes included), for example by taking into consideration the characteristics of the subsequent processing steps and the type of ceramic product to be made.

This mix of ceramic raw materials is then subjected to a dry grinding step, aimed at reducing the dimensions thereof, until a ceramic powder P is obtained, for example a micronized ceramic powder, i.e. with particles having an average dimension lower than <NUM> micrometres.

It should be here specified that, in the context of the present discussion, the dimension of a particle or of a granule is generally intended as its maximum linear dimension, which can be, for example, assimilated to the maximum diameter in the case of substantially spherical particles/granules or to the greater diagonal in the case of substantially prismatic particles/granules.

In particular, the ceramic powder P obtained at the end of the grinding step may include a quantity of particles having dimensions lower than <NUM> micrometres greater than or equal to <NUM>% of the total weight of the ceramic powder P, for example greater than or equal to <NUM>% of said total weight.

Particles having dimensions comprised between <NUM> micrometres and <NUM> micrometres (extremes included) may be present in the ceramic powder P in a weight percentage comprised between <NUM>% and <NUM>% of its total weight (extremes included).

The ceramic powder P may possibly also contain particles having dimensions higher than <NUM> micrometres but in smaller and generally decreasing percentages.

In particular, the ceramic powder P may contain a quantity of particles having dimensions comprised between <NUM> and <NUM> micrometres (extremes included) comprised between <NUM>% (absence) and <NUM>% (extremes included) of the total weight.

Further, the ceramic powder P may be substantially free of particles having dimensions greater than <NUM> micrometres.

A specific example of the particle size distribution of ceramic powder P is given in Table <NUM> below:.

Within the values indicated above, the particle size spectrum of the ceramic powder P may vary depending on the characteristics of the raw materials, the characteristics of the subsequent processing steps and the type of product to be made.

The ceramic powder P obtained at the end of the dry grinding step may also have an apparent density comprised between <NUM> and <NUM>/cm<NUM> (extremes included).

It should be here specified that the apparent density of a granular or powdered material represents the density of such material considering also the inter- and intra-particle spaces. It may be calculated as the ratio between the mass of a quantity of said granular or powdered material and its apparent volume, e.g. the volume that said quantity of material occupies when it is poured slowly and without compression into a graduated container.

This parameter may also vary, within the expected range, depending on the characteristics of the raw materials and the desired particle size.

Finally, the ceramic powder P obtained at the end of the dry grinding step may have a humidity lower than or equal to <NUM>%, for example comprised between <NUM>% and <NUM>% (extremes included).

It should be here specified that, in the context of this discussion, humidity of a material refers to the percentage by weight of water contained in a sample of that material, compared to the total weight of the sample.

This percentage can then be calculated using the following formula: <MAT> where P is the total weight of the sample and P' is the weight of the same sample after a step of complete dehydration.

In order to perform the dry grinding, the plant <NUM> may comprise a single grinding apparatus or a sequence of grinding apparatuses suitable for subjecting the ceramic raw materials to a progressive dimension reduction, for example a pre-crushing, a crushing and finally a micronization.

At least the final portion of the dry grinding step, such as micronization, may be performed by means of a mill, such as a peg mill, a rotary ring mill, a pendular mill, a vertical roller mill, or a discontinuous or continuous cylindrical ball mill.

All of these mills are per se known and are therefore neither illustrated nor described in detail.

However, it should be specified that, in some embodiments, the grinding apparatuses may belong to a plant that is separate and independent of the plant <NUM>, which may simply receive the already dry ground ceramic powder P as an input.

In any case, the dry grinding step is performed by loading and grinding the ceramic raw materials inside the grinding apparatuses, without adding water or other liquid substances.

In this way, the only humidity that may be present during the grinding step is that intrinsically contained in the ceramic raw materials.

In order to obtain the above-mentioned humidity values, it is preferable that the ceramic raw materials are already sufficiently dry before subjecting them to the dry grinding (micronization) step.

In the presence of significant humidity in the raw materials, it is possible to include a step of drying the ceramic raw materials, to be carried out before the dry grinding step, for example through natural drying methods (solar evaporation) or forced drying through dryers.

In the presence of raw materials with low/medium plasticity and a modest humidity content, it is also possible to install heating systems, such as burners and/or heat recovery systems, directly inside the grinding apparatuses, so as to allow simultaneous drying and grinding (micronization) of the aforementioned raw materials.

Optionally, one or more powder binders (for example boric acid, FP590, etc.), obtained at the end of the dry grinding step, may be subsequently added to the ceramic powder P preferably in quantities lower than <NUM>% by weight, having the purpose of increasing the cohesion between the raw materials.

After the possible addition of the aforementioned powder binders, the ceramic powder P obtained at the end of the dry grinding (micronization) step is subjected to at least one wetting step with a liquid substance.

This wetting step can be achieved by mixing, preferably uniformly, a dosed and calibrated quantity of said liquid substance into the ceramic powder P.

The liquid substance may include water and possibly water-soluble binders and/or additives (e.g., CMC, starch, lignite, boric acid, SIL60, etc.), preferably in quantities lower than <NUM>% by weight.

By means of the wetting step of the ceramic powder P, an agglomerate A is obtained, which generally has a higher humidity, and possibly a higher apparent density and/or an average larger particle size, than the initial ceramic powder P.

In particular, the humidity of the agglomerated product A obtained at the end of the wetting step may be comprised between <NUM>% and <NUM>% (extremes included).

The relative density of the agglomerated product A may be comprised between <NUM> and <NUM>/cm<NUM> (extremes included).

As regards particle size, the agglomerated product A obtained at the end of the wetting step may include a quantity of particles having dimensions lower than <NUM> micrometres comprised between <NUM>% and <NUM>% (extremes included) of the total weight of the agglomerated product A.

Particles having dimensions comprised between <NUM> micrometres and <NUM> micrometres (extremes included) may be present in the agglomerated product A in a percentage by weight comprised between <NUM> % and <NUM>% of its total weight (extremes included).

The agglomerated product A may also contain particles having dimensions higher than <NUM> micrometres in smaller but not entirely negligible quantities.

In particular, the agglomerated product A may contain a quantity of particles having dimensions comprised between <NUM> and <NUM> micrometres (extremes included) comprised between <NUM>% and <NUM>% of the total weight (extremes included).

In addition, the agglomerated product A may contain particles having dimensions greater than <NUM> micrometres in a quantity comprised between <NUM>% and <NUM>% of the total weight (extremes included).

Table <NUM> below shows an example of particle size distribution of the initial ceramic powder P and an example of particle size distribution of the agglomerated product A obtained after the wetting step:.

To perform the wetting step, the plant <NUM> may comprise an apparatus <NUM> for humidifying and densifying the ceramic powder P to obtain the agglomerated product A, a preferred embodiment of which is illustrated in <FIG>.

This humidification and densification apparatus <NUM> may comprise means for feeding <NUM> the ceramic powder P and a dosing device <NUM> for the calibrated dosing of the liquid substance to the ceramic powder P.

The feeding means <NUM> may comprise a weighing belt <NUM>, which is adapted to receive ceramic powder P from a variable speed star extractor <NUM>, placed for example at the outlet of a storage hopper <NUM>, so as to convey a duly calibrated flow of said ceramic powder P to the dosing device <NUM>.

The dosing device <NUM> may comprise a multistage pump <NUM>, which is adapted to withdraw the liquid substance from a tank <NUM> (see <FIG>) and introduce it towards a series of superimposed discs <NUM> that distribute the sprayed liquid substance into the flow of ceramic powder P falling towards the bottom of the dosing device <NUM>.

The ceramic powder thus humidified is then collected on the bottom of the dosing device <NUM>, which preferably has a conical conformation with a vertical axis and concavity facing upwards, where it agglomerates giving rise to the agglomerated product A. Finally, the dosing device <NUM> comprises one or more scrapers <NUM>, which may be placed on the inclined surface of the conical bottom and lead the agglomerated product A to discharge.

However, alternative means for feeding, for example by means of variable speed auger feeds, as well as alternative means for humidifying and densifying the ceramic powders, for example by means of vertical and/or horizontal wetting machines having a central shaft with vanes and/or tools for suspending the ceramic powder P and spraying systems by means of specific high-pressure nozzles, are not excluded.

Optionally, the agglomerated product A obtained at the end of the wetting step may be subjected to a further densification step, especially in the cases where the agglomerated ceramic powders have an apparent density lower than <NUM>/cm<NUM>.

The densification step can be carried out by using compacting rollers on a belt that are used at low pressure.

After this possible densification step, the agglomerated product A obtained at the end of the wetting step is subjected to a compaction step, during which the same is subjected to a certain compaction pressure, so as to obtain one or more compacted elements C (for example, but not necessarily one or more briquettes).

The compaction pressure that is applied to the agglomerated product A during this step may be lower than or equal to <NUM>/cm<NUM>, for example comprised between <NUM> and <NUM>/cm<NUM> (extremes included).

Within this range, the compaction pressure may vary depending, for example, on the degree of cohesion of the raw materials, the particle size and apparent density characteristics of the ceramic powder P, and the quantity and characteristics of the liquid substance with which said ceramic powder P was wetted.

In particular, the quantity and characteristics of the aforesaid liquid substance (e.g. quantity and type of binders) should preferably be chosen and calibrated, during the previous wetting step, precisely so that the compaction pressure required to obtain the compacted elements C is lower than or equal to <NUM>/cm<NUM>.

In this way, the compaction step can be carried out by means of technical equipment and in a relatively simple way, which makes it particularly efficient and productive.

For example, to perform this compaction step, the plant <NUM> may comprise compaction means <NUM>, a preferred embodiment of which is illustrated in <FIG>.

Said embodiment provides two parallel and mutually counter-rotating pressure rollers <NUM>, each of which has a side surface <NUM>, generally cylindrical, which is flanked and opposed to the side surface <NUM> of the other roller <NUM>.

The side surfaces <NUM> of the two rollers <NUM> may be shaped, so as to present a plurality of recesses (not visible) capable of substantially defining tiles.

The agglomerated product A is dispensed between the side surfaces <NUM> of the two rollers <NUM>, for example by an auger hopper <NUM>, so as to be compressed within said recesses and obtain the compacted elements C.

In other embodiments, however, the side surface <NUM> of the rollers <NUM> may be smooth or knurled.

The compaction means <NUM> may further be associated with a cleaning system <NUM> adapted to emit jets of compressed air on the side surface <NUM> of the rollers <NUM> to ensure cleaning thereof.

Finally, it is not excluded that, in other embodiments, the compaction means may comprise one or more compacting rollers placed on a belt, parallel compaction belts, compaction systems by means of rotating rollers placed on tables or tracks provided with a die, rotating tables or tracks provided with a die with fixed compaction rollers, mechanical or hydraulic presses provided with a mould.

Subsequently, the compacted elements C obtained as a result of the compaction step are subjected to a crushing step, during which they are crushed so as to obtain a ceramic granulate G with a predefined particle size.

To perform this crushing step, the plant <NUM> may comprise crushing means <NUM>, a preferred embodiment of which is illustrated in <FIG>.

The crushing means <NUM> according to this embodiment may comprise at least one hammer mill, by means of which the compacted elements C are crushed to a desired particle size.

The hammer mill generally comprises an outer casing <NUM>, within which a rotatable rotor <NUM> is housed to which articulated hammers <NUM> are associated that are adapted to contact and crush the compacted elements C.

The hammers <NUM> may have various conformations and shape and the rotor <NUM> may be provided with clockwise or counterclockwise rotation.

However, it is not excluded that, in other embodiments, the crushing means <NUM> may include other types of mills, such as disc mills, opposing roller mills or peg mills.

In order to avoid clogging of the crushing means <NUM>, caused by the humidity in the compacted elements C, the process may also comprise a step of heating thereof.

This heating step may be performed by providing the crushing means <NUM> with a heating system <NUM> adapted to heat the outer casing <NUM> of the mill, for example of the mill illustrated in <FIG> or any of the other mills mentioned above.

This heating system <NUM> may comprise, for example, electrical resistances applied to said outer housing <NUM>.

However, it is not excluded that, in other embodiments, the aforesaid heating step may be obtained with other means, for example by introducing hot air inside the mill or by introducing hot air, liquids and/or oils in a suitable cavity between the outer casing <NUM> and an inner casing.

After the crushing step, the process comprises subjecting the granulate G thus obtained to a sieving step with a sieve, so as to separate therefrom coarse granules S1 having dimensions greater than a first predetermined value. This first value may be for example but not necessarily equal to <NUM> micrometres.

To perform this sieving step, the plant <NUM> comprises sieving means <NUM>, a preferred embodiment of which is illustrated in <FIG>.

Such sieving means <NUM> may comprise a sieve provided with a sieving mesh <NUM>, preferably but not exclusively made of stainless steel, and possibly with a vibrating device <NUM> suitable for vibrating the sieving mesh <NUM>, preferably but not necessarily at an adjustable frequency and intensity.

The sieving mesh <NUM> may be oriented at an angle with respect to a hypothetical horizontal plane.

The vibrating device <NUM> may comprise one or more electromagnets mechanically connected to the sieving mesh <NUM>, either directly or indirectly.

The granulate G is poured above the sieving mesh <NUM>, so that the coarse granules S1, not being able to pass, flow on the sieving mesh <NUM> towards a first discharge mouth <NUM>, while the finer granulate V, crossing the sieving mesh <NUM>, reaches a second and distinct discharge mouth <NUM>.

In order to avoid clogging of the sieving mesh <NUM>, caused by the humidity in the granulate G, the sieving mesh <NUM> can also be heated by means of a suitable heating system, for example by means of electrical resistances fixed in a heat exchange relationship with the sieving mesh <NUM>.

The sieving mesh <NUM> may further be provided with a cleaning device <NUM>, comprising for example one or more brushes, which may be operated in a timed manner so as to clean the sieving mesh <NUM> of material residue.

In general, the sieving means <NUM> may however comprise any other type of sieve, including for example circular sieves, inclined sieves with vibrators and/or electromagnets placed laterally, anteriorly or posteriorly which directly or indirectly stress the sieving mesh, tumbler sieves, rotary sieves.

In any case, the granulate V that pass through the sieving mesh <NUM> (reaching, for example, the second discharge mouth <NUM>) will be made up only of granules having dimensions smaller than the set value (and defined by the mesh dimensions of the sieving mesh), while the granules that are separated and retained by the sieving mesh (reaching, for example, the first discharge mouth <NUM>) represent the coarse granules S1.

These coarse granules S1 may possibly be recovered and conveyed back to the crushing step, for example by feeding them to the inlet of the crushing means <NUM> together with the compacted elements C coming from the compaction step, so as to reduce production waste.

After this sieving step, the sieved ceramic granulate V (i.e., the one purged of coarse granules S1) is further subjected to an inertial separation step, so as to separate therefrom fine particles S2 having dimensions smaller than a second predetermined value.

Of course, this second value is preferably lower than the first value used in the sieving step.

By way of non-limiting example, the second value may be equal to <NUM> micrometres. To perform this inertial separation step, the plant <NUM> comprises separation means <NUM>, a preferred embodiment of which is illustrated in <FIG>.

These separation means <NUM> comprise a multiple cross-flow inertial separation device, which comprises an outer casing <NUM> within which the sieved ceramic granulate V flows by gravity, from top to bottom, from an inlet mouth <NUM> to an outlet mouth <NUM>.

A plurality of chutes <NUM>, preferably having an adjustable inclination, are arranged inside the casing <NUM>, which are arranged alternately and distributed substantially in a herringbone pattern along the direction of descent of the sieved ceramic granulate V. At the same time, an air current is created inside the casing, flowing from the bottom to the top, hitting in counter-current the sieved ceramic granulate V that flows down along the chutes <NUM>.

This air current can be generated by a suitable suction device <NUM> (see <FIG>).

In this way, the larger and heavier granules of the sieved granulate V continue to fall along the separation device, reaching the outlet mouth <NUM>, while the smaller and lighter granules are dragged upwards by the air current and transported by the latter inside a tank <NUM> associated with the suction device <NUM>.

The ceramic granulate that reaches and flows out of the outlet mouth <NUM> represents the finished granulate GF.

The inertial separation device can vary in the number of stages, the angle of the curves, the internal speeds and the air/product ratio, in order to be able to adjust the percentage of residual fine particles (having dimensions lower than the second predetermined value) in the finished granulate GF.

However, it is not excluded that, as an alternative to the device illustrated in <FIG>, separation means <NUM> of other embodiments may comprise other types of inertial separators, for example pneumatic type separators, cyclonic type separators, gravity type separators or pneumatic vibrated fluidised bed type separators.

In any case, the fine granules S2 that are separated during the inertial separation step (and that accumulate, for example, in the tank <NUM>) can be recovered and conveyed back to the wetting step, for example by previously combining them to the ceramic powder P at the inlet of the humidification and densification apparatus <NUM>, thereby further reducing production waste.

As mentioned above, the ceramic granulate GF, also purged of fine granules S2, constitutes the finished ceramic granulate and is generally characterised by low air content, high flowability, homogeneous humidity, a narrow particle size and a low percentage of fine particles.

It should be here noted that although reference was made in the foregoing discussion to an inertial separation step following the sieving step, in other embodiments, the inertial separation step could be performed prior to the sieving step.

It is also not excluded that certain embodiments may involve only the sieving step or only the inertial separation step or possibly neither of them.

In any case, it is preferable that the finished ceramic granulate GF (i.e. obtained from the crushing step preferably followed by the sieving step and/or by the inertial separation step) may have at least one of (preferably more than one or all of) the following characteristics:.

The compression ratio is the ratio between the apparent volume of the granulate and the apparent volume of the compacted material obtained after the pressing step.

The above mentioned characteristics of ceramic granulate GF are summarized in Table <NUM> below:.

An example of particle size distribution of ceramic granulate GF is shown in detail in Table <NUM> below:.

A more specific example of ceramic granulate GF, obtainable from the above process, may have at least one of (preferably more than one or all of) the following characteristics:.

These data are also shown comparatively in Tables <NUM> and <NUM> below:.

In particular, Table <NUM> shows the values of the compression ratio, apparent density, angle of repose and humidity of the example of ceramic granulate GF obtainable by the above process, comparing them with those relating to a granulate obtained by means of the dry process described in <CIT> and with those relating to an atomized one obtained by wet grinding.

Table <NUM> shows the particle size distribution of the example of granulate GF obtained with the process outlined above, comparing it with the particle size distribution of the granulate obtained by means of the dry process described in <CIT> and with that of the atomized one obtained by wet grinding.

As mentioned in the introduction, the ceramic granulate GF, obtainable with the process and the plant <NUM> outlined above, can be effectively used for manufacturing any ceramic product.

In general, this manufacture involves subjecting the ceramic granulate GF to a forming step, for example by pressing, extrusion, casting or other processes, so as to form a semi-finished product having a certain geometrical shape.

In particular, forming by pressing can be carried out inside a traditional mould (discontinuous pressing) or above a sliding belt with or without a mould (continuous or semi-continuous pressing).

After possible decoration steps, the semi-finished product obtained after the pressing step is subjected to a high-temperature firing step that transforms the raw materials of the granulate into new crystalline and/or glassy compounds, giving the product thus obtained particular chemical/physical properties, including the solidity and mechanical resistance necessary to maintain its shape.

In this specific type of applications, the ceramic granulate GF of the invention overcomes the characteristics of the granulates obtainable with known wet and dry granulation systems, guaranteeing a humidity, a particle size distribution and an apparent density completely similar to that of atomized powders as can be verified in Tables <NUM> and <NUM>. In addition, the particularly narrow particle size and the content of fine particles limit the classic phenomena of segregation of the powders that can be observed with the products obtained through the wet and dry granulation technologies of the known type. These characteristics make the granulate GF obtained with the process outlined above a solution that fully meets the demands of the ceramic market for the production of large-size formats even with the use of mouldless pressing systems and high energy efficiency.

It should be here pointed out that the particle sizes of the materials mentioned in the previous discussion refer to the materials as obtained from the respective process steps, without them undergoing any drying step preparatory to the measurement of the particle size.

In other words, the particle size of each material is measured by preparing a certain quantity of material without drying it, for example <NUM> grams of undried material, and by passing it through a series of sieves by falling with different, increasingly smaller mesh sizes.

Claim 1:
A process for preparing a ceramic granulate, comprising at least:
- a step of dry grinding ceramic raw materials to obtain a ceramic powder (P),
- a step of wetting said ceramic powder (P) with at least one liquid substance to obtain an agglomerated product (A),
- a step of compacting said agglomerated product (A) by applying a compaction pressure to obtain at least one compacted element (C),
- a step of crushing said compacted element (C) to obtain the ceramic granulate (G).
- a step of sieving with a sieve the ceramic granulate (G) to separate the coarse particles (S1) therefrom,
- a step of inertial separation of the ceramic granulate (V) to separate the fine particles (S2) therefrom.