The present invention refers to dyeing device and processes using indigo and/or other colorants to which the warp yarn chain and/or fabrics are subjected in a continuous manner. In particular, the invention relates to a continuous dyeing device and processes in dyeing machines and/or plants that must operate with reduction baths and at high or low temperatures. A typical application of this dyeing technology is that of the continuous dyeing of the warp chain for denim fabric, using indigo or other colorants, such as sulphur, indanthrene and reactive based colorants. Denim is the fabric normally used for the manufacturing of jeans and sportswear articles in general, and is the fabric used in the greatest quantity throughout the world. Classical-type denim is manufactured by weaving pre- dyed cotton yarn; in particular, only the warp is dyed in -a continuous manner with indigo or other colorants, whereas the weft is used in its raw state. Typically and traditionally, the dyeing of the warp chain for denim fabric is realised using both rope and shift systems in open vats at low temperature, using indigo, an ancient natural colorant, that is currently- produced by synthesis. The special dyeing method required for the • application of indigo colorant on cotton yarn is characteristic to this colorant. In fact, said colorant has a relatively small molecule with reduced affinity for cellulose fibre, and therefore for application on said fibre, it needs to be not only chemically reduced in an alkaline bath (in leuco form) but also requires a plurality of impregnations with squeezing and oxidation stages in the air, between each bath. Therefore in order to obtain medium or dark blue denim, the yarn must be subjected to a first dyeing process (impregnation, squeezing, oxidation) immediately followed by other over-dyeing stages: the greater the number of stages, the darker the colour, and the stronger the solidity of the required colour. The dyeing process described above is currently applied to the warp chain, using indigo in all the machines and installations in a continuous manner, for both rope and shift systems. More precisely, the machines described above are normally composed of 2 or more pre-treatment vats, 8 or more dyeing vats complete with the relative squeezing and oxidation units, followed by 3 or more units for final washing stages. The dyeing vats are connected to each other by a circulation system for mixing, changing and strengthening the dye bath, according to a known system, not described herein. It is known that the dyeing in these machines is performed in an alkaline environment and with a calculated excess of sodium hydrosulphite and that, as a result of the bath/air contact, it reacts with the oxygen in the air losing its reducing capacity towards the indigo. Because of the easy oxidation capacity of the hydrosulphite, metered quantities of hydrosulphite must be added to the dyeing bath to contrast this loss. This reintegration of the sodium hydrosulphite with stechiometrically corresponding amounts of caustic soda must be performed with regularity and precision in order to keep the dyeing capacity of the bath unaltered, and to guarantee constant and repeatable results. Among the aforesaid machines, those used in shift dyeing systems are then connected in line in dyeing installations to a slashing machine, that performs the slashing, the drying, and the winding of the dyed yarn on a beam, ready to be placed on the loom. The aforesaid dyeing machines must be constructed respecting determined basic parameters in relation to the immersion and oxidation times, and this is to permit the yarn to absorb the dye in the best possible conditions, and after squeezing, to be completely oxidated before entering into the following bath, so that it can be intensified, in other words so that the colour tone can be darkened. The average immersion time for the yarn in the dyeing bath is normally approximately 8-12 seconds, while the oxidation time after squeezing is approximately 60 seconds, which means that the yarn must remain exposed to the air for 60 seconds before it can be immersed again in the following vat, and this process is repeated for all the vats. Reduced oxidation time is possible only on those machines that are equipped with oxidation intensification devices, such as those described in patent n0 EP533286 by the same Applicant. The average dyeing speed can be calculated as approximately 30 metres per minute, and therefore this signifies an average length of 6 - 8 metres of yarn immersed in each bath, while the length of yarn exposed to the air between one bath and another is at least 30 metres and more. Therefore, considering a machine with eight dyeing vats as a basic installation, this means that a substantial length of yarn runs through the dyeing baths and the relative oxidation devices, since, by multiplying: 6m x 8 + 30 m x8, this equals 288 metres. These 288 metres of yarn, added to those much shorter lengths of yarn being processed in the other component machines on the line (dyeing machine + slasher) reach a total of 400 - 500 metres which make the line difficult to control, and at each batch change, certain quantities are considered as lost because the dyeing is not uniform and because of problems connected with the start-up of a new batch. The aforesaid machines must also adapt to dyeing processes with other colorants, such as the aforesaid sulphur, indanthrene and reactive based colorants, which require different methods from those used for indigo for their application. These machines, which use different processes from those used for indigo dyeing, therefore require flexibility and adaptability so as not to excessively increase the costs connected with the installation of specific dyeing systems. In light of what has been described above, it is clear that there is a need for a dyeing device and process ■ that will provide a considerable reduction in the yarn rejects between each batch, as well as a reduction in the size, and consequently the cost, of dyeing installations . Therefore, the purpose of the present invention is to realise a dyeing device that in one or more units can be used in continuous dyeing processes using indigo, and which will not only reduce the number of the vats normally used in the prior art, with the relative and consequential economical advantages, but which will also make it possible to work in a manner that will reduce the reject material in each batch. Another purpose of the present invention is to supply a device and a process able to work in inert environments, permitting a reduction in the consumption of hydrosulphite and soda in indigo dyeing. Another purpose of the present invention is to supply a device and process that permits the increase of colorant diffusion in the fibre during indigo dyeing, and to increase the pick-up capacity of the colorant itself. A further purpose of the present invention is to supply a device -and process that permit dyeing using colorants with high affinity such as sulphur, indanthrene and reactive colorants. Another purpose of the present invention is to supply a device and process that permits dyeing in the best possible technological conditions using indanthrene colorants with the pigmentation method and with reactive colorants using the two-stage method. Another purpose of the present invention is to provide the possibility of dyeing in small batches, or reduced yardage, an aspect that is increasingly in demand by the markets These and other purposes are achieved by the continuous dyeing device and process using indigo and/or other colorants for warp chain according to the present invention that has the characteristics described in the appended claims 1, 24, 30, 32, 35. Substantially, a continuous dyeing device using indigo and/or other colorants for warp chains according to the present invention is a type equipped with at least a first and a second dyeing compartment, suitable for containing dyeing vats, contained at least partially in a hermetically sealed chamber. The device comprises at least one squeezing element, interposed between the two dyeing compartments, and at least one means for heating and/or dehydrating the yarn to increase the diffusion of the colorant in the fibre and the pick up of the colorant itself, positioned downstream of the first dyeing compartment and the squeezing element. Further characteristics and advantages of the present invention will be made clearer in the following description, provided as an example, but not to be considered limiting in any manner, with reference to the appended drawings wherein: figure 1 shows a side view in elevation of a dyeing device according to the present invention; - figure 2 shows a side view in elevation of a dyeing device according to the present invention used for a continuous dyeing process of the warp chain using indigo; - figure 3 shows a side view in elevation of a dyeing device according to the present invention used for a continuous dyeing process of the warp chain using sulphur colorant; figure 4 shows a side view in elevation of a dyeing device according to the present invention used for a continuous dyeing process of the warp chain using indanthrene colorant; - figure 5 shows a side view in elevation of a dyeing device according to the present invention used for a continuous dyeing process of the warp chain using reactive colorants; and figure 6 shows a side view in elevation of an alternative embodiment of the dyeing device according to the present invention. The aforesaid figures show a continuous dyeing device using indigo and/or other colorants such as sulphur, indanthrene or reactive based colorants for warp chains according to the present invention. For greater descriptive clarity, hereafter reference will be made to warp chains only, even though obviously the invention also applies to fabrics. As can be seen in figure 1, the dyeing device, identified throughout by the reference numeral 100, is of the type equipped with at least two dyeing compartments 1, 2, adapted to contain the dyeing baths 11a, lib, lie, Hd, and in turn, contained, at least partially in a hermetically sealed chamber 20. The device 100, also comprises at least one squeezing element 14, interposed between the two dyeing compartments 1 and 2, and at least one means 3 for directly heating and/or dehydrating the yarn 13. The direct heating of the yarn 13 increases the diffusion of the colorant in the fibre after the impregnation in dyeing compartment 1, while the consequent dehydration caused by the evaporation of the water contained in the yarn, according to the type of colorant employed, prevents hydrolisation and/or provides greater pick up of the colorant in the following dyeing compartment 2. Advantageously, according to the present invention, the means 3 for direct heating and/or dehydration of the yarn 13 is positioned upstream of the second compartment 2. In this manner, the dehydration of the yarn 13 permits the yarn itself to increase the absorption capacity in the second bath - in other words, in compartment 2, which would otherwise be almost zero. Chamber 20, hermetically sealed, comprises at least one base 21, in turn comprising the two dyeing compartments 1 and 2 and at least one hood 22, that can be raised and reclosed over the base 21 to facilitate cleaning and maintenance interventions. Chamber 20 is hermetically closed thanks to special sealing means 9. In particular, in the preferred embodiment shown in figures 1 - 5, the sealing means 9 are represented by a hydraulic seal around the perimeter that is made with the base 21, comprising the two compartments 1 and 2, containing the baths 11a, lib, lie, Hd, that extend partially out from the side walls of the hood 22, and at least one dividing wall 7 for each compartment 1 and 2. Each dividing wall 7 is attached to the respective compartment 1 or 2, goes down into the baths lla, lib, lie, Hd, as shown in the figures, and has a seat 8 adapted to engage with the hood 22 to realise hermetic sealing. As an alternative, said hermetic sealing means 9 could be formed by gaskets (not shown) interposed between the hood 22 and the base 21, while remaining within the context of the present invention. The means 3 for directly heating the yarn 13 are illustrated in the preferred embodiment shown in the figures, as heated cylinders 73, preferably cylinders heated by a fluid. More precisely, three heated cylinders 73 are illustrated, over which the yarn 13 passes, arranged in a line one behind the next, directly upstream of the second dyeing compartment 2. According to the type of colorant used in the dyeing process, the cylinders 73 may also not be heated. For this purpose, in order to heat or not heat the cylinders 73 as required, a switch-controlled means is included, not shown, and adapted to activate or exclude the heating of cylinders 73. Said switch-controlled means are of the known type, or in any case, can be easily realised by those skilled in the art, and therefore will not be described herein. Said direct heating means 3 for the yarn 13 could also be realised alternatively using an infrared source adapted to heat the yarn 13 directly by irradiation or by using microwave or radio frequency sources adapted to heat the yarn 13 directly. However, it must be noted that whatever appropriate means used for heating the yarn 13 will remain within the context of the present invention. As a further example, for this purpose, the yarn 13 could be subjected to at least an inert dehumidified hot fluid flow. Upstream of the means 3 for direct yarn 13 heating, as stated previously, a squeezing means 14 is foreseen, capable of applying strong pressure on the yarn 13. More precisely, the squeezing element 14 is able to apply pressure on the warp chain 13 in a range between 3 and 20 tons. Preferably, the squeezing element 14 composed of two cylinders opposite each other, is able to apply pressure on the warp chain 13 in a range between 5 and 12 tons. Squeezing of this strength applied on the yarn 13 as it exits from the first dyeing compartment 1 eliminates any excess bath liquid from the yarn 13 in an excellent manner. Moreover, as can be seen in figure 1, the dyeing compartments 1 and 2 are also equipped with at least one means 17 for a heating or cooling action on the dyeing baths 11a, lib, lie, Hd, that is indirect and without any contact on the vats . In particular, the compartments 1 and 2 each present at least one coil 27 inside which a heating or cooling liquid circulates to heat or cool the dyeing baths Ha, lib, Hc, Hd, according to the dyeing process, in an indirect manner and without any contact with the vats contained in compartments 1 and 2. For this purpose, the coils 27 form, in a known way, a cavity in proximity to the bottom of the compartments 1 and 2. Further return rollers 30 and 31 are present inside the chamber 20, adapted to define the yarn 13 path inside the chamber 20. Compared to dyeing compartment 2, the dyeing compartment 1 has a larger yarn content, and consequently a larger vat in order to take best advantage of the dyeing affinity of the colorants. In other words, the dyeing compartment 1 has a larger yarn capacity than compartment 2. Advantageously, according to the present invention, there are also three immersion rollers 29 positioned in proximity to the bottom of compartment 1 and another in proximity to the bottom of compartment 2, so as to force the yarn 13 to pass through the dyeing baths near the bottom of the compartments 1 and 2. The three immersion rollers 29 in the dyeing compartment 1 are interposed by two intermediate squeezing elements 32 adapted to apply light pressure, that is - less than 6 tons, but preferably less than 1 ton, on the yarn 13. The pressure applied by the intermediate squeezing elements 32 facilitates the penetration of the colorants in the yarn 13 and provide greater colour uniformity. The two compartments 1 and 2 advantageously present overflow type entries 33a, 33b and exits 34a, 34b. More precisely, in the case of indigo dyeing, the two compartments 1 and 2 preferably operate with a single bath 11a, lie at maximum level, with the feeding respectively from the overflow entries 33a, 33b, and with the downflow from the two overflow exits 34a, as shown in figure 2. During indigo dyeing, the compartments 1 and 2 are placed in communication by means of a known hydraulic circuit, and therefore not described herein. The hydraulic circuit that provides fluid communication between the two compartments 1 and 2 can however be closed to prevent dyeing bath communication between the two compartments 1 and 2, as occurs, for example, in the case of dyeing operations using indanthrene or reactive colorants. Therefore the two dyeing compartments 1 and 2 can operate using different baths and/or different bath levels according to the dyeing process underway. More precisely, in the case of dyeing with indanthrene and reactive colorants, the two compartments 1 and 2 preferably operate with the two different baths lib and Hd, and at minimum level, with feeding from the overflow entries 33b and downflow from the overflow exits 34b. In the case of dyeing with sulphur, indanthrene or reactive based colorants, the two compartments 1 and 2 are connected to the relative hydraulic circuits (independent from that used for indigo dyeing) that can be cut off using valves, said circuits being of a known type and therefore not described any further herein. When the baths are at low level, the compartments 1 and 2 provide the maximum yarn/bath contact time but with the minimum bath fluid possible, an essential technological requisite for eliminating the known defect of colouring difference between the head and tail of the yarn, an effect that occurs with colorants other than indigo because of their greater affinity, when vats with large quantities of liquid are used. The possibility of using compartments 1 and 2 with a maximum yarn content and the minimum bath liquid possible is realised thanks to the special shape of the bottom of the compartments 1 and 2 around the rollers 29. The device 100 according to the present invention also presents an element 15, for adequate squeezing positioned downstream of the second compartment 2 to eliminate any excess bath liquid from the yarn 13 as it exits from the chamber 20 before the following oxidation or steaming stage. In particular, said squeezing element 15 is positioned outside the chamber 20 in a manner so that it is directly downstream of the second compartment 2. Furthermore, the device 100, according to the present invention, also comprises means for drawing in fluid mixed with steam from the chamber 20. For this purpose, the device 100 according to the present invention presents a closed circuit 4 for steam suction adapted to draw in fluid with the steam from the chamber 20, and if necessary, according to the dyeing process being performed by the device, it can also return said dehumidified fluid to the chamber 20. As shown in figure 1, therefore, the suction circuit 4 presents at least one steam suction means 40, such as a centrifugal suction means, adapted to draw in the fluid with the steam from chamber 20, and at least one heat exchanger 41 to condense the steam from chamber 20 and send back the dehumidified fluid to the said chamber 20. In a known way, the heat exchanger 41 comprises a coil 42 crossed by a coolant, and a discharge valve 43 for the water that condenses in the bottom of the heat exchanger 41. The suction circuit 4 foresees a further three-way discharge valve, not shown, positioned upstream of the heat exchanger 41 for direct discharge of steam to the exterior during dyeing processes using sulphur, reactive or indanthrene colorants; in this case a valve 47 will introduce air into the chamber 20. In order to reduce the consumption of the hydrosulphite and soda used in indigo dyeing baths 11a and lie, and provide the heating and dehydration of the yarn without oxidation of the colorant contained in the yarn, the device 100 according to the present invention is able to perform processing in an inert environment. For this purpose means 50 are foreseen for introducing deoxygenated air and/or nitrogen into the chamber 20 and means 51 for the extraction of oxygen from the chamber in order to create a deoxygenated and therefore inert processing environment inside the chamber 20. The means 50 for the introduction of deoxygenated air/nitrogen inside chamber 20 comprise an inlet valve 45 connected to a source of pressurised deoxygenated air or nitrogen, not shown. On the other hand, the means 51 for the extraction of oxygen comprise a discharge valve 46. An initial flow of nitrogen or deoxygenated air for a determined period of time with valve 46 open will permit the exit of the oxygen from the chamber 20, because of the over-pressure and difference of specific weight . The flow time necessary to create an inert environment inside chamber 20 is determined by instrumental measurement of the internal conditions of chamber 20, or alternatively, according to assessments and calculations made by experts. Figure 6 shows an alternative embodiment of the present invention which is very similar to that shown in figures 1 to 5 except for the fact that it presents two bases 21 and two hoods 22, that can be raised and closed hermetically on said bases 21 for cleaning and maintenance interventions. In this case, the hermetic sealing means 9 create a seal between each base and corresponding hood. The device 100 according to the present intervention provides for yarn dyeing as stated previously, using indigo , sulphur, indanthrene or reactive colorants. In particular, the indigo dyeing process using device 100, fig. 2, according to the present invention presents the following stages: a) immersion of the yarn 13 in the first compartment 1 containing the indigo dyeing bath 11a at high level; b) squeezing of the yarn 13 on exit from the bath 11a of first compartment 1 applying strong pressure in a range between 5 and 12 tons; c) direct heating of the yarn 13 to increase the diffusion of the colorant in the fibre and to dehydrate it in order to increase the absorption of the colorant in the following compartment 2; d) immersion of the yarn 13 in the dyeing bath lie containing indigo at high level in the second compartment 2; e) application of a second strong pressure squeezing on yarn 13 on exit from the second compartment 2/ f) subjecting yarn to oxidation, in a known way, outside the device 100; The aforesaid dyeing process presents the particularity of being substantially carried out in an inert environment. In particular the stages from a) to d) are carried out in an inert environment without the yarn, impregnated with reduced bath liquid (leuco) coming into contact with the oxygen in the air, thus preventing the destruction of the hydrosulphite. Furthermore, before beginning the indigo dyeing process, a flow of nitrogen or deoxygenated air is introduced into chamber 20 for a required period of time using means 50, and the oxygen is extracted using means 51 in order to create a substantially inert environment. The inert environment generated in this manner will be maintained in this state thanks to the perfectly hermetic sealing of chamber 20. During the stages from a) to d) , and in particular during stage c) steam is produced as a result of the dehydration of the yarn 13 heated by means 3. The nitrogen or deoxygenated air with the steam that has been generated in this manner, is drawn in by the closed suction circuit 4 and sent to the heat exchanger 41. The steam is condensed inside the heat exchanger 41 to form water that is then discharged through valve 43, while the dehydrated deoxygenated air or nitrogen returns to the interior of the chamber 20. Advantageously, according to the present process, the dyeing baths 11a and lie contained in compartments 1 and 2 can be heated to facilitate the penetration in the yarn, or can be suitably cooled to increase the affinity of the indigo towards the fibre with a consequential increase in the colour intensity which, as is well known, increases as the temperature is reduced. In particular the bath lie in the second compartment 2 is cooled, passing a coolant through the coil 27 in the second compartment if the heated yarn 13 on exit from the cylinders 73 raises the temperature of the bath too much. Furthermore, in order to facilitate the penetration and uniformity of the colorant on the yarn in bath 11a in the first compartment 1, the yarn 13 is subjected to light pressure by elements 32 just before the bath. Figure 3 shows a continuous dyeing process using sulphur-based colorant for yarn 13, on the device 100 according to the present invention. To summarise, said process comprises the following stages: a) immersion of the yarn 13 in the first compartment 1 containing a low level of dyeing bath lib with a sulphur-based colorant (for dyeing a black colour, a high level bath is used) ; b) squeezing by applying strong pressure ranging between 5 and 12 tons on the yarn 13 on exit from the bath lib in the first compartment 1; c) immersion of yarn 13 in the dyeing bath Hd with a sulphur colorant content at low level, in the second compartment 2 (high level is used for dyeing black colours) ; d) squeezing by applying strong pressure on the yarn 13 on exit from the second compartment 2; e) yarn is subjected to a steaming process in an appropriate steamer, not shown. It is important to note that the steam that evaporates from the high temperature dyeing baths and from the yarn during stages from a) to d) is drawn in by the suction circuit 4 and discharged externally through a three-way discharge valve, not shown. In this situation, the hood 22 will prevent the dispersion of any smells in the surrounding external environment . With this dyeing process as well, the yarn 13 is subjected to light squeezing by the squeezers 32 near the first compartment 1 to facilitate the penetration of the colorant in the yarn and make the colour more uniform. Furthermore, with this type of sulphur-based colorant, the dyeing bath lib, Hd contained in both the first compartment 1 and in the second compartment 2 is heated in a known way. Basically, the dyeing process using sulphur differs from the process using indigo in the type of bath used and for the different application temperature, as well as for the fact that it is possible not to heat the cylinders 73 which, in this case, act simply as return rollers, and for the fact that the process does not foresee an oxidation stage, but simply a steaming stage. Figure 4 shows a continuous dyeing process using indanthrene colorants for yarns 13 in the device 100 according to the present invention. To summarise, said process comprises the following stages : a) immersion of the yarn 13 in the first compartment 1 containing a low level of pigmentation bath Hb with a indanthrene-based colorant b) squeezing by applying strong pressure ranging between 5 and 12 tons on the yarn 13 on exit from the bath lib in the first compartment 1; c) direct heating of the yarn 13 to dehydrate it in order to prevent hydrolisation of the bath contained in the second compartment; d) immersion of the yarn 13 in the chemical bath Hd contained at low level in the second compartment 2; e) squeezing by applying strong pressure on the yarn 13 on exit from the second compartment; f) yarn 13 is subjected to a steaming process in a suitable steamer, not shown. In this dyeing stage as well, during the stages from a) to d) steam is also created and in particular, during stage c) , caused by the evaporation of water from the heated yarn 13. This steam is drawn in by the suction circuit 4 and discharged externally. Furthermore it should be noted that in this process the dyeing bath Hb contained in the first compartment 1 is heated and the bath Hd in the second compartment 2 is cooled. Also according to this dyeing process, the yarn 13 is subjected to light squeezing by the squeezer elements 32 near the first compartment 1 to facilitate the penetration of the colorant inside the yarn and make the colouring more uniform. Lastly, figure 5 shows a continuous dyeing process with reactive colorants according to the two-stage method. In short, this process comprises the following stages: a) immersion of the yarn 13 in the first compartment 1 containing a low level of dyeing bath lib with a reactive colorant ; b) squeezing by applying strong pressure on the yarn 13 on exit from the bath lib in the first compartment 1; c) direct heating of the yarn 13 to dehydrate it in order to prevent hydrolisation of the bath contained in the second compartment; d) immersion of the yarn 13 in the saline alkaline bath Hd contained at low level in the second compartment 2; e) squeezing by applying strong pressure on yarn 13 on exit from the second compartment; f) the yarn 13 is subjected to a steaming process in a suitable steamer, not shown. During the stages from a) to d) steam is created and in particular during stage c) caused by the heating of yarn 13. The steam generated in this manner is drawn in by the suction circuit 4 and discharged externally. In this process using reactive colorants in two stages, the dyeing bath contained in the first compartment 1 is heated and the bath in the second compartment 2 is cooled. In this case as well the yarn is subjected to light squeezing by means of the squeezer elements 32 near the first compartment 1 to facilitate the penetration of the colorant in the yarn and to make the colour more uniform. The device 100 and the processes according to the present invention therefore achieve the purposes proposed in the introduction to the description and contrary to machines and processes used up till the present time in indigo dyeing systems, the invention permits a considerable reduction in the number of the processing vats and as a result also a reduction in the cost of the equipment and a reduction in production reject material during batch changes. Advantageously, the device 100 and the processes realised using the device according to the present invention also provide the possibility of working in an inert environment when using indigo, thus permitting the dehydration of the yarn without the oxidation of the colorant, as well as the considerable reduction of the normal consumption of hydrosulphite and soda. The heating and/or dehydration of the yarn by the heating means 3 according to the present invention provides an increase in the diffusion of the colorant in the yarn and the pick-up (colorant absorption capacity) of the yarn itself, thus making the dyeing process more efficient, economical and ecological. In other terms, in the case of indigo dyeing, for the same level of colour tone and intensity obtained on the yarn, the present device 100 and the dyeing processes using the device provide the possibility of considerably reducing the number of necessary over¬ dyeing actions. The device according to the present invention also offers the possibility of dyeing small batches, or smaller yardage, an aspect increasingly in demand in the market. Indeed, it must be remembered that in traditional installations, the minimum pieces that can be dyed depends on the length of the yarn that constitutes the total path of the installation. In order to obtain medium or dark colour intensity, traditional dyeing installations using indigo require a large number of vats and as a result the installation size and cost are increased proportionally. The present invention has been described as an example but to be considered limiting by no means, according to its preferred embodiments, but it should be understood that variations and/or modifications can be applied by those skilled in the art while remaining within the scope of protection as defined in the appended claims.