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    • 专利摘要:
    The invention relates to a foam element (7) made from a foam and particles (11) of at least one hydrophilic substance, such as cellulose, hyperabsorbents. The foam element (7) containing the particles (11) has a reversible ability to absorb moisture. Part of the particles (11) is entirely housed in the foam. Another portion of the particles (11) is deposited to protrude from a surface (13) of the foam, such as cell walls (9) or cellular networks (10).
    公开号:BE1019498A5
    申请号:E2010/0033
    申请日:2010-01-21
    公开日:2012-08-07
    发明作者:Manfred Marchgraber；Franz Schaufler
    申请人:Eurofoam Gmbh；
    IPC主号:
    专利说明:

    FOAM ELEMENT IN WHICH HYDROPHILIC SUBSTANCES ARE INCORPORATED
    The invention relates to a foam element made from a foam and particles comprising at least one hydrophilic substance incorporated in the plastic, such as cellulose, with hyperabsorbents and a foam element containing the particles having a reversible ability to absorb moisture, as described in claims 1-7.
    At present, foams are used or used in many areas of daily life. For many of these applications, the foams are in contact with the body and are generally simply separated by one or more intermediate layers of textiles. Most of these foams are made from synthetic polymers such as polyurethane (PU), polystyrene (PS), synthetic rubber, etc., which, in principle, do not show an absorption capacity of adequate water. Especially when the mosses are in contact with the body for a long period of time or during an energetic physical effort, there is the appearance of an unpleasant physical sensation due to the large amount of moisture that is not absorbed. Therefore, for most applications, it is necessary that hydrophilic properties are provided to these foams.
    This can be done in a variety of ways. One possibility, as described in patent application DE 199 30 526 A, for example, is to give the foam the structure of a flexible hydrophilic polyurethane foam. This is achieved by reacting at least one polyisocyanate with at least one compound containing at least two bonds that react with isocyanate in the presence of sulfonic acids containing one or more hydroxyl groups, and / or their salts and / or polyalkylene ethers. glycol catalysed by monools. These foams are used for the manufacture of household sponges or hygiene articles. Another possibility is described in patent application DE 101 16 757 A1, based on an open-celled aliphatic polymeric hydrophilic foam having a separate additional layer made from cellulose fibers in which a hydrogel is housed, which serves as storage medium.
    The patent EP 0 793 681 B1 and the German translation of the patent DE 695 10 953 T2 describe a process for the production of flexible foams, for which hyperabsorbent polymers (SAPs), also known as hydrogels, are employed. The SAPs that are used can be premixed with the prepolymer, which makes the process very simple for the foam manufacturer. These SAPs can be selected from SAPs grafted with starch or cellulose using acrylonitrile. acrylic acid or acrylamide as unsaturated monomer, for example. These SAPs are marketed by Höchst / Cassella under the brand name SANWET IM7000.
    The text of patent WO 96/31555 A2 describes a foam with a cellular structure; this foam also contains hyperabsorbent polymers (SAPs). According to this embodiment, SAP can be made from a synthetic polymer or, alternatively, from cellulose. The foam employed in this embodiment is intended to absorb moisture and fluids and retain them in the foam structure.
    The text of patent WO 2007/135069 A1 describes shoe soles having properties that absorb water. According to this embodiment, the water-absorbing polymers are added before proceeding to the foaming stage of the plastic. These water-absorbing polymers are generally manufactured by polymerizing an aqueous monomeric solution and then optionally crushing the hydrogel. The water-absorbing polymer and the dry hydrogel made therefrom are then milled and screened once they have been produced, and the particle sizes of the dry and screened hydrogel are preferably lower at 1000 pm and preferably above 10 pm. In addition to the hydrogel, a filler may also be added and blended prior to the foaming process, in which case the organic fillers that may be employed include coal black, melamine, rosin and cellulose fibers, polyamide, polyacrylonitrile, polyurethane or polyester based on the principle of aromatic and / or aliphatic dicarboxylic acid esters and carbon fibers, for example. All substances are added to the reaction mixture separately from one another to produce the foam element.
    With respect to their properties, prior art foams are designed to be able to store and retain the moisture they absorb over a long period of time. Absorbed moisture and absorbed water are not restored to the original state due to evaporation of moisture in the ambient atmosphere over a period of up to 24 hours, such as explained in WO 2007/135069 Al.
    This rate of evaporation is much too slow in normal applications, such as in the case of mattresses, shoe insoles or car seats, for example, which are used for several hours a day and therefore , which have less than 24 hours to evaporate the absorbed moisture. In this context, one can speak of equilibrium moisture and the value of humidity is that at which the foam is in equilibrium with the humidity contained in the ambient atmosphere.
    Similarly, the underlying purpose of the present invention is to provide a foam element which, with respect to its moisture control, exhibits an important ability to absorb moisture and then demonstrates a high rate of evaporation of absorbed moisture, stored.
    This object is achieved by the present invention by means of features which are defined in claim 1 wherein at least a partial amount of the particles is fully housed in the foam and another partial amount of particles is deposited so as to exceed a surface of the foam, such as cell walls or cellular networks.
    The advantage of these characteristics lies in the fact that all the particles contained in the foam are not entirely surrounded by the latter, thus offering greater possibilities of contact with the ambient conditions both with regard to the taking moisture and evaporation of moisture. This partial amount of particles therefore results in a relatively fast and significant absorption capacity of the moisture or fluids to be absorbed; however, moisture or absorbed fluids are evaporated into the ambient atmosphere as quickly as possible from the state induced by use, thereby restoring equilibrium moisture. This results in a rapid elimination of moisture which allows the object to be reused after a short period of time.
    Independently of the above, the object of the invention can also be achieved on the basis of other characteristics which are defined in claim 1 according to which the foam without hydrophilic substance has an absorption capacity greater than 2, 8% by weight corresponding to an equilibrium moisture at a temperature of 23 ° C and a relative humidity of 93% while a proportion of the particles with reference to the total weight of the foam is included in a range whose lower limit is 0.1% by weight and the upper limit is 35% by weight.
    The advantage of these characteristics lies in the fact that the foam proposed as initial material already shows a significant absorption capacity without proceeding to the addition of the hydrophilic substance; however, it can easily be adapted to a range of different conditions of use by incorporating additional particles depending on the amount employed as a proportion by weight. If the amount of added particles is varied, not only is it possible to adjust the moisture control of the foam member, but it is also possible to adjust the various values of the associated forces as well as the elasticity. The higher the proportion of particles, the lower the elasticity, which can be compensated by increasing the weight in volume or the density.
    Independently of what is said above, the object of the invention can also be achieved on the basis of the features which are defined in claims 3 and 4. The advantage of the features defined in claims 3 and 4 lies in the fact that In spite of the particles incorporated in the foam, a compressive hardness suitable for the desired purpose can be obtained. This means that depending on the desired purpose of the foam element, it is possible to preset the values relating to the compressive hardness but that the user continues to be guaranteed optimum control of the humidity of the element. foam in its entirety. Due to the significant value of temporary storage of moisture, or water, which can be absorbed into the foam element during use, the user is sure to experience a pleasant and dry sensation during the 'use. As a result, the body does not come into direct contact with moisture.
    Independently of what is said above, the object of the invention can also be achieved on the basis of the features which are defined in claim 5. The advantage of the features defined in claim 5 lies in the fact that again, depending on the desired use of the foam element, sufficient elasticity can be achieved in the context of the various desired uses despite the presence of added particles which constitute the hydrophilic substance, providing a supporting effect associated with the user of the foam element. Similarly, it is possible to guarantee the user a certain comfort within predefined limits while providing adequate control of the humidity.
    Regardless of what is said above, the object of the invention can also be achieved based on the features which are defined in claim 6. The advantage of the features defined in claim 6 lies in the fact that can achieve a significant moisture absorption of the foam that is greater than that of conventional foam. Therefore, it is not only possible to achieve a high moisture absorption capacity, the latter being able to evaporate from the foam element, after use, in a relatively short period of time, which makes it quickly ready for a new use. This being so, a dry foam element is quickly ready for a new use.
    Regardless of what is said above, the object of the invention can also be achieved on the basis of features which are defined in claim 2. The advantage of features defined in claim 2 is that even with a foam containing no added hydrophilic substance, higher moisture absorption can be achieved in the case of predefined exposure to moisture and this can be further improved by the addition of particles which absorb and evaporate rapidly 1 ' humidity. As a result, it is not only possible to absorb and store a significant amount of moisture over a period of time during use, moisture evaporates rapidly in the environment after use. This means that a dry foam element is quickly ready for re-use after a relatively short period of time.
    Regardless of what is said above, the object of the invention can also be achieved on the basis of the features which are defined in claim 8. The advantage of the features defined in claim 8 lies in the fact that Because of the increase in bulk weight or density relative to the added particles to obtain better control of moisture, sufficient elasticity values can also be obtained. Therefore, not only is it possible to obtain a very important capacity of water vapor absorption and moisture absorption followed by a rapid rate of evaporation, but the corresponding elasticity and the effect associated support for the user can thus be adjusted.
    When adding cellulose to the foam structure, as defined in claim 10, it is also possible to obtain sufficient moisture or fluid absorption capacity, and the moisture or moisture content of the foam. Absorbed fluids evaporate into the ambient atmosphere as quickly as possible following use to restore equilibrium moisture. As a result, the moisture absorbed by the foam element evaporates quickly while it remains comfortable to use. This is the case even after it has absorbed a significant amount of moisture, it can be used again even after a relatively short time and a dry foam element is quickly ready for a new use. .
    A further advantage lies in another exemplary embodiment given in claim 11, characterized in that depending on the structure of the foam resulting foam, the length of the fibers can be determined so as to ensure optimal transport of the foam. moisture, which allows for both rapid absorption and rapid evaporation after use.
    An exemplary embodiment defined in claim 12 is also advantageous since it makes it possible to achieve a much more precise distribution of the cellulose particles in the structure of the foam; therefore, the foam element can be easily adapted to suit different applications.
    The embodiment defined in claim 13 makes it possible to improve the particle delivery capacity. The specific surface is increased due to the structure of the surface, which is irregular and not completely smooth which makes it possible to witness an exceptional adsorption behavior on the part of the cellulose particles.
    Another embodiment as defined in claim 14 provides the possibility of employing these particles without obstructing the fine orifices of the nozzle, even when using said CO 2 foam manufacturing process.
    A further advantage lies in another embodiment of claim 15 since a spherical shape is avoided and an uneven surface with no fraying of fibrous type and no fibril is obtained. A rod-shaped model is avoided and this contributes to efficient distribution within the foam structure.
    As a consequence of the embodiment of claim 16, the absorption capacity and the evaporation capacity of the element. foam can be easily adjusted according to the proportion of cellulose added, which allows to adapt it to different applications.
    As a consequence of the embodiment of claim 17, the cellulose can be added and moved during the manufacturing process at the same time as at least one other additive, which means that only the following must be taken into account. a single additive when mixed with a reaction component.
    An additional advantage lies in another embodiment of claim 2, since it allows the use of particles that can be easily manufactured from natural materials. This again makes it possible to adapt the absorption capacity and the evaporation of the moisture of the foam element so that it is suitable for different applications.
    An additional advantage lies in the embodiment of claim 18 since a natural material can be employed and it is possible, however, to prevent the occurrence of an unpleasant odor.
    As a consequence of the embodiment of claim 19, the particles are also nested in a coating without diminishing the ability of absorption and evaporation of moisture. This provides additional protection for the particles in the foam member and slows down, or completely prevents, the deterioration of the particles, especially in the area of sharp edges.
    On the basis of another embodiment defined in claim 20 or 21, the mutual mixing of the particles in one of the base materials used to make the foam is prevented, thereby ensuring a uniform distribution of the particles at the same time. interior of the foam element in its entirety during the foam manufacturing process. A substantially uniform distribution of particles throughout the section of the foam member to be produced can thus be achieved.
    A further advantage lies in the exemplary embodiment of claim 22 since the particles are disposed on the surface of cell walls and cellular networks which means that there is a high concentration of particles to absorb the particles. moisture and evaporate moisture in these areas of open cell foams. This makes it possible to further improve the storage and evaporation behaviors.
    As a result of the embodiment of claim 23, the coating applied to the foam member may be modified to suit a variety of applications since moisture may be absorbed by the surface of the foam. foam element, which is already large in size, and be evaporated through the particles contained in the coating.
    As a consequence of the embodiment of claim 24, the addition of a natural material has a positive effect on the user when he comes into direct or indirect contact with the foam member. The added material, which contains the appropriate substances, can also be used to provide a healing, calming or protective effect.
    As a consequence of the exemplary embodiment of claim 25, the foam member can be easily adapted to a range of different applications.
    An additional advantage lies in the exemplary embodiment of claim 26 since the resulting foam element can be used in a variety of different applications.
    Housing the particles within the cell structure as defined in claim 27 allows moisture to be absorbed by the particles disposed in the peripheral region of the cell walls and cell networks, thereby means that the space inside cell walls and cellular networks is also used to control humidity. This means that the absorbed moisture can be directed from the particles disposed in the peripheral region to the interior of the foam structure. This once again improves the absorption capacity and the subsequent evaporation of moisture.
    On the basis of another embodiment described in claim 28, it is possible to achieve a better moisture transport inside the foam element.
    The use of the foam element for a variety of different applications is also advantageous because it improves wearing comfort during use and the subsequent drying time is also faster. This is particularly advantageous in the case of different types of seats and mattresses, as well as for the types of applications in which the body transpires.
    In order to allow a clearer understanding of the invention, it will now be explained in more detail below with reference to the accompanying drawings.
    These drawings are simplified diagrams that illustrate the following:
    Fig. 1 is a first graph illustrating the moisture absorption between two predefined climates based on different samples and different sampling points; . *
    Fig. 2 is a second graph illustrating the different moisture absorption capabilities of conventional foam and foam replaced by cellulose particles;
    Fig. 3 is a third graph illustrating the different rates of evaporation of moisture from conventional foam and foam replaced by cellulose particles;
    Fig. 4 is a bar graph illustrating the absorption of water vapor by the plastic foam;
    Fig. 5 is a simplified large scale diagram illustrating a detail of the foam member and its foam structure;
    Fig. 6 is a simplified large scale diagram illustrating another detail of the foam structure of the foam member;
    Figs. 7-15 are simplified and highly schematic diagrams that illustrate the various ways in which particles can be incorporated into the foam and that the coating is applied to the foam.
    First of all, it should be noted that the identical parts described in the various exemplary embodiments are indicated by identical reference numbers and that the identical component names and descriptions given in this patent text can be transposed in terms of meanings to like parts that have the same reference numbers or the same component names. In addition, the positions chosen in the context of the description, such as vertex, bottom, side, etc., relate to the drawing which can be specifically described and can be transposed in terms of meanings to a new position when the we proceed to the description of another position. The individual features or combinations of features from the various exemplary embodiments illustrated and described can be constructed as independent inventive solutions or as solutions provided by the invention per se.
    All figures referring to ranges of values in this description shall be interpreted to include any or all of the partial ranges, in which case, for example, the range of 1 to 10 shall be understood to include all partial ranges. from the lower limit of 1 to the upper limit of 10, ie all partial ranges having as their starting point the lower limit of 1, or more, and ending with the upper limit of 10, or less, eg 1 to 1.7, or 3.2 to 8.1 or 5.5 to 10.
    A more detailed explanation is first given for the hydrophilic substance, provided in cellulose form, incorporated in the plastic foam, particularly in the foam element made therefrom.
    However, it is also possible to add other hydrophilic substances. These can consist of hyperabsorbents, for example, or, alternatively, particles made from a multitude of different woods. These materials may have a particle size of less than 400 μιη. If the particles made from these woods are used, it is advantageous that they be coated with a substance which inhibits or prevents deterioration. Another possibility is to impregnate them completely. Regardless of what is said above, however, it is also possible to embed the wood particles in a plastic material by means of an extrusion process or to embed them therein and then reduce them to the particle size desired using a crushing process, such as shredding or grinding.
    The foam member is, therefore, made from the plastic foam and the hydrophilic substance incorporated therein. The plastic foam can in turn be manufactured from a suitable mixture of components which can be foamed together, preferably in liquid form, by a method known for a long time.
    As already explained above, in the patent specification WO 2007/135 069 A1, the cellulose fibers are added in addition to the polymer which absorbs water in the form of an extra charge. These are intended to increase the mechanical properties of the foam when necessary. In this regard, however, it has been discovered that the addition of fibrous additives makes it more difficult to transform the initial mixture to be foamed due to changes in fluidity. For example, the fibrous cellulose particles mixed with the polyol component, especially prior to the foaming step, make it more viscous, which makes it more difficult or impossible to mix with another component, know the isocyanate at the level of the gauging head of the foaming unit. They may also complicate the spread of the reaction component on the conveyor belt of the foam forming unit. Fibrous cellulose particles may also tend to adhere to the conveyor belts of the reaction mixture, forming deposits.
    Therefore, it is simply possible to add fibrous additives within certain limits. The smaller the amount of fibrous additives, as a proportion, especially the shortened cellulose fibers, the lower the water absorption capacity when added to the foam. It can be expected that even the addition of small amounts of fibrous cellulose powders increases the viscosity, especially of the polyol component. Although, in principle, it is possible to convert these mixtures, the modified viscosity during processing must be taken into account.
    Cellulose and the yarns, fibers or powders made therefrom are generally obtained by processing and grinding the cellulose or, alternatively, wood and / or annuals with the aid of a generally known method.
    Depending on the nature of the production process, powders of different qualities (purity, size, etc.) are obtained. All these powders have in common a fibrous structure because the natural cellulose of any size shows a marked tendency to form these fibrous structures. Even MCC (microcrystalline cellulose), which can be described as spherical, is still made from pieces of crystalline fiber.
    Depending on the microstructure, a distinction is made between different types of cellulose structure, especially cellulose-I and cellulose-II. These differences between these two types of structures are described in detail in the relevant literature and can also be seen using X-ray technology.
    A substantial portion of the cellulose powders consist of cellulose-I. The production and use of cellulose-I powders are protected by a large number of patents. Many technical details of the grinding processes are also protected, for example. Cellulose-I powders are of a fibrous nature, which does not contribute much to a number of applications and may even be an obstacle. For example, fibrous powders often cause the fibers to cling to each other. They are also associated with a limited ability to flow freely.
    Cellulose powders based on cellulose-II are currently very difficult to find on the market. These cellulose powders having this structure can be obtained either from a solution (usually viscose) or by grinding the cellulose-II products. Such a product may consist of cellophane, for example. These fine powders whose grain size is 10 pm or less can also be obtained in very small quantities only.
    Spherical, non-fibrillated cellulose particles having a particle size in the range of 1 μm to 400 μm may be produced from a non-derived cellulose solution in a mixture or an organic substance and 'water. This particle size can also be used for all other added particles. This solution is cooled below its hardening temperature and the solidified cellulose solution is then milled. Subsequently, the solvent is washed and the milled particles are dried. The subsequent grinding is generally carried out in a crusher.
    This is particularly advantageous if at least the following individual additives are incorporated into the pre-prepared cellulose solution prior to its cooling and curing. This additive can be selected from the group comprising pigments, inorganic substances such as titanium oxide for example, particularly substoichiometric titanium dioxide, barium sulfate, ion exchangers, polyethylene, polypropylene, polyester, carbon black, zeolite, activated carbon, polymeric hyperabsorbents or flame retardants. They are then incorporated simultaneously into the cellulose particles produced. They can be added at different times during the production of the solution but under no circumstances can they be added before curing. In this regard, from 1% by weight to 200% by weight of additives may be incorporated, based on the amount of cellulose. It has been discovered that these additives are not removed during washing but remain in the cellulose particles and strongly retain their function. For example, if activated carbon is incorporated, its active surface area, which can be measured using the BET method, for example, is also preserved intact in the finished particles. The additives present on the surface of the cellulose particles as well as those present inside these particles are also fully preserved. This can be considered particularly beneficial since only small amounts of additives must be incorporated into the pre-prepared cellulose solution.
    The advantage is that it is only necessary to add the cellulose particles already containing the functional additives to the reaction mixture so as to produce the foam element. While in the past all the additives were added separately and individually to the reaction mixture, it is now simply necessary to take into account one type of additive when setting up the foam manufacturing process. This avoids uncontrollable fluctuations in the suitability of many of these different additives.
    The consequence of this approach is that a single cellulose powder is obtained, which is made of particles having a cellulose - II structure. The cellulose powder has a particle size within a range whose lower limit is 1 μm and the upper limit is 400 μm for a mean particle size of x50 characterized by a lower limit of 4 μm and an upper limit of 250 μm in the case of a monomodal particle size distribution. The cellulose powder or particles have particles whose shape is approximately spherical, characterized by an irregular surface and crystallinity within a range whose lower limit is 15% and the upper limit is 45% based on the method. from Raman. The particles also have a specific surface (Adsorption-N2, BET) characterized by a lower limit of 0.2 m 2 / g and an upper limit of 8 m 2 / g for a bulk density with a lower limit of 250 g / l and a upper limit of 750 g / 1.
    The structure of Cellulose II is produced by dissolving and re-precipitating the cellulose, and the particles are very different from particles made from cellulose without a dissolution stage.
    The size of the particles in the range cited above whose lower limit is 1 μιη and the upper limit is 400 μπι with a particle distribution characterized by a value x50 characterized by a lower limit of 4 μιη, especially of 50 μιη, and an upper limit of 250 μιη, especially 100 μπι, is naturally affected by the procedure used for grinding during the grinding process. However, this distribution of the particles can be obtained particularly easily if one opts for the specific production method based on the hardening of a solution of non-agglomerating cellulose and because of the mechanical properties provided to the hardened cellulose compound. The application of shear forces to a hardened cellulose solution under identical grinding conditions gives rise to different but fibrous properties.
    The shape of the particles employed is approximately spherical. These particles have a crystallographic ratio (1: d) whose lower limit is 0.5, especially 1, and the upper limit is 5m, especially 2.5. They have an irregular surface but do not show any fraying of fibrous type or any fibril under a microscope. It is absolutely not about spheres with a smooth surface. This form is also not particularly suitable for the desired applications.
    The bulk density of the cellulose powders described in the present, which is between a lower limit of 250 g / l and an upper limit of 750 g / l, is significantly greater than that of fibrillar particles known in the art. The bulk density has significant processing advantages as it also improves the compactness of the cellulose powder described herein and, among other things, results in better flowability, miscibility within the range of different environments and in reducing the problems occurring during storage.
    In short, it can be said that the resulting cellulose powder particles are able to flow more freely due to their spherical structure and induce almost no change in viscosity due to their structure. Characterization of particles using the particle sizing device widely used in industry is also easier and meaningful because of the spherical shape. The structure of the irregular surface and which is not completely smooth gives rise to a larger surface area, which contributes to the extraordinary adsorption behavior of the powder.
    Regardless of what is said above, it is also possible to mix a pure cellulose powder, or particles thereof, with other cellulose particles, which also contain incorporated additives whose lower limit is 1% by weight and the upper limit is 200% by weight in proportion to the amount of cellulose. These individual additives can also be selected from the group comprising pigments, inorganic substances such as titanium oxide, for example, especially substandard titanium dioxide, barium sulfate, ion exchangers, polyethylene, polypropylene, polyester, activated carbon, polymeric hyperabsorbers and flame retardants.
    Depending on the foam manufacturing process used to produce the foams, the spherical cellulose particles have been found to be particularly useful in comparison to fibrous cellulose particles, especially in the case of C02 foam manufacturing. The manufacture of C02 foam can be carried out using the Novaflex-Cardio process or by similar methods, for example, for which nozzles are used whose orifices are particularly fine. Crude and fibrous particles could immediately block the jet holes and cause other problems. For this reason, the high degree of fineness of spherical cellulose particles is particularly advantageous in the context of this specific foam manufacturing process.
    The foam member and the production approach of the foam member proposed by the present invention will now be explained in more detail with reference to a number of examples. These are constructed, as far as possible, as exemplary embodiments of the invention; however, the invention is in no way limited by the scope of these examples.
    Figures referring to moisture as% by weight refer to the mass or weight of the entire foam element (plastic foam, cellulose particles and water or moisture).
    Example 1: The foam member to be produced can be made from a plastic foam such as polyurethane foam, for example, and a full range of different options and manufacturing methods can be used. These foams generally have an open-cell structure. This can be done using a "QFM" foaming machine marketed by Hennecke, and the foam is produced in a continuous process using a high-pressure gauging device. All the necessary components are accurately metered under the control of a computer via controlled pumps and are mixed using the stirring principle. In this particular case, one of these components is the polyol, which is replaced by the cellulose particles described above. Since the cellulose particles are mixed with a reaction component, the polyol, various adjustments must be made to the formula, such as water, catalysts, stabilizers and TDI so as to strongly neutralize the effect of cellulose powder incorporated for production and subsequent physical values obtained.
    A possible foam based on the invention is produced with 7.5% by weight of spherical cellulose particles. To do this, a spherical cellulose powder is first produced which can then be added to a reaction component of the foam to be produced. In terms of quantity, the proportion of particles, particularly cellulose, compared to the total weight of the foam, more particularly of the plastic foam, can be in a range whose lower limit is 0.1% by weight, all especially 5% by weight, and the upper limit is 35% by weight, most preferably 20% by weight.
    Example 2 (Comparative Example):
    In order to allow comparison with Example 1, a foam member is made from a plastic foam that is produced without the addition of cellulose powder or cellulose particles. It can be a standard foam, an HR foam or a viscose foam, each consisting of a known formula and then being foamed.
    The first objective is to determine if the cellulose particles are uniformly distributed in all layers of the resulting foam element in terms of height. This is accomplished by determining said moisture equilibrium based on the water intake by the foams in a standard climate at 20 ° C and 55% hr. and in another standardized climate at 23 ° C. and 93% hr. To do this, samples of the same size are taken from foam blocks manufactured as specified in Examples 1 and 2 at three different heights. the water intake in the two standardized climates described above is measured. In this respect, 1.0 m represents the top layer of the foam block, 0.5 m the middle layer and 0.0 m the bottom layer of the foam from which the samples are taken from the replaced plastic foam by cellulose particles. The total height of the block is about 1m. The cellulose-free plastic foam of Example 2 is used for comparison.
    As can be seen from these figures, the foam replaced by cellulose particles absorbs significantly more moisture than the cellulose-free foam, both in the standard climate and in the other climate standardized with moisture of physical balance. There is also a relatively good correlation for the measurement results for the different points from which the samples are taken (top, middle, bottom), which leads to the conclusion that there is a homogeneous distribution of samples. cellulose particles in the foam element produced.
    Table 2 below shows the mechanical properties of the two foams manufactured as described in Examples 1 and 2. It clearly appears that the type of foam made from the cellulose particles has mechanical properties which are comparable to the foam which is not replaced by cellulose particles. This involves problem-free processing of the reaction components, especially if they incorporate the spherical cellulose particles.
    The foam having added cellulose particles should have the following desired values for the two desired types of foam:
    The average weight by volume or density of the entire foam element is within the range of which the lower limit is 30 kg / m3 and the upper limit is 45 kg / m3.
    Fig. 1 indicates the percent moisture of the foam for samples of the same type but taken at different locations from the foam member as described above. The moisture of the foam as [%] is shown on the y-axis. The proportion of cellulose powder or cellulose particles added, in this example, is 10% by weight and the cellulose particles are the spherical cellulose particles described above. These different individual samples, with and without additives, are represented on the abscissa axis.
    The foam moisture measurement points of the individual samples shown as circles represent the initial value and the measurements shown in square form are obtained for the same sample but after a day of moisture uptake. The lower initial values are determined for the standard climate described above and the other value shown for the same sample represents moisture uptake in the other standardized climate after 24 hours at 23 ° C and 93% h. r .. The abbreviation hr refers to the relative humidity or humidity in the air and is given in%.
    Fig. 2 represents moisture uptake over a period of 48 hours, with time values (t) being plotted on the x-axis by [h]. The initial state of the body of the sample is again that of the standard climate of 20 ° C and 55% hr. defined above. The other climate standardized at 23 ° C and 93% hr. is intended to represent a climate based on use or on the body climate so as to determine the period during which the moisture of the foam increases in% by weight. The moisture values of the foam are shown on the y-axis as [%].
    The first line graph 1 whose measurement points illustrated in circles represent a foam element with a predefined size of the sample based on Example 2 without the addition of cellulose particles or cellulose powder.
    The other line graph 2, whose measurement points, shown as squares, represent the foam moisture of a foam member to which 7.5% by weight of cellulose particles or cellulose powder is added . The cellulose particles again consist of the spherical cellulose particles described above.
    The 48-hour moisture graph illustrates that the physical balance moisture of "mosses" in the "body climate" is reached after only a short time. It can thus be concluded that the foam replaced by cellulose particles is capable of absorbing twice as much moisture in 3 hours as a foam based on Example 2 to which cellulose particles are not added.
    Moisture measurements are obtained by storing the pieces of foam with a volume of about 10 cm3 in a dryer whose humidity in the air is determined (using a saturated KN03 solution) and 93% hr), having previously been used to dry the samples. The samples are removed from the dryer after a set period of time and the weight gain (= water intake) is measured. Fluctuations in moisture uptake can be explained by sample handling as well as a slight lack of homogeneity in the samples.
    Fig. 3 illustrates the drying behavior of a foam element to which cellulose particles are added based on Example 1 compared to a foam based on Example 2 to which no cellulose particles are added. For comparison purposes, both samples were first conditioned in the "body climate" for 24 hours. It is again a temperature of 23 ° C and a relative humidity of 93%. Moisture values of the foam are plotted on the y-axis as [%] and the time (t) in [min] is plotted on the abscissa. The specified percent values for foam moisture are given in percent by weight based on the weight or weight of all foam elements (plastic foam, cellulose particles and water or moisture).
    The measurement points illustrated in circles are again related to the foam element based on Example 2 to which no cellulose particles are added representing a corresponding line 3 which represents the decrease in moisture. The measurement points illustrated in the form of squares are determined for the foam element to which cellulose particles are added. Another corresponding line 4 also represents the evidence of a rapid evaporation of moisture. The proportion of cellulose particles is again 7.5% by weight.
    It is obvious that the equilibrium moisture of 2% is already restored after a period of about 10 minutes. This is much faster than in the case of a foam of the prior art that requires several hours to evaporate a comparable amount of water.
    When the foam element replaced by cellulose particles based on the crystalline modification of cellulose-II is conditioned in the "body climate" for a period of 24 hours and then exposed to the "standard climate", it initially absorbs a carbon content. in moisture greater than 5% by weight and the moisture content is reduced by at least 2 (two)% over a period of 2 min after being introduced into the "standard climate".
    From the two graphs shown in Figs. 2 and 3, it can be seen that the foam element replaced by particles, more particularly by cellulose particles, has a moisture absorption capacity greater than 3.5% by weight in the case a "body climate" of 23 ° C and a relative humidity of 93% which is, therefore, greater than the capacity of the foam element to which no cellulose particles are added.
    In this regard, it is also possible to add additives to the base material (s) used to make the plastic foam so as to increase the ability of the plastic foam to absorb moisture, even without the particles. This additive is generally added to, or mixed with, the polyol component prior to the foam manufacturing process. However, the disadvantage is that the elasticity of the resulting plastic foam decreases and is less than that of the same plastic foam produced without the additive. In order to increase the elasticity of the plastic foam, its weight in volume can be increased, again increasing, therefore, the elasticity. Bulk weight or density should be selected to be greater than 45 kg / m3. The same is true for plastic foams to which particles are added, even if no additives are added to the base materials used to make the plastic foam in order to increase the moisture absorption capacity.
    For example, in the case of a plastic foam which is not added to a hydrophilic substance, a moisture absorption capacity of greater than 2.8% by weight can be obtained in the case the "body climate" of 23 ° C and 93% relative humidity.
    Fig. 4 is a bar graph showing the absorption of water vapor "Fi" based on Hohenstein in [g / m2] and these values are represented on the ordinate axis. The "Fi" value for a material is a measure of its ability to absorb water vapor. The value Fi is determined by estimating the weight of the sample at the start of the measurement and at the end of the measurement and the difference in weight represents the water vapor absorbed over a short period of time .
    The period during which water vapor is absorbed from the standard climate of 20 ° C and 55% hr. defined above and in the standardized climate of 23 ° C and 93% hr. also defined above (application climate and body climate) for the two measured values obtained is 3 (three) hours. The samples are "B" type foam samples described above. A first bar graph 5 illustrates a "B" type foam without cellulose or added cellulose particles. The value measured in this case is about 4.8 g / m2. The foam replaced by cellulose, on the other hand, indicates a larger value of about 10.4 g / m 2 and this can be represented on another bar graph 6. This other value is, therefore, greater than a value of 5 g / m2 based on Hohenstein.
    Figs. 5 and 6 illustrate a detail of the foam, especially plastic foam, forming the foam member 7 on a larger scale on which several cells 8 are schematically illustrated on a simplified basis. The term "cell" 8 denotes a small cavity in the foam structure, which is partially and / or completely surrounded by cell walls 9 and / or cellular networks 10. If the cell walls 9 are continuous and surround the cavity which form the cell 8 in its entirety, it can be concluded that the structure of the foam is a structure based on closed cells. If, on the other hand, the cell walls 9 or the cellular networks 10 are only partial, it can be concluded that the structure of the foam is a structure based on open cells, in which the individual cells 8 are connected to each other. with the others.
    As also illustrated on a simplified basis, the particles 11 described above are disposed or lodged in the foam, especially in the plastic foam, of the foam member 7. Sometimes only a partial amount of the particles 11 is partially accommodated in the plastic foam of the foam member 7. This means that these partial amounts of particles 11 are merely partially disposed within the plastic foam and protrude from the cell wall 9 or the cellular network 10 towards the the cell 8 forming the cavity. Partial regions of particles 11 are accommodated in the plastic foam. However, another partial amount of particles 11 can be fully housed in the cellular structure of the plastic foam, and thus is completely surrounded by it.
    As schematically illustrated at the top left of FIG. 5, the plastic structure of the plastic foam is provided with an additional coating 12 or has one on the surface of one of the cell walls 9 or one of the cellular networks 10. This coating 12 may be applied by immersion or by impregnation but also using a completely different coating process. This coating 12 must show a high permeability to moisture and the particles 11 can also be contained in the fluid used for the coating 12. This can be achieved by mixing and thus replacing the particles 11 by the coating 12 to the liquid state and the particles are maintained, or bonded, using the coating 12 as an adhesion process during the drying process.
    Regardless of what is said above, however, it is also possible for at least some of the particles 11, but generally for all the particles 11, to be provided with another separate coating, which also demonstrates a high permeability to moisture or water vapor.
    Regardless of what is said above, however, and as can be seen from the detail illustrated in FIG. 6, it is also possible that none of the particles 11 described above is disposed in the cell wall 9 or in the cellular network 10, but rather that the particles 11 are exclusively contained in the coating indicated schematically 12, where they are fixed so as to provide the desired absorption of moisture. The individual particles 11 can in turn be made from the different materials described above, and it is also possible to use any combination of individual particles 11. These various combinations of different particles 11 are also possible in disposing the particles 11 on or in the cell walls 9 or the cellular networks 10.
    Figs. 7 to 15 are a simplified illustration of the foam element 7, and the coating 12 described above can be applied to at least some areas of its surface 13. For the sake of simplicity and to ensure the clarity of the diagrams the cell walls 8 and the cellular networks 9 have been omitted and the foam element 7 and the coating 12 are each represented in block form on an exaggerated scale. The aim is to provide the clearest possible illustration of the various possibilities of arranging the particles 11 in or on the foam element 7 and / or in or on the coating 12.
    Fig. 7 illustrates the foam element 7 in which the particles 11 described above are incorporated, a proportion or a partial amount of the particles 11 being disposed completely inside the foam while another proportion or partial amount of the particles 11 is arranged to extend outwardly from the surface 13 of the foam material of the foam member 7. In this regard, a proportion or a partial amount of the totality of the particles 11 is disposed in the vicinity of the surface 13 so that they protrude from the surface 13, while a partial region or a partial portion of these particles 11 is still housed in the foam and is thus retained and secured by the latter. The term "proportion or partial amount of particles 11" refers to a specific amount in terms of quantity or number of pieces. The partial region or the partial portion of the particles 11 refers to a determined size of an individual particle 11 based on the volume.
    Fig. 8 illustrates another foam member 7 which is provided with the coating 12 described above. The particles 11 are all entirely housed in the foam element 7 and, in this embodiment, no particle 11 protrudes from the surface 13 of the foam material of the foam element 7. The coating 12 is, on its turn, also replaced by the particles 11 and, in this embodiment, all the particles 11 protrude from the surface 14 of the coating 12. In this embodiment, the particles 11 are disposed in the region of the surface 14 of the coating 12 and more or less strongly exceed it - depending on the depth at which the particles are nested - and are retained by the coating 12 since a portion of them still extends across the coating 12 .
    Fig. 9 illustrates another foam member 7 which is, in turn, provided with a coating 12 at at least one of its surface regions 13. In this embodiment, some of the particles 11 are also fully housed in the foam and a proportion or a partial amount of the particles 11 also exceeds the surface 13 of the foam. The particles 11 in the coating 12 are all exclusively disposed in the region of the surface 14, in this embodiment, and more or less strongly exceed it at some of these regions, depending on the depth according to which the particles are nested. As illustrated, a particle 11 in the region of contact between the coating 12 and the foam of the foam member 7 can extend from the foam and through the coating 12 since a partial amount of particles 11 is arranged to protrude from the surface 13 of the foam.
    The particles 11 in the foam illustrated in FIG. 10, are arranged in a manner identical to that described in FIG. 9. A partial amount of the particles 11 is, therefore, entirely housed in the foam of the foam member 7 and a partial amount of the particles 11 is, in turn, disposed so as to protrude from the foam surface 13 . The particles 11 of the coating 12, in this embodiment, are entirely disposed inside the coating 12. As illustrated in the case of a particle 11, it protrudes from the surface 13 of the foam 7 through the surface 13 and thus also extends through the coating 12 once the latter has been applied.
    In the case of the foam element 7 illustrated in FIG. 11, all the particles 11 are entirely disposed within the foam used to manufacture the foam member 7. The particles 11 disposed in the coating 12 constitute a partial amount which is entirely disposed within the coating 12 and constitute another partial quantity that protrudes from the surface 14.
    According to the exemplary embodiment of the foam element 7 illustrated in FIG. 12, the particles 11 are fully housed in the foam and a partial amount in turn exceeds the surface 13 of the foam. Again, the coating 12 contains a partial amount of particles 11 which are entirely disposed within the coating 12. Another partial amount of the particles 11 protrudes from the surface 14 and a partial portion of the particles 11 is accommodated in the coating 12 .
    In the case of the exemplary embodiment illustrated in FIG. 13, the particles 11 are arranged in the foam so that they protrude exclusively from certain regions of the surface 13 and a partial portion of these particles 11 is accommodated in the foam. The particles 11 contained in the coating 12 are all entirely housed therein. As illustrated using a single particle 11, it may protrude from the surface 13 of the foam and extend into the coating 12.
    According to the exemplary embodiment illustrated in FIG. 14, the foam contains none of the particles 11 described above. On the other hand, the coating 12 contains both a partial amount of particles 11 which are entirely disposed within the coating 12 and another partial amount of particles which protrude from the surface 14.
    Finally, in the case of the exemplary embodiment illustrated in FIG. 15, the particles 11 contained in the foam protrude exclusively from the surface 13 and a partial portion of these particles 11 is disposed in the foam. In this embodiment, no particle 11 is fully housed in the foam. The coating 12 contains both a partial quantity of particles 11 entirely housed in the coating 12 and another partial quantity of particles 11 exceeding, more or less strongly, from the surface 14, depending on the depth at which the particles are nested. . At the region of contact between the foam and the coating 12, the particles 11 are illustrated as protruding from the foam surface 13 of the foam member 7 and thus extending through the coating 12.
    The foam member is made from a plastic foam, and a PU foam is used as the preferred foam. As explained above in connection with the individual diagrams, moisture uptake is determined from said equilibrium moisture representing a "standard climate" at 20 ° C with a relative humidity of 55%. In order to simulate a use, another standardized climate is defined at 23 ° C with a relative humidity of 93%. This other standardized climate is intended to represent the moisture absorbed during use in the body of a human being transpiring, for example a person. The cellulose incorporated in the foam element is intended to disperse the absorbed moisture during a period of use with a lower time limit of 1 hour and the upper time limit is 16 hours again after use and thus restore to the entire foam element the equilibrium moisture with reference to the ambient atmosphere. This means that the stored moisture evaporates from the cellulose very quickly after use, which is emitted into the ambient atmosphere and thus allows the foam element to dry.
    As mentioned above, it can be said that there is equilibrium moisture when the foam member has been exposed to one of the ambient atmospheres described above to a degree that the moisture value of the The foam element (foam moisture) is in equilibrium with the humidity value in the ambient atmosphere. When the equilibrium moisture level is reached, there is no longer any moisture exchange between the foam member and the surrounding atmosphere around the foam member.
    The test methods described above can be carried out so that the foam element is exposed to the first ambient atmosphere characterized by the first climate which is based on the predefined temperature and relative humidity of the air, for example 20 ° C and 55% hr, until the equilibrium moisture is reached in this ambient atmosphere, whereupon this same foam element is exposed to a second ambient atmosphere, modified or different, which is different from the first ambient atmosphere. This second ambient atmosphere has a second climate characterized by a higher temperature and / or relative humidity of the upper air compared to the first climate, for example 23 ° C and 93% of hr. Therefore, the value moisture from the foam increases and moisture is absorbed by the cellulose that is incorporated into the foam. Subsequently, the same element is exposed again to the first ambient atmosphere and, following the lapse of time between 1 hour and 16 hours specified above, the initial value of the moisture of the foam which corresponds to the equilibrium humidity based on the first ambient atmosphere is restored. Consequently, during this time, the moisture absorbed by the cellulose, in the context of the second ambient atmosphere, is evaporated in the ambient atmosphere and, consequently, reduced.
    The lower value of 1 hour specified herein depends on the amount of liquid or moisture absorbed but can also be much lower, in which case it can be adjusted within minutes.
    Apart from the spherical cellulose particles described above, it is also possible to use cellulose in the form of cut fibers characterized by a fiber length whose lower limit is 0.1 mm and the upper limit is 5 mm. . However, it is also possible to use cellulose in the form of crushed fibers characterized by a particle size whose lower limit is 50 μm and the upper limit is 0.5 mm.
    Depending on the field of application, the foam to be produced has different properties and these are characterized by a range of different physical properties. For example, the density may be between a lower limit of 14 kg / m3 and an upper limit of 100 kg / m3.
    The compressive strength at a compression of 40% may be within a range whose lower limit is 1.0 kPa, preferably 2.5 kPa, and the upper limit is 10.0 kPa, preferably 3.5 kPa. The elasticity as measured by the ball test may have a value whose lower limit is 5% and the upper limit is 70%. However, this range of values can also be between a lower limit of 25%, preferably 35%, and an upper limit of 60%, preferably 50%. This test method is performed according to EN ISO 8307 and the rebound height and inverse parallel elasticity are determined.
    If the produced foam element is made from a polyurethane foam, especially a flexible foam, it can be produced with both a TDI base and an MDI base. However, it is also possible to use other foams, such as polyethylene foam, polystyrene foam, polycarbonate foam, PVC foam, polyimide foam, foam foam, silicon, PMMA foam (polymethyl methacrylate), rubber foam, which form a structure of the foam in which the cellulose can be housed. Depending on the selected foam material, it can be said that the foam is a plastic foam or, alternatively, a rubber foam, eg a latex foam. The importance of moisture uptake will then depend on the raw material and the method used to produce the foam because the reversible ability to absorb moisture is achieved by incorporating or interlocking the cellulose. It is preferable to use open-cell type foams which allow a smooth exchange of air with the ambient atmosphere. It is also essential to ensure that the cellulose is uniformly distributed in the foam structure as described above in connection with the tests performed. If the foam does not have an open-celled structure, it can be treated specifically using known methods to obtain open cells.
    If polyol is used as the starting material for one of the reaction components, the cellulose can be added prior to the foam manufacturing process. The cellulose can be added by keeping it under agitation or by dispersing it using methods known in the industry. The polyol employed is that which is necessary for the corresponding type of foam and is added in the required amount specified in the formula. However, the moisture content of the cellulose particles must be taken into account when establishing the formula.
    As explained above, the particles 11 are preferably introduced and replaced by the components that make up the plastic foam prior to the foam manufacturing process. In order to achieve a uniform distribution within the usual liquid base material, it is advantageous that the difference between the volume weight or the density of the particles 11 and the initial material used to make the plastic foam, for example the polyol, is in the range of ± 10%, preferably ± 0.5% to ± 3.0%. This is particularly advantageous if the particles 11 and the initial material used to make the plastic foam, for example the polyol, have respectively a volume by weight or a density which are approximately the same. This avoids undesired sagging and ensures even distribution of the particles 11 within the plastic foam to be produced.
    For reasons of quality, it is currently a question of opting for a density of 45 kg / m3 and more in the case of mattresses.
    The polyol is added to a mixing vessel using metering pumps in a measured amount ranging from 60 kg / min to 150 kg / min and at a temperature between 18 ° C and 30 ° C. The specified amount of polyol must be maintained accurately so that the particles 11 to be mixed, especially the cellulose, can be added in a defined mixing ratio. The proportion of polyol / particle mixture 11 is: 5 parts + 1 part / 2 parts + 1 part. The particles 11 are not introduced by means of a screw conveyor grounded and operated at slow speed because the entire mixing zone is in an environment protected against explosions. A mixture of particles 11, especially cellulose powder, in contact with the air gives rise to an explosive dust when used according to a specific mixing ratio.
    The amount of the particles 11, such as the cellulose powder, is added to the polyol at a determined speed ranging from 3 kg / min to 6 kg / min so as to ensure that the continuous distribution of the solvent in the drum region results in a non-agglomerated dispersion. The finished dispersion is mixed for a period of time between 10 minutes and 20 minutes. In order to achieve optimal nucleation, the dispersion is degassed using a vacuum of -0.6 bar for 3 minutes. In other cases, an opposite steam load in the mixture would cause problems during the foam production process.
    Another important factor is the moment in which the transformation takes place once the dispersion has been formed. The transformation must take place during a period of 1 and 3 hours. If the transformation does not take place during this period, the density (kg / m3) of the foam to be produced may not be consistent with the desired value and will therefore exhibit pronounced variations.
    The material heated by the mixing process is brought back to a processing temperature of between 20 ° C and 25 ° C. From this point, the polyol-particle dispersion mixture is ready to be processed in the machine for producing the foam.
    When establishing the production formula of the foam to be produced, it is necessary to take into account the current climatic conditions, such as the air pressure and the relative humidity of the air. It is also necessary to take into account the moisture present in the cellulose powder prepared during the calculation of the components. The temperature of the raw material should also be taken into account for the appropriate area of the mixture to be foamed. "Insufficient foaming" would cause defects inside the block. This can be prevented by altering the amount of amine added. The nature of the open cells can be regulated by adjusting the tin catalyst, thus allowing the production of non-irritating blocks. A foam of optimal quality can be obtained in this way.
    A variation in the pressure of the mixing chamber between 1.1 bar and 1.8 bar causes a change in the size of the cells so as to produce the structure of the desired foam.
    Another important factor for an ideal foam manufacturing process is the speed of the conveyor belt along with the amount ejected. For example, the release rate is between 2 m / min and 5 m / min for an ejection amount of between 60 kg / min and 150 kg / min.
    In addition to producing blocks with an optimal rectangular shape, the Planiblock system also allows uniform distribution of hardness, density and particles 11, especially cellulose, through the section or volume of the block. foam in its entirety.
    The blocks are processed and cooled in storage rooms protected from atmospheric conditions. To do this, long cooling periods of at least 20 hours give the best results.
    These crude blocks in which the particles 11 are incorporated are then stored for further processing. The particles 11 contained in the foam do not affect the subsequent processing of the foam.
    The foam is preferably cut on different machines with a circular section band measuring system. In addition to facilitating straight cutting on horizontal cutting machines and vertical cutting machines, it is also possible to cut more complicated shapes in two- and three-dimensional directions on CNC automatic copiers and on CNC machines. cutting of special shapes.
    It may also be advantageous for aloe vera to be added to the foam, particularly to the plastic foam and / or the particles 11 and / or the coating 12 as an ingredient or active ingredient. This can be achieved by adding or mixing it and thus replacing one of the initial bases or materials used to make the foam, especially to the plastic foam and / or the particles 11 and / or the coating 12 during the process of manufacturing. Regardless of what is said above, however, it is also possible to add aloe vera as an ingredient or active ingredient to the foam, especially to the plastic foam and / or particles. and / or the coating 12 afterward using a wide range of known methods. These may include a spraying process or immersion process in an immersion tank, for example.
    The foam member may be used to manufacture individual plastic foam products, particularly plastic and the products may be selected from the group consisting of mattresses, seats or vehicle seat parts such as cars, trains, trams, airplanes, camping equipment, parts of coatings for motorized vehicles such as door coverings, roof coverings, the covering of a luggage compartment, the coating of the engine compartment, foot soles and other parts of footwear such as insoles for footwear, seat belt pads, helmet pads, upholstery, pillows and cushions, padding for medical devices.
    The exemplary embodiments illustrated as examples represent possible variants of the foam element having a hydrophilic substance in the form of cellulose incorporated into the plastic foam, and it should be noted at this stage that the invention is not limited to these illustrated variants, but rather that these individual variants can be used in different combinations with each other and that these possible variations are within the abilities of those skilled in the art given the technical teaching which is provided. Similarly, all the conceivable variants that can be obtained by combining the individual details of the variants described and illustrated are possible and are included within the scope of the invention.
    The basic purpose of independent inventive solutions can be found upon reading the description.
    List of reference numbers 1 Line chart 2 Line chart 3 Line chart 4 Line chart 5 Bar chart 6 Bar chart 7 Foam element 8 Cell 9 Cell wall 10 Cellular network 11 Particle 12 Coating
    权利要求:
    Claims (29)
    [1]
    A foam member (7) made from a foam and particles (11) of at least one hydrophilic substance, the foam member (7) containing the particles (11) having a reversible ability to absorb the moisture, characterized in that at least a partial amount of the particles (11) is completely lodged in the foam and another partial amount of particles (11) is deposited so as to protrude from a surface (13) of the foam in that the foam without hydrophilic substance has an absorption capacity of greater than 2.8% by weight corresponding to an equilibrium moisture at a temperature of 23 ° C and a relative humidity of 93% and a proportion of the particles (11) with reference to the total weight of the foam is in a range whose lower limit is 0.1% by weight and the upper limit is 35% by weight.
    [2]
    Foam element (7) made from a foam and particles (11) of at least one hydrophilic substance, the foam element (7) containing the particles (11) having a reversible ability to absorb the moisture, characterized in that at least a partial amount of the particles (11) is completely lodged in the foam and another partial amount of particles (11) is deposited so as to protrude from a surface (13) of the foam in that the foam without hydrophilic substance exhibits an absorption capacity of greater than 2.8% by weight corresponding to an equilibrium moisture at a temperature of 23 ° C and a relative humidity of 93%, in that the particles are made from wood and in that the particle size is less than 400pm.
    [3]
    Foam element (7) as claimed in claim 1, characterized in that the foam element (7) replaced by the particles (11) exhibits a hardness of compression, during a compression of 40%, within a range with a lower limit of 1 kPa and an upper limit of 10 kPa.
    [4]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the compression hardness of the replaced foam element (7) is within a range whose lower limit is 2.5 kPa and the upper limit is 3.5 kPa.
    [5]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the foam element (7) replaced by the particles (11) exhibits elasticity, based on on the ball test in accordance with EN ISO 8307, the lower limit of which is 5% and the upper limit is 70%.
    [6]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the foam replaced by the particles has a moisture absorption capacity greater than 3.5%. by weight which corresponds to an equilibrium moisture at 23 ° C and a relative humidity of 93%.
    [7]
    Foam element (7) according to claim 1, characterized in that said particles constitute 5 to 20% of the total weight of the foam.
    [8]
    Foam element (7) according to one or other of the preceding claims, characterized in that the density of the foam replaced by the particles is greater than 45 kg / m3.
    [9]
    Foam element (7) according to one or other of the preceding claims, characterized in that said particles comprise cellulose hyperabsorbers.
    [10]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the particles (11) are made from cellulose and are selected from a type of structure based on the modification crystalline cellulose - I and / or cellulose - II.
    [11]
    Foam element (7) as claimed in claim 10, characterized in that the cellulose is employed in the form of cut fibers characterized by a length of fibers the lower limit of which is 0.1 mm and the upper limit is of 5 mm.
    [12]
    Foam element (7) as claimed in claim 10 or 11, characterized in that the cellulose is used in the form of crushed fibers characterized by a particle size whose lower limit is 50 μτη and the upper limit is 0.5 mm.
    [13]
    Foam element (7) as claimed in claim 10, characterized in that the cellulose is employed in the form of spherical cellulose particles.
    [14]
    Foam element (7) as claimed in claim 13, characterized in that the cellulose particles have a particle size of which the lower limit is 1 μm and the upper limit is 400 μm.
    [15]
    Foam element (7) as claimed in claim 13 or 14, characterized in that the cellulose particles have a crystallographic ratio (1: d) whose lower limit is 0.5, especially 1, and the upper limit is 5, especially 2.5.
    [16]
    Foam element (7) as claimed in one of claims 10 to 15, characterized in that a proportion of the cellulose with reference to the total weight of the foam is selected to be between a lower limit 0.1% by weight, most preferably 5% by weight, and an upper limit of 25% by weight, most preferably 20% by weight.
    [17]
    Foam element (7) as claimed in one of claims 10 to 16, characterized in that the cellulose contains additives selected from the group comprising pigments, inorganic substances, such as titanium oxide. , substoichiometric titanium oxide, barium sulfate, ion exchangers, polyethylene, polypropylene, polyester, carbon black, zeolite, activated carbon, polymeric hyperabsorbents and flame retardants.
    [18]
    18. Foam element (7) as claimed in claim 2, characterized in that the particles (11) of the woods are coated with a substance for inhibiting decomposition, more particularly in that they are impregnated therein.
    [19]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the particles (11) are provided with a coating exhibiting a high permeability to moisture and vapor. of water.
    [20]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the difference between the volume weight or density of the particles (11) and the polyol used to make the plastic foam is included in a range of ± 10%, preferably ± 0.5% to ± 3.0%.
    [21]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the particles (11) and the polyol used to make the plastic foam have a weight in volume or a density which are approximately identical .
    [22]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that the structure of the foam is provided with a coating (12) comprising a fluid exhibiting a high permeability to the foam. humidity and that the coating (12) is also replaced by the particles (11).
    [23]
    Foam element (7) as claimed in claim 22, characterized in that a part of the particles (11) is entirely housed in the coating (12) and in that another part of the particles (11) is arranged to protrude from the surface (14) of the coating (12).
    [24]
    Foam element (7) as claimed in one of the preceding claims, characterized in that aloe vera is added to the foam and / or the particles (11) and / or the coating (12). as an active ingredient.
    [25]
    Foam element (7) as claimed in claim 5, characterized in that the foam replaced by the particles (11) exhibits an elasticity measured by means of the ball test according to the EN standard. ISO 8307, whose lower limit is 25%, preferably 35%, and the upper limit is 60%, preferably 50%.
    [26]
    Foam element (7) as claimed in one of the preceding claims, characterized in that the foam is selected from a group comprising polyurethane foam (PU foam), polyethylene foam, foam of polystyrene, polycarbonate foam, PVC foam, polyimide foam, silicon foam, PMMA (polymethyl methacrylate) foam, rubber foam.
    [27]
    Foam element (7) as claimed in any one of the preceding claims, characterized in that another partial amount of the particles (11) is accommodated in the cellular structure of the foam.
    [28]
    Foam element (7) as claimed in claim 26 or 27, characterized in that the foam has an open-celled structure.
    [29]
    Use of a foam member (7) as claimed in any one of claims 1 to 28 in the manufacture of a foam product, characterized in that the foam product is selected from the group consisting of mattresses, seats or parts of seats for vehicles such as cars, trains, trams, airplanes, camping equipment, parts for motor vehicles such as door coverings, roofs, the covering of a luggage compartment, the covering of the engine compartment, the soles of shoes and other parts of the footwear such as insoles for footwear, pads for seat belts, ear cushions for helmets, upholstery of furniture, pillows and cushions, padding for medical devices.
    类似技术:
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    同族专利:
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    法律状态:
    2022-01-10| HC| Change of name of the owners|Owner name: NEVEON AUSTRIA GMBH; AT Free format text: DETAILS ASSIGNMENT: CHANGE OF OWNER(S), CHANGE OF OWNER(S) NAME; FORMER OWNER NAME: EUROFOAM GMBH Effective date: 20211123 |
    优先权:
    申请号 | 申请日 | 专利标题
    AT1012009|2009-01-22|
    ATA101/2009A|AT507850B1|2009-01-22|2009-01-22|FOAM ELEMENT WITH HYDROPHILES INSERTED IN IT|
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