• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A process for the manufacture of shaped articles from waterhardening material reinforced with fibrillated organic films. The process is effected continuously and comprises the following steps: a. forming continuous lengths of networks with a great many meshes; b. simultaneously advancing a plurality of said networks into contact with a water-hardening material so as to form a composite layer, and c. shaping said composite layer into the desired configuration and allowing it to set.
    公开号:SU860689A1
    申请号:SU782703673
    申请日:1978-12-26
    公开日:1981-08-30
    发明作者:Мартин Жозеф Мариа Бейен Ян
    申请人:Стамикарбон Б.В. (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR OBTAINING CONSTRUCTION PRODUCTS
    The invention relates to methods for producing building products from water-cured building mixtures based on cement, gypsum, and the like, reinforced with nets of fibrillated polymer films. A known method for the continuous manufacture of construction products reinforced with asbestos fibers, such as asbestos-cement, by continuous supply of asbestos-cement suspension, compaction and molding of products TI However, asbestos fibers pose a serious danger to the health of personnel engaged in the production and processing of asbestos-cement products Closest to the proposed is a method of obtaining building products by continuously feeding reinforcing nets and combining them with a water-curable mineral mixture with osleduyuschimi seals and moldings. A gypsum-concrete mix is used as a water-borne mineral mixture, and metal meshes are used as reinforcing meshes. Molded products are subjected to cutting and subsequent curing. G23 However, products reinforced with metal nets have a greater thickness and increased rigidity, and are easily corroded, especially in places of reduced thickness. The purpose of the invention is to increase the elastic properties of products and their cheapening. This goal is achieved by the fact that in the method of obtaining building products by continuously feeding reinforcing nets and combining them with a water-curing mineral mixture followed by compaction and molding of the products, the reinforcing nets are obtained by extrusion of an organic polymer film, stretching, fibrillation and stretching, and with water-curing the mixture combines a minimum of five reinforcing meshes. In this case, reinforcing meshes are obtained by extrusion of an organic polymer film from a polymer mixture with additives of an antioxidant and a metal deactivator. In addition, reinforcing meshes are obtained by pulling a polypropylene film at 100-155 ° C. Grids are obtained by stretching a fibrillated organic film in a direction that is oriented somewhat below
    gloom regarding the direction of fibrillation.
    The term cell is used in that context to denote the vacant areas within the bred network and the network bound with wocs.
    The number of networks included in the layer, the number of cells within the networks, a minimum of two per square antimeter, is such that the number of cells per cubic centimeter of the final molded product is at least 100. The number of cells in a given layer size depends on the number of networks, entered per unit thickness of such a layer, the number, size and type of cells per network, and the extent to which networks are increased in size as a result of stretching. The best performance is achieved when the number of cells is (At least -200 per cubic centimeter of the molded product. Even more cells, for example over 300 or more than 500 per cubic centimeter of product, can be used. The introduction of such a large number of cells per unit volume of the molded product has favorable effect on the behavior of products under bending conditions. Thus, in the process of pseudoplastic deformation, very fine multiple cracking occurs, with the result that the product is more It restores its original shape and achieves higher physical characteristics. By multiple cracking it is meant that the product, when bent or stretched, forms discrete cracks at a distance of less than 10 mm from each other, and most generally In case of these cracks, they have a size not exceeding about 3 mm.
    The number of networks included per centimeter of layer thickness preferably exceeds 10, ideally more than 25, and optimum results are achieved when the number of networks per centimeter of thickness exceeds 50.
    It is important that the number of cells in the networks, which are increased in size by stretching the fibrillated organic film, should be at least 2, preferably 3, per square centimeter network meter. This number is determined both by the degree of stretching or enlargement of the fibrillated organic film, and by the number of original cells in the transverse and longitudinal directions. Stretching, which can be carried out in the transverse and longitudinal directions, has a multiplicity of from 1.5 to 150 times, more preferably from 1.5 to 50 times, compared to the original size.
    ideally, the cells have a diameter or smallest size of about 200 microns, preferably greater than 300 microns.
    The percentage (by volume of networks in the final product should be 0.25-20% by volume, preferably 2-15% by volume. Most preferably, the volume percentage of networks is about 3-10% by volume of the final product. Products can also be made while ensuring that the network and cell concentrations described above are only in the surface layer of the molded product, having a minimum thickness of 1 mm, with fewer or no networks in the middle section of the product.
    A network of fibrillated polymer fibers is obtained by extruding an organic polymer material into a film, having a thickness of 11000 μm, preferably 10-200 μm. This extruded film can then be cut into strips of suitable width and stretched, for example, 10 times compared to the original size . This stretching causes the material to go into a state of intrinsic fibrillation. Fibrillation in this case is provided by various, well-known methods, including passing an elongated film on a roll with nails, on a brush or comb, or by acting on a film of shear stress with rolls or air currents. Fibrillation can also be achieved with rotation. In this way, sufficiently long sections of fibrillated organic films can be obtained, which can be directly used in the implementation of the proposed method or reeled on the drum, and then unwound and used in the practical implementation of the method.
    The term long enough or continuous is used in this context to refer to fibrillated organic films as encompassing the use of discrete segments that are fed to a treatment, for example, from a drum, but which have a length many times the length of the final molded product.
    The preferred organic film forming material for making the network is a polyolefin. The network is obtained by extruding a polyolefin; for example polypropylene, in a film that is stretched with a stretch ratio of 6-20, preferably 6-14, and most preferably 8-12 compared with the original size. The temperature of the stretching film should be
    20-160 ° C, preferably lOO-lSO C, but best results are obtained at ISO-ISO C temperatures. It is better that the polypropylene used does not have too high a molecular weight. The melt flow index 1 (at 230 ° C and a load of 2.16 kg) should be 1-5, more preferably 2-4. This characteristic is very important for proper fibrillation. and, therefore, the final properties of reinforced, water-cured products made of these materials.
    The polymer material used to form the fibrillated films may be a polyolefin, but it may also be any other of a whole range of thermoplastic materials that form films and fibers, such as styrene and vinyl chloride polymers or their copolymer. Particularly suitable for these purposes are partially crystalline polymers, such as polyamides and polyesters. Particular preference is given to modified or unmodified polyolefins. Chlorinated polyethylene or polypropylene can be used as the modified polyolefin. Examples of unmodified polyolefins are polyethylene and polypropylene. The most suitable polymer is homopolymer-polypropylene, although it is possible to use also copolymers and block copolymers, for example, with ethylene, as well as mixtures of polymers.
    A polymer can also contain various types of fillers and auxiliary substances, such as carbon black, polar substances, pigments, light and heat stabilizers, and antioxidants. It is important that true stabilizers are introduced into the networks, and favorable results are achieved using a metal deactivator and an antioxidant. These compounds are used in amounts of 0.0012.5% by weight, preferably 0.011% by weight. Best metallodeaktivatorami are kompleksukvdie agents, examples of which are phosphoric acid, citric acid, ethylenediaminetetraacetic acid or its salt, N, N-disalitsilidenetilendiamin, latsitin, gluconic acid, hydrazine derivatives, derivatives oxanilides, particularly "H bis-3, 5 (ditert-butyl-4-hydroxyphenyl) propionyl-hydrazine. Citric acid is preferably chosen as the metal deactivator, regardless of whether or not it is free of water.
    The antioxidant may be an amine, in particular an aromatic and secondary amine, such as N, N-disubstituted p-phenylene diamines, diphenylamine derivatives, aminophenol derivatives, condensation products of aldehydes and amines, or ketones and amines. Used antioxidants also include sulfur compounds, for example, mercaptans, thioethers, disulfides and dithiocarbamates, of which zinc dimethyldithiocarbamate can be an example. It is also possible to use phosphorus compounds, for example, derivatives of phosphoric acid or dithiophosphoric acid. However, preference is given to the group of amines.
    The proposed method also uses 1 film materials that can be treated, for example, with radiation, such as UV light, and corona discharge or by acidification with acids, such as chromic acid, to achieve adhesion between the network and the water-curing mass.
    The nets used can be obtained by stretching the film in the direction of its length or longitudinally followed by fibrillation in the film in a known way. However, the film may be stretched in the width direction, i.e. transversely, prior to fibrillation. The film should be pulled out at its temperature below the melting point of the polymer material. The polymer film to be drawn and fibrillated may be a flat sheet material or may have thickened areas or ribs. Thicker ribs are connected by thinner sections of the film, from which fibrillation can be carried out more easily. These thickened areas, ribs or ridges can be formed from the very beginning in the extrusion process by using an extrusion die of appropriate design, or thinner film sections can be made using rolls. The advantage of the latter is that the direction of the ridges can be easily chosen. It is recommended to choose the cell structure during fibrillation so that the cells are located in the form of parallel rows that pass through the angle of 20-80 to the direction of the film length, and the distance between them so as not to exceed twice the cell size in the longitudinal direction.
    An extruded film can be fibrillated by mechanical means, but spontaneous fibrillation by crystallization is also possible. In the latter case, measures should be taken to ensure that the degree of crystallization is at least 30%, for example, by cooling one of the rolls with which the film contacts. This method is fibril-j
    Casting is preferably used for films that are provided with ridges parallel to each other and. located at an angle of 40-70 to the longitudinal direction. In this case, stretching can be carried out longitudinally, transversely, or in both directions to form a network. Combinations of films obtained in this way, having ridges or fins at different angles to the direction of stretching, provide products with higher strength.
    Networks that are fibrillated in different directions, i.e. longitudinally and transversely, can be used together in the product. The advantage of this design is that the product obtained is characterized by greater isotropy of the strength characteristics. The directions of fibrillation are actually normal to each other.
    The nets used to implement the proposed method can be obtained by weaving long fibers of a fibrillated organic film, having the distance between the fibers necessary for forming the required cell sizes. However, this method does not provide the advantage of directly using fibrillated organic films by stretching them to form a network.
    The water-reducible material with which it is brought into contact with the network contains a water-curable bond, aggregated particles, if necessary, and water. The relative contents may vary over wide intervals, but the ratio between the amount of water and the amount of water-curing binder is generally between 0.2 and 0. The aggregated particles used, in particular sand, must be so small that the average particle size is l is less than 1 mm, and the amount used can vary widely. The ratio between the amount of water-curing binder and the amount of aggregated filler particles is preferably from 0.05 to 3. Various aggregated particles can be added to the water-curing binder — fillers and / or auxiliary substances, including sand, gravel, chalk, crushed quartz, polymeric waste, sulfur, clay, fibers, e-vulcanized or unvulcanized rubber, mineral wool, fiberglass, curing accelerators, pigments and auxiliary agents. Certain advantages are achieved by adding polyvinyl alcohol or polyvinyladetate to a suspension of water and a binder, which contributes to increasing the impermeability of the final product to oxygen. These additives additionally serve to better protect the polymer network from exposure to oxygen diffusing into the product, which is especially important when using polypropylene networks.
    The water-curing material may additionally contain auxiliary substances to improve or speed up its processing into final products. Such excipients will include so-called defloculants (anti-flaking agents) or other surfactants, accelerators or cure retarders, and thickeners. These excipients may also be incorporated into film material from which they can slowly be added in a controlled manner. In addition, other additives, such as flame retardant and / or flame protective substances, may be included in the water-curable material and / or the polymer film from which the networks are made. For example, antimony trioxide and chlorinated and / or brominated compounds can be added to one or both components either together or separately.
    The products produced using this process cannot be manufactured in the usual way using techniques used in the manufacture of asbestos-cement products, according to which the suspension of water-curable material and fibers are mixed to a uniform consistency in conventional rotary-type mixing equipment, and then processed into layers and cured . Such equipment cannot be used in the case of continuous networks or fibers according to the proposed method.
    These difficulties are overcome by forming continuous networks of fibrillated organic films and at the same time pushing many such networks into contact with a water diversion material. The fibrillated organic films can be continuously extruded, stretched and subjected to fibrillation with direct feed to the process. Fibrillated films or nets can also be unwound from the drums on which they are stored and continuously fed into. process. In the latter case, it is preferable that layers of networks are placed on the drum so that they can be unwound both directly and simultaneously brought into contact with the water-curing material with the formation of a layer. To feed more networks, it is possible to simultaneously unwind a number of longitudinal drums. Increasing the size of the fibrillated films with the formation of nets fed into the process can be accomplished by various means known in the technical field under consideration, for example by using wedge-toothed chains. If the film is stretched and fibrillare longitudinally, the nets should be stretched wide. for example, ten times the original width. Since this stretching in widths requires relatively little effort, it is possible to use a method that involves passing the network along curved surfaces or curved sections or stripes, which is a transverse stretching of the network. The advantage of this method is that for similar. transverse expansion does not require any special equipment having moving parts. On the other hand, when the film is stretched and fibrillated in the transverse direction, the required increase should be achieved by longitudinal extension of the network. This can be achieved by faster rotation of the transfer roller in comparison with the feed roller, which leads to faster transport relative to the feed. V After the network has been stretched, they must be secured in the required size, especially in the transverse direction, for example, by heat treatment or the so-called extension spreaders to which the fibers of the network are attached. If necessary, these networks can be made to have thickened areas along the sides of the networks that serve as guides, have a greater thickness and, therefore, higher rigidity. These guides may be attached to the spacer belts. The contacting of the networks with the water-curing material in order to infiltrate the networks can be carried out by various methods. These include casting, in which the slurry of the water-curing material is molded and poured with the aid of a distributor onto the nets during their coiling and advancing through the process. The various components of the water-curing material can also be applied by spraying or spraying. Excess water can be removed, for example, by suction through a porous material, and the resulting network of networks and water-curable material are then compacted with vibration and / or compression, which contributes to better adhesion, after which the layer is formed to achieve the desired configuration of the final shaped product and the layer is allowed to set. It is possible to form a series of such layers, which continuously combine, form, and make it possible to harden in order to obtain a thicker shaped molded product. Together with the nets, one or several different types of film can be introduced and introduced into the layer. These MorvT films are plastic films, or sheets of paper, cardboard and similar materials, or spun, woven or woven fabrics of natural or artificial materials, or metal foil. Films can be produced: imegacimi cells are made if necessary, but the area of these cells should be smaller than that of the network cells. If cells are provided, they can be used to discharge excess water in the event of further processing of the bed. These films can perform a number of different functions, including the function of a covering film or a decorative film on one or on another. both flat or wide sides of the molded product. Such a film can also be used to facilitate the separation of layers in the last stage. The film can also serve as a substrate during the manufacture of the layer or later as a substrate for the product in its final form, and in the latter case the film should not be completely hermetic and a small area per cell may be acceptable. Such a film can also be used to maintain the desired size or increase the networks by fixing them on the film by gluing, stitching, stapling or ultrasonic methods. The networks can also be fixed by using local heating or melting under the influence of high-frequency heating, irradiating hot air, or contacting combustible objects with layers of the networks. The application of these methods also ensures that networks are attached only to each other, to each other, without attaching to the film. In addition, layers of other materials, such as foamed polymers or other foamed, swollen or lightweight materials, can be introduced into the manufactured product. Examples of such materials are expanded polyethylene, polypropylene, polyvinyl chloride, polystyrene, or polyurethane, and mineral materials such as perlite, mineral wool or fiberglass. An additional layer or layers of these materials can give the products insulating properties, as well as provide weight reduction, cost, and improve protection from moisture, shock, or jolts. These additional layers or sheets can be fed either continuously, or periodically, or can be obtained on site, after which an additional layer is applied or a sheet of foam material can be worn on the molded layer of water-curing material and networks. If necessary, light and / or foamed or swollen matter can be processed as a filler added to a pre-prepared suspension of a water-curable binder, water and any other filler or extensions. It is also possible to apply separate cement layers with a different composition, for example, one or more cement layers containing glass beads. Thus, one of the positive effects of the invention is from the wideness of the range of modifications and changes that are possible without a significant change in the production process. The proposed method is characterized by flexibility in the sense that it is possible to change the number of networks, the number and nature of Other materials included in the water-curing composition. FIG. 1 shows the scheme for carrying out the proposed method; in fig. 2 is a bend curve for a four-point bend test. The stretched and fibrillated organic film 1 is wound in the form of an endless belt from a drum 2, after which it is given the required width for forming networks with an expander 3 having a curvilinear surface and working in combination with a wedge-shaped toothed chain (not shown). It is possible to jointly feed a multitude of such networks from one drum or from several drums (not shown). If required, another film 5 may be supplied from the drum 4, for example a film of another polymeric material. The additional film itself can have cells, and the network can be attached to the fixture film with device 6 using glue or heat. The networks are then promoted on: a contacting board with a water-drying material, in this case portland cement, sand and water supplied through pipelines 7. In a particular embodiment of the invention, an additional film 9 having a smaller area of Thereafter, one or more networks 11 may be applied to the layer from the drum 10. Additional water-curing material is fed through conduit 7 by spraying, pouring or spraying. The resulting layer is then pressurized to achieve a proper mechanical bond between the networks and the water-curing material. The resulting layer, if required, is molded in tool 12 by crimping and cutting, and then set or hardened in tool 13. The final profile may be a sheet or other profiles, such as a pipe, a corrugated sheet or a box-shaped profile. The layer obtained before curing can also be processed into pipes or other products by wrapping this layer around a mandrel or other shape as the latter is rotated. This can be carried out in continuous mode by slowly moving the mandrel during its rotation. Thereafter, the continuous pipe obtained in this way can be sawn or cut into pieces, followed by curing. It is also possible to lay several layers around the mandrel at different angles, with the result that the product is given increased strength. Used & used to implement this method of winding the net preferably should be one that is relatively weakly enlarged, although the number of cells per cubic centimeter in the final product should still be at least 100 and preferably at least 200. For example, when the network is elongated , race & irenia should be less than 100%. A water-curing material can also be applied to the network by passing networks through a bath containing a suspension of water-curing material. However, in order to achieve the best results, the suspension should contain a surfactant in an amount of 0.01–5 wt.% Based on the weight of the water-cured material, and preferably 0.05–4 wt.%. Examples of surfactants used are sulfonic and urea-formaldehyde resins, cellulose derivatives, and sulfonated melamine-formaldehyde resins. Another means of applying a water-curable material is to spray the slurry into a network or separately apply one or more components of the water-curing material to the network. During the formation of layers, excess water, if any, can be removed with suction devices. When whitening is required, the layer during formation can be supported by an endless rotating flax of cloth or other supporting material which is preferably porous.
    The materials obtained in accordance with the inventive method are characterized by properties that in some respects are much superior to those of ordinary asbestos cement. Products made by the proposed method are characterized by a smooth bending curve, as shown in FIG. 2, where the deflection is represented in the load function. Such a smooth curve of bending is an indication that very fine multiple cracking occurs, which is a characteristic that contributes significantly to the achievement of properties such as tightness and recovery after deflection under load. The proposed method. has the flexibility to allow for many modifications of the nature of the molded products that can be made. Received by; In the proposed method, the products additionally have the advantage that their relatively easy cutting and other processing are possible, and also nails can be driven into them and screws can be screwed in without danger of splitting or knocking out pieces.
    These products can also be used where asbestos-cement products are not applicable due to limitations due to their properties. The use of the materials obtained is assumed mainly in construction, where they are used in the form of sheets, pipes, corrugated sheets, slate, panels, ducts and gutters.
    Example. The sheet is prepared in accordance with the method described above and illustrated in FIG. 1, and only networks obtained from fibrillated organic films are used, the networks are performed by extruding polypropylene having a melt flow index of 2.5 (230 ° C. 2.16 kgf, into the film and stretching the film eight times at a temperature of 140s, which results in a final film thickness of 25 microns.After this, fibrillation is carried out mechanically by means of a roller with brushes, which ensure the formation of a series of parallel The cuts are made at an angle of 43 to the direction of the length of the film. Three films having a total thickness of 75 µm are combined and wound onto drums according to fifteen .. To obtain a reinforced cement sheet, 4 drums are used sequentially, which
    Simultaneous passage through the process of all 18 networks with the formation of a layer and a final sheet.
    The films are wound up from the reels and the width is increased by 6 to 100 cm, and the number of cells in the formation of the nets is 3 cells per square centimeter. Then the film is contacted and impregnated with a suspension of Portland cement grade A, water and sand. Sand particles have dimensions of 100.-200 microns.
    0 The water-cement factor (WCF) is 0.75 and the amount of sand is 20% by weight relative to cement.
    In this way the layer formed
    5 then pressed to a thickness of 6.6 Yul and cut. The SCF for cut sheets is 0.25. The final product contains 5% of polypropylene networks and has 810 cells per cubic centimeter of the final product. After hardening for 18 days at a relative humidity of 9.5%, the following characteristics were measured:
    Bending strength, N / mm (MPa)
    40 10 10 Elastic modulus, Tti / MM
    Tensile strength, N / mm (MPa) Water absorption after hardening for 28 days in water at, vol.% Charpy impact viscosity, N / mm
    40
    Figure 2 shows the curve obtained by constructing the dependence of the load-deflection in bending test
    0 on a four-point scheme. This curve is very smooth without any discontinuities, which indicates a very thin type of multiple cracking. In addition, a good curve is observed in the area of pseudoplastic deformations.
    This thin type of multiple cracking gives a molded product high physical characteristics, including maintaining impermeability, such as water, and the ability of the product to regain its original shape more quickly and more fully after removing the load. This fine type of multiple cracking also allows a more sophisticated safety factor to be used in strength calculations. Along with the above properties, the resulting material has a large number of cells per cubic centimeter of product.
    Formula ° Invention
    1. The method of obtaining construction products putsh (continuous supply of atsti
    权利要求:
    Claims (3)
    [1]
    Claim
    1. The method of obtaining building products by continuously supplying reinforcing nets and combining them with a water-cured mineral mixture with subsequent compaction and molding of products, characterized in that, in order to increase the elastic properties of products and reduce their cost, reinforcing nets are obtained by extrusion of an organic polymer film, stretching , fibrillation and stretching, we take with a water-cured mixture combine at least five reinforcing mesh.
    [2]
    2. The method of pop. 1, characterized in that the reinforcing mesh is obtained by extrusion of an organic polymer film from a polymer mixture with the addition of an antioxidant and a metal deactivator.
    [3]
    3. The method according to PP. 1i2, characterized in that the reinforcement, the grid is obtained by stretching POLYPROM e pilenovoy film at a temperature of 100-155 in S.
    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    AU4258078A|1979-07-05|
    IT1110857B|1986-01-06|
    EG13784A|1982-09-30|
    NO784436L|1979-07-03|
    AU522565B2|1982-06-17|
    PL212294A1|1979-10-08|
    DK583078A|1979-07-01|
    ZA786925B|1979-12-27|
    DD141031A5|1980-04-09|
    IE47688B1|1984-05-30|
    NO148876B|1983-09-26|
    IE782458L|1979-06-30|
    EP0003245A1|1979-08-08|
    GR73134B|1984-02-07|
    NO148876C|1984-01-04|
    FI784053A|1979-07-01|
    JPS5496518A|1979-07-31|
    BR7808618A|1979-07-10|
    ES476271A1|1979-04-16|
    IT7852494D0|1978-12-29|
    US4242407A|1980-12-30|
    PT68960A|1979-01-01|
    YU305578A|1983-01-21|
    DE2861837D1|1982-07-01|
    EP0003245B1|1982-05-12|
    NL7714571A|1979-07-03|
    PL126003B1|1983-06-30|
    CA1122383A|1982-04-27|
    IN150465B|1982-10-16|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    NL7714571A|NL7714571A|1977-12-30|1977-12-30|METHOD FOR MANUFACTURING ARTICLES FROM WATER-CURING MATERIAL|
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