• 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:
    Method for producing a concrete building material, in particular a fiber concrete, particularly preferably an ultra-high-performance fiber concrete, for a construction site comprising the steps of: filling a coarse-grain bulk material mixture into a coarse-grain bulk material container (6); - Filling a fine grain bulk material mixture in a fine grain bulk material container (7), wherein the fine grain bulk mixture comprises a binder; - Processing the coarse grain bulk mixture and the fine grain bulk mixture with the addition of water to the concrete building material.
    公开号:AT518345A1
    申请号:T50096/2016
    申请日:2016-02-15
    公开日:2017-09-15
    发明作者:
    申请人:Dipl Ing Franz Götschl；Dipl Ing Dr Techn Lutz Sparowitz；
    IPC主号:
    专利说明:

    The invention relates to a method for producing a concrete building material, in particular a fiber concrete, particularly preferably an ultra-high-performance fiber concrete, for a construction site.
    In construction, different concretes are used depending on the application.
    In the case of so-called delivery or ready-mixed concrete, the entire production process takes place in a ready-mixed concrete plant. The fresh concrete is often transported after mixing in truck mixers over relatively long distances to the site. Because the chemical hydration process starts with mixing, there is only a limited time window available for transport and installation.
    On the other hand, construction site concrete is also processed, which is produced directly on the construction site. The construction site concrete can be used if the access routes from the stationary concrete plant are too long. Construction site concrete is also sometimes used on major construction sites.
    In the recent past, novel concrete technologies have been developed for which the existing manufacturing processes have proved to be of little benefit. Fiber concrete, which is a high-end product of the current concrete technology in the form of Ultra High Performance Fiber Reinforced Concrete (UHPC), is particularly affected by this • UHPC can be self-compacting and flowable, allowing UPHC to be poured into very tight shapes • UHPC is essentially impermeable to the ingress of liquids and gases • UHPC has very high mechanical resistance, especially in terms of compressive strength, Compound resistance and abrasion resistance • UHPC is particularly resistant to chemical agents such as chloride (in the form of road salt, seawater, etc.) • The durability of UHPC is very high, comparable to granite • The useful life of UHPC structures is much longer than at comparable Structures made of normal concrete or steel. • When UHPC is applied to existing concrete structures, a positive connection with the substrate can be achieved. The resulting concrete body is similarly stable as in a one-piece production.
    The outstanding mechanical properties of UPHC, however, contrast with its comparatively complicated handling, which is not sufficiently taken into account with the existing manufacturing processes. On the one hand, the use of UHPC as delivery or ready-mixed concrete is not desirable because the desired properties of the UHPC over the delivery route can not be reliably guaranteed in all cases.
    On the other hand, dry blends are available, which can be processed with the addition of water directly on the construction site to fiber concrete. However, a disadvantage is the high cost of these ready mixes, which have contributed to the fact that UHPC has been used only to a limited extent.
    The object of the present invention is to alleviate or remedy the disadvantages of the prior art.
    The invention is therefore particularly aimed at providing a method with which an economical production of concrete building materials under controlled conditions is made possible.
    This object is achieved by a method according to claim 1, a coarse grain bulk container according to claim 11, a fine grain bulk container according to claim 12 and a transport and
    Mixing vehicle according to claim 13 solved. Preferred embodiments of the invention are indicated in the dependent claims.
    Accordingly, the method according to the invention has at least the following steps: filling a coarse-grain bulk material mixture into a coarse-grain bulk material container; - Filling a fine grain bulk mixture in a fine grain bulk container; - Processing of the coarse grain bulk mixture and the fine grain bulk mixture with the addition of water to the concrete building material.
    The invention is based on the surprising finding that the division of the dry starting materials for the concrete building material into a coarse-grain bulk material mixture and a fine-grain bulk material mixture in particular brings about an advantageous reduction of the drying effort. The coarse-grain bulk material mixture is filled into the coarse-grain bulk material container, the fine-grain bulk material mixture into the fine-grain bulk material container separated therefrom. Thus, the coarse grain bulk mixture and the fine grain bulk mixture can be transported in a separate state. The coarse grain bulk mixture has a larger average grain size than the fine grain bulk mixture. The advantage of this embodiment is, in particular, that higher demands are placed on the degree of drying of the fine grain bulk material mixture. This is especially true because the fine grain bulk material mixture has the binder, which sets in the processing of the dry ingredients with the addition of liquid ingredients, especially water, to the concrete building material and develops the required strength. In order to prevent partial setting of the binder during storage and transport, it is essential to fill the fine grain bulk mixture including the binder in a highly dry ("dust dry") condition into the fine grain bulk container In particular, the coarse-grained bulk material mixture may be free of binders, in particular free of cement. As a result, the expenditure for drying the starting materials of the concrete building material can be substantially reduced can be processed into the concrete construction material shortly before the intended use by adding the liquid constituents, in particular water.
    According to a preferred embodiment, the processing of the coarse-grain bulk material mixture and the fine-grain bulk material mixture to the concrete building material takes place on the construction site. In this embodiment, a site concrete or in-situ concrete is provided. Accordingly, the coarse-grained bulk material mixture and the fine-grained bulk material mixture are processed in the immediate spatial environment of the site where the concrete building material is to be used for the construction or renovation of a building. For this purpose, the coarse grain bulk mixture and the fine grain bulk mixture are mixed together with the addition of liquid ingredients, especially water. By processing on the construction site, the desired properties of the concrete building material can be precisely adhered to. Impairment of the concrete properties (keyword: elephant skin formation) due to chemical processes during transport can be reliably avoided.
    According to a further preferred embodiment, the filling of the coarse-grain bulk material mixture into the coarse-grain bulk material container and / or the filling of the fine-grain bulk material mixture into the fine-grain bulk material container is carried out in one factory. This embodiment has the particular advantage that the mixing of the dry constituents of the concrete building material takes place under precisely controllable conditions in the factory. The coarse-grain bulk material mixture and the fine-grain bulk material mixture are delivered separately to the construction site and processed there to form the concrete building material. Especially at UHPC, specialized personnel are required to produce the desired bulk material mixes. Advantageously, in this embodiment, specialized personnel are required only in the factory, whereas the processing of the dry bulk mixtures on site requires no special knowledge.
    According to a further preferred embodiment, the coarse-grained bulk material mixture has a proportion of more than 60% by mass, preferably more than 75% by mass, particularly preferably more than 90% by mass, in particular more than 99% by mass, of an aggregate with grain sizes of more than substantially 0 , 04 mm, preferably of more than substantially 0.05 mm, more preferably of more than substantially 0.06 mm. Accordingly, the coarse-grained bulk material mixture consists of more than 60 percent by mass, but preferably to a much higher proportion, of an aggregate whose particle sizes are consistently greater than substantially 0.04 mm, but preferably greater than substantially 0.06 mm. However, the coarse-grained bulk material mixture may have comparatively small proportions of constituents which have a particle size below the stated limit values. For the purposes of this disclosure, the grain size is the equivalent diameter, i. the corresponding diameter of a perfect sphere, understood. The equivalent diameter is determined in particular as a screen diameter.
    Particularly preferably, the grain sizes of the aggregate of the coarse-grained bulk material mixture are smaller than substantially 10 mm, particularly preferably smaller than 9 mm, in particular smaller than substantially 8 mm. Furthermore, it is advantageous if the aggregate has a particle size distribution, i. is blended along a grading curve. As a result, in particular optimal compaction of the concrete building material can be ensured.
    The process according to the invention can be used with particular advantages in the production of fiber concrete, in particular UHPC. In this embodiment, the coarse grain bulk mixture contains fibers, in particular steel fibers. In the prior art, the fibers are supplied to the fresh concrete in a mixer until the end of the mixing process. Then it has to be mixed until the fibers are evenly distributed in the concrete. In the embodiment described above, the fibers can already be well mixed or homogenized with the aggregates during the mixing together of the coarse-grain bulk mixture, which is preferably carried out in the central plant. This eliminates this delicate mixing process on the site.
    As fibers steel fibers are preferably provided. The advantage of steel fibers lies in the fact that steel shows a pronounced flowability before the tensile failure. This allows the steel fibers to transfer tensile forces obliquely across cracks, causing plastic deformation.
    According to a further preferred embodiment, the fine-grained bulk material mixture has a proportion of more than 60% by mass, preferably more than 75% by mass, more preferably more than 90% by mass, in particular more than 99% by mass, of a fine-grained mixture with particle sizes of less than substantially 0, 2 mm, preferably less substantially 0.15 mm, in particular smaller substantially 0.125 mm, on. Accordingly, the fine-grain bulk material mixture consists of more than 60% by mass, but preferably to a much higher proportion, of a fine-grain mixture whose particle sizes are consistently smaller than substantially 0.2 mm, but preferably smaller than substantially 0.125 mm. However, the fine grain bulk material mixture may have comparatively small proportions of constituents which have a particle size above the stated limit values.
    The fine-grain mixture preferably comprises a rock flour. Furthermore, it is advantageous if the fine-grain mixture has a particle size distribution, i. is blended along a grading curve, whereby the advantageous properties of UHPC can be optimally utilized.
    The advantages of the method according to the invention can be utilized, in particular, by virtue of the fact that the binder comprises cement, in particular also microsilica and / or nanosilica. Accordingly, the fine grain constituents of the concrete building material are summarized in the fine grain bulk mixture, which in their own, i. completely separated from the coarse grain bulk container,
    Fine grain bulk container is filled. By separating the solid ingredients of the concrete building material based on their grain size, the energy expenditure in the production of concrete structural material can be significantly reduced, since only the components of the fine grain bulk material mixture including the binder are subjected to intensive drying, whereas the coarse grain bulk mixture with a certain residual moisture in the Coarse grain bulk containers can be filled. This residual moisture can already be measured in the respective storage tank and taken into account when dosing the water at the construction site.
    Furthermore, it is advantageous if the fine-grain mixture contains a flow agent in the dry state and / or a retarder in the dry state and / or a defoamer in the dry state. In the case of a UHPC, the water content should be limited as far as possible to the chemically required minimum. Therefore, a high performance superplasticizer known in the art is required to process the fresh concrete, i. sufficiently fluid to do. By also known per se-retarder the time is extended within which the concrete must be installed. When the concrete is completed near the installation site, a retarder is usually not required. In such cases, it may even make sense to use a Abbin-de-accelerator, for example, if the young concrete is to be charged early. With the help of known defoamers, the foam formation on the concrete surface can be reduced.
    In the method described above, a coarse grain bulk container, in particular a big bag, can be used, which is filled with a coarse grain bulk mixture which has a proportion of more than 60% by mass, preferably more than 75% by mass, particularly preferably more than 90% by mass, in particular of more than 99% by mass, of an aggregate having particle sizes of more than substantially 0.04 mm, preferably of more than substantially 0.05 mm, particularly preferably of more than substantially 0.06 mm.
    Furthermore, in the method according to the invention, a fine grain bulk material container, in particular a big bag, which is filled with a fine grain bulk material mixture which contains more than 60% by mass, preferably more than 75% by mass, particularly preferably more than 90% by mass, can be used. in particular of more than 99% by mass, of a fine-grain mixture having particle sizes of less than substantially 0.2 mm, preferably less than substantially 0.15 mm, in particular less than substantially 0.125 mm.
    According to a particularly preferred embodiment, the concrete building material produced according to the above method comprises fresh concrete, i. before hardening, the following components.
    Coarse grain bulk mixture:
    Fine-grain bulk material mixture
    Liquid ingredients
    The processing of the coarse grain bulk mixture and the fine grain bulk material mixture to the concrete building material may preferably be carried out in a transport and mixing vehicle, with a storage facility for fine grain bulk containers and for coarse grain bulk containers, with a mixing device for processing the coarse grain bulk mixture and the fine grain Bulk mix to the concrete building material.
    The processing of the coarse-grain bulk material mixture and the fine-grain bulk material mixture in the transport and mixing vehicle can be substantially simplified if a conveyor, in particular a trolley unit, for conveying the coarse-grain bulk material container and / or the fine grain bulk material container provided by the storage device to the mixing device is. The trolley unit preferably has a guide rail, which extends in particular substantially in the longitudinal direction of the transport and mixing vehicle, along which a trolley together with coarse grain bulk goods container and / or fine grain bulk goods container is movable. Preferably, two trolley units, one trolley unit each for the longitudinal transport of the coarse-grain bulk mixture and a trolley unit for the longitudinal transport of the fine-grain bulk mixture, are provided.
    According to a further preferred embodiment, the mixing device has a planetary mixer. Such planetary mixers are well-known per se in the art (see, for example, DE 10 2012/210558 A1), so that further details on this can be dispensed with. In the planetary mixer, mixing elements in the form of a center rotation preferably run around a central axis of rotation and a planetary rotation about a planetary rotation axis. The angular velocities of the two partial rotations which define the cycloids, more precisely the epicycloid path of the mixing elements, are constant, so that the web speed of the mixing elements is also constant.
    According to a further preferred embodiment, the mixing device has a colloidal mixer. Such Kolloidalmi shear is described for example in DE 20 2010 003100 Ul. The colloidal mixer preferably has a mixing trough in which a premixing zone and below a dispersing zone are formed. In the premixing zone in this embodiment, a premixing device for mixing in solid is provided, and in the dispersing zone a dispersing device for a colloidal digestion.
    According to a particularly preferred embodiment, the liquid constituents, in particular water, and then the fine-grained bulk mixture are first added to the colloidal mixer and homogenized to form a suspension. The fine grain
    Bulk mixing may already contain the flux in the dry state, further simplifying on-site processing. Alternatively, however, the flux may be added as a liquid component, requiring a metering device to be present on site, which complicates processing but provides more flexibility in formulations. Subsequently, the suspension is passed into a second mixing unit, in particular a planetary mixer, where it is mixed with the coarse grain / bulk material mixture. Advantageously, the colloidal mixer and the planetary mixer can work in parallel.
    In an alternative embodiment, the colloidal mixer is omitted, wherein first the water with the fine grain bulk mixture and then the coarse grain bulk mixture is introduced into the planetary mixer.
    For self-sufficient processing of the starting materials in the concrete building material, it is advantageous if the transport and mixing vehicle has a water tank and optionally at least one container for at least one liquid addition, in particular a flow agent.
    Furthermore, at least one metering unit is preferably provided for metering water out of the water tank and optionally from liquid addition from the container into the mixing device.
    The invention will be further elucidated on the basis of a preferred embodiment, to which it is not intended to be limited. In the drawing shows:
    1 is a functional diagram of a plant for filling a coarse-grained bulk material mixture in coarse-grain bulk material container and a fine-grain bulk material mixture in fine grain bulk material container.
    Fig. 2 and Fig. 3 are schematic views of a transport and mixing vehicle according to the invention, with which the coarse grain or fine grain bulk containers transported to a construction site and there the concrete material is produced;
    Fig. 4, 5 are schematic views of a transshipment process of pure transport vehicles in the transport and mixing vehicle according to the invention as shown in FIG. 2, 3;
    Fig. 6 shows schematically a construction site on which the concrete building material is used.
    In Fig. 1, a stationary metering and mixing plant, hereinafter referred to as premix plant or plant 1, shown schematically, with which two different bulk mixtures for the production of fiber concrete in their own bulk material containers are filled.
    As can be seen from FIG. 1, the plant 1 (shown only schematically) storage container 2a, 2b, 2c, 2d, 2e, 2f, 2g, 2h for the different proportions of the bulk material mixtures. The storage containers 2a, 2b, 2c contain aggregates, wherein quartz sand with grain sizes of 60 to 250 micrometers in the storage container 2a, quartz sand with grain sizes of 200 to 1000 micrometers in the storage container 2b, basalt split / diabase with grain sizes of 1500 to 4500 in the storage container 2c Micrometer is held. The storage container 2d contains quartz powder with grain sizes of 0.3 to 100 micrometers. The reservoir 2e includes dusty microsilica. In the reservoir 2f a powdered binder, in particular cement, is added. Optionally, a plurality of storage containers 2g are provided which contain dry matter chemicals such as flow agents, retarders and defoamers. Furthermore, a Vorratsbe container 2h is provided for steel fibers. Finally, a reservoir 2i for water, a reservoir 2j for liquid fluid, a reservoir 2k for a liquid antifoam, a reservoir 21 for a liquid setting accelerator may be provided.
    In the illustrated work 1 two different bulk mixtures are prepared and filled into the bulk material container 6, 7 from. The bulk material containers 6, 7 can be filled in succession, but preferably in parallel with different contents.
    On the one hand, a coarse-grained bulk material mixture is produced, which contains the aggregate with particle sizes, in particular between 0.06 mm and 4.5 mm, and the short fiber reinforcement, preferably steel fibers. The various aggregates are dosed after a sieving line and premixed dry with the steel fibers.
    For this purpose, the plant 1 has a metering device 3a with a balance, with which the starting materials from the storage containers 2a, 2b, 2c are provided in the desired amounts. The metering device 3a is set up to dose the starting materials from the storage containers 2a, 2b, 2c according to a predetermined grading curve in order to obtain the desired particle size distribution in the coarse grain / bulk material mixture. Furthermore, a mixing device 4a can be seen schematically, with which the coarse-grain bulk material mixture is premixed. The mixing device 4a are also supplied, preferably via a fiber dosing and vibrating machine 4b, steel fibers from the reservoir 2h. From the mixing device 4a, the bulk material mixture passes into a filling device 5a, with which the coarse-grain bulk material mixture is filled into coarse-grain bulk material container 6. As coarse grain bulk containers in particular so-called big bags (English "Flexible Intermediate Bulk Container", short FIBC) are used.
    On the other hand, a fine grain bulk material mixture is produced, which contains a fine grain mixture of dust-dry fine grains with particle sizes in particular <0.125 mm. The fine grain mixture includes cement, minerals and other additives such as dusty microsilica. Like the coarse grain bulk material mixture, the fine grain mixture is metered and homogenized after a sieving line.
    For this purpose, the plant 1 to a further metering device 3b, with which the starting materials are provided in the desired amounts. The quartz powder from the storage container 2d is fed, optionally via a dry-fire system 3c and a buffer store 3d, to the further metering device 3b. Accordingly, the content of the storage container 2f, optionally via a cement cooling system 3e and a buffer 3f, the further metering device 3b is supplied. The further metering device 3b is also connected to the reservoir 2e, which contains the microsilica. The further metering device 3b is set up to dose the starting materials from the storage containers 2d, 2e, 2f in accordance with a predetermined sieving line in order to obtain the desired particle size distribution in the fine-grain bulk material mixture. In Fig. 1, a further mixing device 4b is schematically shown, with which the fine grain bulk material mixture is premixed. The further mixing device 4b is connected on the one hand to the further metering device 3b. On the other hand, the further mixing device 4b, in particular via a precision metering device 4c for dust-like chemical additions, be connected to the storage containers 2g. From the mixing device 4b, the fine grain bulk material mixture passes into a further filling device 5b, with which the fine grain bulk material mixture is filled into fine grain bulk material container 7. As a fine grain bulk container 7 big bags are used in particular.
    In Fig. 1, the system components for the production of the coarse-grain bulk material mixture with arrow la, the system components for the production of fine grain bulk material mixture with arrow lb, the reservoir 2i, 2j, 2k, 21 for the liquid concrete addition with arrow lc summarized. The filled coarse grain bulk containers 6 are stored in a first warehouse 9, the filled fine grain bulk containers in a second warehouse 10.
    The filled bulk containers 6, 7 are stored in the factory 1 and transported by a special transport and mixing vehicle 11 (see FIGS. 2 to 4) to a construction site. The processing to the concrete building material, in particular UHPC, also takes place in the transport and mixing vehicle 11.
    The volume of the coarse grain bulk mixture in the coarse grain bulk container 6 and the volume of the fine grain bulk mixture in the fine grain bulk container 7 are preferably such that the coarse grain bulk mixture and the fine grain bulk material together with the liquid additions of the contents of a conventional mixer on the Fill construction site. For each mixing batch, the entire contents of two big-bags and the corresponding liquid additions, such as water, possibly flow agents, etc., mixed together.
    The plant 1 can, if necessary, produce big bags around the clock and supply a number of transport and mixing vehicles 11 with filled bulk containers 6, 7.
    When larger quantities of fresh concrete are to be produced, the filled bulk containers 6, 7 can be transported to the construction site by means of air-conditioned trucks 30, where they are transhipped into the transport and mixing vehicle 11 using a forklift 31 and used for the production of the UHPC ( see Fig. 4, 5). Smaller volumes of, for example, less than 10 cubic meters can carry the transport and mixing vehicle 11 itself.
    For the production of a concrete building material, in particular a fiber concrete, particularly preferably an ultra-high-performance fiber concrete, for a building site a method can therefore be carried out with at least the following steps:
    In a premix plant 1 - providing a coarse grain bulk mixture; - mixing the coarse-grain bulk mixture; - filling the coarse grain / bulk mixture in coarse grain
    Bulk goods container 6; - Storage of the coarse grain bulk container 6; - Providing a fine grain bulk mixture; - mixing the fine grain bulk mixture; - Filling the fine-grain bulk mixture in fine grain bulk container 7; - Storage of fine grain bulk containers 7; - optional storage of liquid concrete admixtures (such as water, plasticizers, etc.) in containers.
    Along a transport route between the premix plant 1 and a construction site - transporting the coarse-grain bulk goods container 6 and the fine-grain bulk goods container 7 to a construction site;
    At the construction site: - Process the coarse-grain bulk material mixture and the fine-grain bulk material mixture with the addition of water, possibly other liquid components, to the concrete building material.
    In Fig. 2 to 4, the transport and mixing vehicle 11 is shown schematically, with which the coarse-grain bulk material mixture and the fine-grain bulk material mixture are processed into the concrete construction material.
    As can be seen from FIGS. 2, 3, the transport and mixing vehicle 11 has a storage device 15 for fine grain bulk goods container 7 and coarse grain bulk goods container 6. Furthermore, a mixing device 16 is provided for processing the coarse-grain bulk material mixture and the fine-grain bulk material mixture to the concrete building material. In the embodiment shown, the mixing device 16 has a planetary mixer 17 and a colloidal mixer 18. In addition, a conveyor 19 in the form of trolley units 19a, 19b for conveying coarse grain
    Bulk containers 6 or fine grain bulk containers 7 provided in the isolated state of the storage device 15 to the mixing device 16. The transport and mixing vehicle 11 also has containers 20 for liquid additions, such as a flow agent, in the mixing device 16. Furthermore, a metering unit 21 is provided for metering water and / or liquid addition from the container 20 into the mixing device 16. The fresh concrete is provided at an output device 22. The transport and mixing vehicle 11 further has a water tank 23 and a generator 24, so that, if necessary, a self-sufficient operation of the transport and mixing vehicle 11 is made possible.
    As further apparent from FIGS. 2, 3, a maneuvering table 26 with an enclosure 27 is also provided, which facilitates the loading and unloading of bulk goods containers 6, 7. In particular, a forklift 31 can pass from the transport vehicle 30 via the maneuvering table 26 to the transport and mixing vehicle 11, cf. 4, 5. Furthermore, a control panel 28 can be seen, with which, in particular by means of radio remote control, the mixing plant and the conveyor 19 are actuated.
    In Fig. 6 is shown as an example schematically a construction site 32 for applying a road surface, on which the UHPC is used. The UHPC is made available directly on site at the transport and mixing vehicle 11. At the construction site 32, the processing of the UHPC is done in a conventional manner. Shown is a solidification region 33 of an already produced section of the road surface. A reinforcing mat 34 is provided in the area of the construction site 32, which is next manufactured with UHPC. In the processing of the UHPC, a wheeled excavator 35, a transverse distribution screw 36, a rake roller 37, and a pull-off and vibration shovel 38 are used. Furthermore, a mobile roofing 39 is schematically illustrated.
    权利要求:
    Claims (18)
    [1]
    Claims:
    A process for producing a concrete building material, in particular a fiber concrete, particularly preferably an ultra-high performance fiber concrete, for a construction site comprising the steps of: filling a coarse-grain bulk material mixture into a coarse-grain bulk material container (6); - Filling a fine grain bulk material mixture in a fine grain bulk material container (7), wherein the fine grain bulk material mixture comprises a binder; - Processing of the coarse grain bulk mixture and the fine grain bulk mixture with the addition of water to the concrete building material.
    [2]
    2. The method according to claim 1, characterized in that the processing of the coarse-grain bulk mixture and the fine-grained bulk material mixture to the concrete building material on the construction site (32).
    [3]
    3. The method according to claim 1 or 2, characterized in that the filling of the coarse-grain bulk mixture in the coarse-grain bulk material container (6) and / or the filling of the fine-grain bulk mixture in the fine-grain bulk material container (7) in a plant (7) is made.
    [4]
    4. The method according to any one of claims 1 to 3, characterized in that the coarse-grained bulk mixture has a content of more than 60 percent by mass, preferably more than 75 percent by mass, more preferably more than 90 percent by mass, in particular more than 99 percent by mass Aggregate having grain sizes of more than substantially 0.04 mm, preferably of more than substantially 0.05 mm, more preferably of more than substantially 0.06 mm.
    [5]
    5. The method according to claim 4, characterized in that the grain sizes of the aggregate of the coarse-grain bulk mixture are smaller than substantially 10 mm, more preferably less than 9 mm, in particular less than substantially 8 mm.
    [6]
    6. The method according to any one of claims 1 to 5, characterized in that the coarse-grain bulk mixture comprises a proportion of fibers, in particular steel fibers.
    [7]
    7. The method according to any one of claims 1 to 6, characterized in that the fine-grained bulk mixture has a content of more than 60 percent by mass, preferably more than 75 percent by mass, more preferably more than 90 percent by mass, in particular more than 99 percent by mass Fine-grain mixture having particle sizes of less substantially 0.2 mm, preferably less substantially 0.15 mm, in particular less substantially 0.125 mm.
    [8]
    8. The method according to claim 7, characterized in that the fine grain mixture comprises a rock flour.
    [9]
    9. The method according to any one of claims 1 to 8, characterized in that the binder comprises cement, in particular also micro-silica and / or nanosilica.
    [10]
    10. The method according to any one of claims 7 to 9, characterized in that the fine grain mixture contains a flow agent in the dry state and / or a retarder in the dry state and / or a defoamer in the dry state.
    [11]
    11. Coarse grain bulk goods container (6), in particular big bag, filled with a coarse grain / bulk mixture which has a proportion of more than 60% by mass, preferably more than 75% by mass, more preferably more than 90% by mass, in particular more than 99% by mass, an aggregate having grain sizes of more than substantially 0.04 mm, preferably more than substantially 0.05 mm, particularly preferably more than substantially 0.06 mm.
    [12]
    12. fine grain bulk material container (7), in particular big bag, filled with a fine grain bulk mixture which has a proportion of more than 60% by mass, preferably more than 75% by mass, more preferably more than 90% by mass, in particular more than 99% by mass, a fine-grained mixture having particle sizes of less than substantially 0.2 mm, preferably less than substantially 0.15 mm, in particular less than substantially 0.125 mm.
    [13]
    13. transport and mixing vehicle (11), with a storage device (15) for a fine grain bulk material container (7) according to claim 10 and for a coarse grain bulk container (6) according to claim 11, with a mixing device (16) for processing the coarse grain Bulk mixture and the fine grain bulk material mixture to the concrete building material.
    [14]
    14. Transport and mixing vehicle according to claim 13, characterized by a conveying device (19), in particular a trolley unit (19a, 19b), for conveying the coarse grain bulk goods container (6) and / or the fine grain bulk goods container (7) from the storage device ( 15) to the mixing device (16).
    [15]
    15. Transport and mixing vehicle according to one of claims 12 to 14, characterized in that the mixing device (16) has a planetary mixer (18).
    [16]
    16. Transport and mixing vehicle according to one of claims 12 to 15, characterized in that the mixing device (16) has a Kolloidalmischer (17).
    [17]
    17. Transport and mixing vehicle according to one of claims 12 to 16, characterized by a water tank (23) and optionally at least one container (20) for at least one liquid addition, in particular a flow agent.
    [18]
    18. Transport and mixing vehicle according to one of claims 12 to 17, characterized by at least one metering unit (21) for metering water from the water tank (23) and optionally from liquid addition from the container (20) in the mixing device (16).
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    DE2414074A1|1975-09-25|Concrete prepn. plant for despatch in mobile concrete mixer lorries - has silos for sand, gravel and cement and associated metering devices
    DE3328898A1|1985-02-28|Dry mix for a screed, and process and equipment for producing it
    DE2658162C3|1980-11-06|Method and device for producing and introducing dam construction material and / or backfill material for routes in mining
    DE102017122400A1|2019-03-28|Method and device for providing soil mortar
    DE4447961B4|2004-08-05|Fine cement-binder mixt. - contains finely ground clinker or finely ground foundry sand, and known additives, and agents
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    同族专利:
    公开号 | 公开日
    EP3208061A1|2017-08-23|
    WO2018149899A1|2018-08-23|
    CN110603125A|2019-12-20|
    EP3582940A1|2019-12-25|
    EP3582940B1|2020-09-16|
    AT518345B1|2019-12-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2729597A1|1976-07-06|1978-01-12|Willem Jan Herman Bake|METHOD AND DEVICE FOR PREPARING AND PASTING CONCRETE|
    JP2006249855A|2005-03-14|2006-09-21|Toshiaki Shirota|Concrete raw material and transportation bag for concrete raw material|
    JP2008302958A|2007-06-08|2008-12-18|Shirota Mariko|Container back|
    DE4447872C2|1994-08-12|2003-01-23|Dyckerhoff Ag|Fine cement-binder mixt.|
    DE19826725A1|1998-06-16|1999-12-23|Wilhelm Haase|Speciality mortar dry premix base compositions for use on building sites|
    DE202010003100U1|2010-03-03|2010-05-12|Mat Mischanlagentechnik Gmbh|Colloidal mixer, in particular for the treatment of building materials|
    DE102012210558B4|2012-06-22|2017-05-24|Ernst-Abbe-Fachhochschule Jena|PLANETARY MIXING TOOL|
    DE102013016425A1|2013-10-02|2015-04-02|Dyckerhoff Gmbh|Method for filling cavities with a filling compound|
    CN105345927A|2015-09-30|2016-02-24|许昌金科资源再生股份有限公司|Dry concrete blending process based on ultrasonic waves|
    CN105948652A|2016-05-09|2016-09-21|西京学院|Preparation method of binary high strength and high elastic modulus hybrid fiber reinforced nano recycled concrete|WO2019053495A1|2017-09-13|2019-03-21|Saroj Vanijya Private Limited|Method of producing raw materials for use in producing a dry mix construction material|
    AT520505A1|2017-10-03|2019-04-15|Franz Goetschl|mixing device|
    CH714974A1|2018-05-09|2019-11-15|Baustoffe Schollberg Ag|Ultra-high-performance concrete.|
    DE202019106485U1|2019-11-21|2020-01-21|Holcim Technology Ltd|Concrete plant|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50096/2016A|AT518345B1|2016-02-15|2016-02-15|Process for the production of a concrete building material|ATA50096/2016A| AT518345B1|2016-02-15|2016-02-15|Process for the production of a concrete building material|
    EP17156274.7A| EP3208061A1|2016-02-15|2017-02-15|Method for producing a concrete material|
    PCT/EP2018/053731| WO2018149899A1|2016-02-15|2018-02-15|Method for producing a concrete building material|
    EP18704033.2A| EP3582940B1|2016-02-15|2018-02-15|Method for producing a concrete material|
    CN201880012144.5A| CN110603125A|2016-02-15|2018-02-15|Method for producing concrete building materials|
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