WO1993011085A1 - Planche de platre fibreux et son procede de fabrication - Google Patents

Planche de platre fibreux et son procede de fabrication Download PDF

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Publication number
WO1993011085A1
WO1993011085A1 PCT/EP1991/002215 EP9102215W WO9311085A1 WO 1993011085 A1 WO1993011085 A1 WO 1993011085A1 EP 9102215 W EP9102215 W EP 9102215W WO 9311085 A1 WO9311085 A1 WO 9311085A1
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WO
WIPO (PCT)
Prior art keywords
fibers
gypsum
wetted
mixing
water
Prior art date
Application number
PCT/EP1991/002215
Other languages
English (en)
Inventor
Karl K. SCHÄFER
Gerhard M. Melzer
Jörg SCRIBA
Suda G. Bhagwat
James Eisses
Original Assignee
Carl Schenck Ag
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Carl Schenck Ag filed Critical Carl Schenck Ag
Priority to PCT/EP1991/002215 priority Critical patent/WO1993011085A1/fr
Publication of WO1993011085A1 publication Critical patent/WO1993011085A1/fr

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B1/00—Producing shaped prefabricated articles from the material
    • B28B1/52—Producing shaped prefabricated articles from the material specially adapted for producing articles from mixtures containing fibres, e.g. asbestos cement
    • B28B1/526—Producing shaped prefabricated articles from the material specially adapted for producing articles from mixtures containing fibres, e.g. asbestos cement by delivering the materials on a conveyor of the endless-belt type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B17/00—Details of, or accessories for, apparatus for shaping the material; Auxiliary measures taken in connection with such shaping
    • B28B17/02—Conditioning the material prior to shaping
    • B28B17/023—Conditioning gypsum
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B19/00—Machines or methods for applying the material to surfaces to form a permanent layer thereon
    • B28B19/0015—Machines or methods for applying the material to surfaces to form a permanent layer thereon on multilayered articles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28B—SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B5/00—Producing shaped articles from the material in moulds or on moulding surfaces, carried or formed by, in or on conveyors irrespective of the manner of shaping
    • B28B5/02—Producing shaped articles from the material in moulds or on moulding surfaces, carried or formed by, in or on conveyors irrespective of the manner of shaping on conveyors of the endless-belt or chain type
    • B28B5/026—Producing shaped articles from the material in moulds or on moulding surfaces, carried or formed by, in or on conveyors irrespective of the manner of shaping on conveyors of the endless-belt or chain type the shaped articles being of indefinite length
    • B28B5/027—Producing shaped articles from the material in moulds or on moulding surfaces, carried or formed by, in or on conveyors irrespective of the manner of shaping on conveyors of the endless-belt or chain type the shaped articles being of indefinite length the moulding surfaces being of the indefinite length type, e.g. belts, and being continuously fed
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/04—Waste materials; Refuse
    • C04B18/18—Waste materials; Refuse organic
    • C04B18/24—Vegetable refuse, e.g. rice husks, maize-ear refuse; Cellulosic materials, e.g. paper, cork
    • C04B18/241—Paper, e.g. waste paper; Paper pulp
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
    • C04B28/14—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing calcium sulfate cements
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00612—Uses not provided for elsewhere in C04B2111/00 as one or more layers of a layered structure
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00612—Uses not provided for elsewhere in C04B2111/00 as one or more layers of a layered structure
    • C04B2111/0062—Gypsum-paper board like materials
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/91—Use of waste materials as fillers for mortars or concrete

Definitions

  • the present invention relates to fiber gypsum board (FGB) and composites and the method of manufacturing the same for use as building materials. More particularly, the invention is directed toward a fiber gypsum board and composites that can have a more variable density, and have greater strength. The invention further relates to novel methods, systems, and apparatus for manufacturing FGB and composites.
  • FGB fiber gypsum board
  • a wet slurry of gypsum is poured between two layers of paper and the slurry is allowed a certain amount of time to set up.
  • the two layers of paper contain the slurry and provide the strength required in installation and use.
  • the wallboard is cut into discrete lengths to accommodate subsequent handling and then dried in heated dryers until the board is completely dry.
  • the bending strength of the board depends on the tensile strength of the paper; while the gypsum serves as a "spacer” and accounts for fire resistance and moisture absorbing and moisture releasing activities.
  • the static properties are limited, and the surface treatment and the joint filler system are determined by the paper.
  • a board having a fiber percentage of 22% of the finished board requires 150% by weight of water to 100% fibers, if the fibers are to carry the water for setting the plaster. I the prior art processes, such a high ratio of water to fiber results in balling.
  • Yet another object is to present a semi-dry process for producing gypsum fiber board in which all or part of the setting water is incorporated by fiber moistening.
  • Another object is to provide a process which can produce gypsum fiber board having either a single homogeneous layer or multiple heterogeneous layers.
  • the invention comprises a method of producing gypsum board, the method including the steps of mixing in a preliminary mixing step a predetermined amount of fibers, an absorbent restricting the adhesion of the fibers to one another, and water to form a mixture of wetted, loose fibers; mixing in a final mixing step the wetted fibers with a predetermined amount of dry calcined gypsum; laying the mixed composition into a matt having a substantially uniform consistency; compressing the matt to form a board composed of bonded fibers and gypsum; and drying the board after complete setting of the gypsum to provide a finished board.
  • the fibers can be, for example, recycled paper fibers or reject fibers of pulp production, wood fibers or mixtures thereof with various mineral fibers that are capable of serving as a water carrier.
  • the absorbent in the preferred embodiment is powdered quick lime.
  • one or more vertical mixers are used to mix the fibers with dry calcined gypsum or with dry calcined gypsum and additives, and the resultant homogeneous mixture is then placed onto a conveyor bel or similar surface to form a moving matt.
  • Additives can be adde to strengthen the board, speed the setting and hydration process or provide other desired characteristics. These additives can b metered into the other ingredients by mixing screws, pinwheels, liquid nozzles or similar mixing devices located at various locations along the production line, thereby providing improved control.
  • the invention further comprises a method of producing fiber gypsum board comprising the steps of mixing in a preliminary mixing ste predetermined amounts of fibers and water respectively, to form mixture of wetted, loose fibers; mixing in a mixing step the wetted fibers with a predetermined amount of dry calcined gypsum premixing an accelerator with one of the components of dry calcined gypsum, fiber and water; promptly laying the mixed composition into a matt; immediately degassing the matt in a first compression step, adding a predetermined amount of water onto the resultant matt; and immediately compressing the matt t form a board composed of bonded fibers and gypsum.
  • less than the amount of water needed to hydrate the gypsum to optimum strength is added to the fibers i the preliminary mixing step, thereby minimizing the tendency of the fibers to ball.
  • An absorbent is preferably added to the fibers before or while they are mixed with water.
  • the amount o water needed to hydrate the gypsum to optimum strength is added to the board after the mixture of wetted fibers and gypsum are mixed.
  • the step preferably occurs while or after the matt of t mixture is degassed.
  • the added water is then sucked into the degassed mixture of wetted fibers and gypsum and distributed throughout much, if not all, of the board.
  • the added water can have an accelerator which allows the board to set in an extreme short time.
  • the resultant board has an excellent distribution fibers and gypsum - and is extremely strong.
  • the invention also comprises systems and apparatus for practicing the methods, and gypsum boards made according to the above methods or combination of these methods.
  • the invention thus comprises a gypsum board made of bonded fibers and gypsum and having no exterior paper coating.
  • the invention also comprises multilayered gypsum boards, such as a board having a lightweight inner layer.
  • FIG. IA is a plot of the bending strength of a board mad according to an embodiment of the invention, versus amounts o absorbent added to the board mixture.
  • Fig. IB is a plot of the bending strength of a board mad according to an embodiment of the invention, versus the amoun water used to initially wet the fiber.
  • Fig. 1C is a schematic diagram illustrating certain step an embodiment of a method of the present invention.
  • Fig. ID is a schematic diagram illustrating steps of ano embodiment of a method of the present invention.
  • Fig. 1 is an illustration of a paper preparation area of production line made according to the present invention.
  • Fig. 2 is an illustration of a plaster preparation area production line made according to the present invention.
  • Fig. 3 is an illustration of a solid additive and starch distribution areas of a production line made according to the present invention.
  • Fig. 4 is an illustration of a core layer material preparation area of a production line made according to the present invention.
  • Fig. 4A is an illustration of the plaster distribution bi of the invention.
  • Fig. 5 is an illustration of a wetted fiber and surface layer preparation area of a production line made according to present invention.
  • Fig. 6 is an illustration of a forming station of a production line made according to the present invention.
  • Fig. 7 is an illustration of a pressing area of a product line made according to the present invention.
  • Fig. 8 is an illustration of a cutting and dryer preparat area of a production line made according to the present invention.
  • Fig. 9 is a drying area of a production line made accordi to the present invention.
  • Fig. 10 is an illustration of a final production area of production line made according to the present invention.
  • Fig. 11 is a cross section of a fiber gypsum board made according to the present invention.
  • Fig. 12 is a cross section of a composite board made according to the present invention.
  • Fig. 13 is a cross section of a fiber gypsum board with a decorative texture imprint made according to the present invention;
  • Fig. 14 is a side view and schematic partial cutaways of turbo mill for dissolving and wetting fibers according to the present invention.
  • Fig. 15 is a schematic side view of a mixing station of t present invention.
  • Fig. 16A is a side view of a vertical mixer and the desig of the mixing and cleaning disks.
  • Figs. 16B are partial cutaways of a front and a top view the vertical mixer of Fig. 15.
  • Fig. 17 is a cross section of a fiber gypsum and wood composite board made according to the present invention.
  • Fig. 18 is a cross section of a second embodiment of a gypsum and wood substrate board made according to the present invention.
  • Fig. 19 is a cross section of a third embodiment of a fib gypsum and wood substrate board of the present invention, the board including a decorative coating made according to the present invention.
  • Fig. 20 is a cross section of a fourth embodiment of the present invention, that embodiment including an intermediate fiber gypsum layer bonded to the substrate and a second fiber gypsum layer on the exterior surface.
  • DETAILED DESCRIPTION OF THE INVENTION The general aspects and principles of the invention will first be described, followed by a detailed description of the preferred embodiment of a production line to practice the methods of the present invention and manufacture fiber gypsum boards according to the present invention. When appropriate, reference will be made to the drawings wherein, wherever possible, like reference numbers refer to like parts.
  • the invention relates to a method and system for the manufacture of boards made of gypsum and fibers, particularly the partial or complete incorporation of the setting water of the dry calcined gypsum via fiber moistening.
  • paper fibers are used as the water carrier, although the use of other fibers, such as wood fibers, falls within the scope of the invention.
  • low density porous particles are also used as the water carrier.
  • Fiber moistening is realized by adding absorbents to the fibers that prevent the fibers from balling at a high fiber moisture.
  • the absorbents preferably also reduce the springback of the pressed, but not dry, preform by softening the fiber.
  • the use of the absorbents also significantly increases the strength of the finished board.
  • the setting water is only partially incorporated via fiber moistening and a post moisteni step is carried out after the final wetted fiber and dry calcin gypsum are mixed and just prior to the compression of the resultant preform.
  • the moist fibers preferably are mixed with the dry calcine gypsum at about the same time that the dry calcined gypsum and moist fibers are transferred onto the forming belt. Since the resultant mixture can be immediately pressed, this method permi the maximum acceleration of the dry calcined gypsum by adding accelerating agents to the dry calcined gypsum, the water, the fibers, and/or the absorbent. By adding an extremely fast reacting accelerator with the water for the post-moistening ste extremely fast setting can be accomplished. The setting of the dry calcined gypsum and most of the hydration are essentially carried out within a few minutes while the matt is compressed a relatively short press in a continuous pressing operation. The resultant process thus reduces the springback of the board. It is thus possible to obtain boards having smooth surfaces, limited thickness tolerances without additional sanding and a high strength.
  • the fibers are formed and wetted in rotary mills.
  • metered amounts of absorbents are added simultaneously with the metered feeding o the fiber mills with dry (ambient moisture up to 8%) disintegrated waste paper.
  • the dry fibers are moistened in an air flow inside the mills during or shortly after the milling. This is achieved by spraying water into wing beater or turbo mills as they operate.
  • the present invention can make fiber gypsum boards from a variety of different fibers.
  • the process can use mechanically dewatered waste paper fibers prepared in a wet process, reject fibers from the paper pulp production, or ther mechanically refined wood fibers.
  • Materials of this type requ a dissolving of the fiber conglomerations and possibly further subsequent moistening and subsequent milling.
  • This dissolving and moistening is done in special mills operating on a principl where disintegration (dissolving) is based on air turbulence. These mills are known as turbo mills, and their use will be described more fully below.
  • metered amounts of moistened fibers and dry calcined gypsum are dispensed in layers on a preforming belt. These layers are then vertically mixed and at the same time transferred onto a forming belt on which a matt of mixed dry calcined gypsum and fibers are deposited.
  • dry additives can be added to the dry calcined gypsum or to the absorbent.
  • Moist additives, soluble or liquid can be added to the water or to the moistened fibers, or can be sprayed on the matt.
  • the resultant matt of wetted fibers and gypsum are formed a conveyor belt and are subject to degassing and compression.
  • the degassing is carried out after the matt is formed and is preferably achieved by opposed conveyor belts which preferably are air-permeable belts. As the matt is initially compressed between air-permeable belts which gradually incline toward eac other, the gas is pressed out of the whole mixture.
  • the degassed matt is then compressed in a continuous pres entering the press prior to the initial setting.
  • This press includes a compressing station (to provide the necessary compressive power) and a calibrating station (to compensate th springback pressure - elastic restoring force) .
  • the preforms can be compressed beyond the desired thickness to reduce the springback to a minimum.
  • pressure sensitive additives it is also possible to press by fixed stops only to the desired final thickness of th wet board leaving the press.
  • the adjustment of the accelerati can be made so the setting for the most part can be completed inside the press.
  • the matt as it leaves the compression stati is then substantially set, so that only a minimum force is necessary to hold the matt to the desired thickness, in the calibration station.
  • the final setting can subsequently be carried out on a conveyor belt or on the individual board segments in a stacking feeder 3180.
  • the stacking feeders preferably go into the drier 3181. Since the process permits the maximum acceleration of the setting of the dry calcined gypsum, it is possible to minimize the machinery expenses for the presses, as well as the conveying devices to t drier. Moreover, it is possible to add the setting water in metered amounts at two or more separate steps, which allows working with the minimum of free water to dry out which reduces the energy consumption as well as the machinery expenditures.
  • the present invention solves the problem of fiber balling adding absorbents to the fibers. It is the purpose of the absorbents to restrict the adhesion of the fibers to one anothe Preferably the absorbents absorb the water, and prevent the fibers from adhering to one another. Fine ground materials, li raw gypsum (which at the same time serves to accelerate the setting of the gypsum) , whitening, bentonite, magnesium oxide (MgO) , cement and lime (CaO or Ca(0H) 2 ) , are possible absorbents.
  • MgO magnesium oxide
  • CaO or Ca(0H) 2 cement and lime
  • paper fibers are used.
  • Lime, particularly CaO soft burned (having a very fast reaction time during the conversion into Ca(0H) 2 ) added during the milling of the dry paper showed the best results.
  • One advantage of CaO is the splitting effect of the already fine particles into an even greater number of fine particles when coming in contact with the normal paper moisture. This results in an even better substantial enclosure of the fiber surface (also, the energy consumption of the mill is decreased by "drying out” caused by the absorption of water in the fibers by the CaO.
  • CaO also is less expensive than Ca(OH) 2 ).
  • the high alkalinity of the lime also causes the fibers to soften similar to the chemical (alkaline) refinement of wood during pulp manufacturing which, a an additional object of development, reduces the springback whil pressing and the springback of the pressed but not yet dried board. By this and the softening the strength of the board increases up to 90% at the same density.
  • the amounts of additives required to avoid fiber balling vary depending on the type of fiber and the degree of moisture. For boards made of paper fiber, the amount of lime added to the fiber preferably falls within the range generally between 2 and 20%.
  • the inventors have found that the ratio of water added to the fiber during the preliminary wetting of the fibers has an effect upon the strength of the final fiber gypsum board. This relationship is shown in the plot included at Fig. IB. As the plot shows, if the percentage of water added to fiber exceeds 80%, the strength of the board begins to decrease. At approximately 100%, the drop in strength becomes more sharp. Although these results specifically apply to boards made from dry milled paper fiber, it is believed that similar relationship will apply to boards made from different processed fibers. In view of these results, when the strongest board is desired, it is preferably to keep the water fiber percentage below 100%, and most preferably below 80%.
  • an additional wetting step is used in the preferred embodiment of the method.
  • water is added, for example, sprayed into the falling material during the transfer onto the forming belt, onto the forming belt for the bottom surface and onto the fiber gypsum matt, or between individual layers, before degassing after the wetted fibers have been mixed, or sprayed onto the fiber gypsum matt, after the wetted fibers have been mixed and preferably after the formed matt of wetted fibers and dry calcined gypsum have been degassed.
  • the water added for example, sprayed onto the board, is readily accepted by the board and migrates into the board.
  • a sufficient amount of water is added onto the board to hydrate the board to optimum strength of the board and to ensure that the gypsum receives a sufficient amount of water to fully hydrate.
  • water is sprayed onto the board i is preferably sprayed onto both sides.
  • the total amount of water available for setting of the dry calcined gypsum added in the fiber and to the fiber-gypsum matt is within 35%-50 by weight of the amount of calcined gypsum included in the board.
  • the water ratio itself added to the fiber and to the fiber and the preform can be higher if, e.g., by very low pressure and low density boards the water is not fully available for the setting of the dry calcined gypsum.
  • the above disclosed supplemental watering step provides two related benefits that provide a stronger board.
  • this second water step allows the user to keep the ratio of water to fiber in the fiber wetting step below 100%, most preferably belo 80%. This results in the strongest board, from a water-fiber standpoint.
  • the lower ratio of water to fiber also means that less absorbent, e.g. lime, is necessary to keep the fibers from balling. Therefore, it is possible to use lower percentages of lime and receive the benefit of stronger boards associated with this lower ratio.
  • the recipe for a board can include the most optimum ratios - namely 3-5% of lime to fiber and less than 80% water to fiber in the wetting step. It is expected that the preferred two-step water method of the present invention can be similarly applied to othe fibers and associated absorbents.
  • FIG IC A principal illustration of the preferred manner of effecting the second watering step is schematically shown in Fig IC.
  • the fiber gypsum matt first goes through degassing A statio where the matt is compressed and gas escapes through the air permeable belts of the degassing station.
  • the wetted mixture of fibers and dry calcined gypsum is then further compressed in the degassing B station.
  • a preselected amount of water is then, for example, sprayed onto both sides of the compressed matt, preferably immediately as the matt exits the degassing station B
  • the suction effect will pull in the sprayed water, rather than air.
  • the fiber gypsum matt since the fiber gypsum matt is already moistened it will readily accept the water and transfer it to the middle, as well as the exterior surfaces, of the board.
  • the board After the partially set matt or board receives the additional spray of water necessary to hydrate the calcined gypsum in the board to optimum strength, the board is then introduced into a compressing station C. In the compression station the matt is subjected to high pressure and is compressed to less than the desired thickness of the board and springs back to the desired thickness. The matt is compressed in the compression station C for approximately 1 to 3 seconds per foot, and during this step the compressed fibers release additional water to the dry calcined gypsum and the dry calcined gypsum begins to set*. The board then goes into a calibration station which holds the board at a desired end thickness.
  • fi powdered or liquid chemicals with acidic or alkaline reaction c be added to the fibers by milling or with the water for moistening or additional moistening of the mixture, matt or preform by changing the pH-value and the softening and binding effect.
  • H 2 S0 4 can be added to the water, which also has an accelerating effect on the setting of the dry calcined gypsum.
  • accelerator additives can be introduced into the fiber gypsum mixture, resulting in extremel quick setting of the dry calcined gypsum.
  • These accelerator additives can be added to the wetted fibers before they are mix with the calcined gypsum, or can be added in dry form to the calcined gypsum before it is mixed with the fibers.
  • a sufficient amount of one or more accelerator additives are added to cause the wetted gypsum fiber mixture to set within th desired time period.
  • an extremely fast accelerator is waterglass.
  • Waterglass was previously theoretically known to b an accelerator but was not practically usable because of its fa reacting time which starts the setting after a few seconds.
  • Th process in accordance with the present invention with post moistening makes usage of waterglass as an accelerator possible This is because after adding it on the degassed preform, the ma or board gets compressed to its final thickness immediately or within a few seconds, preferably while the matt or board is moving at a speed of 1 to 3 seconds per foot.
  • Waterglass can be added to the spraying water in Fig. IC a also improves the properties of the board, for example, strengt and moisture resistance.
  • the availability of this quick settin in the present invention permits the creation of a production line in which the matt is substantially set as it exits the calibration station. As a result, the length of the compressio station can be reduced, and considerably less compression is needed in the calibration station. Accordingly, the costs of t equipment needed to compress and calibrate the matt while the d calcined gypsum is setting is substantially reduced.
  • the ratio of fibers to gypsum can vary over a wide range, specifically including the lower percentage required by some fire regulations.
  • the balling of the fibers, when wetted, is prevented by adding a sufficient amount of an absorbent that is capable of restricting the adhesion of the fibers to one another.
  • the ratio of water added to wet the fibers and the rat of the absorbent are preferably kept within ranges that provide the strongest end product.
  • the amount of water wetted to the fiber in the preliminary wetting step is at least sufficient to enable the resultant matt of wetted fibers and gypsum to readil accept additional water that is added in a subsequent spraying step.
  • the matt leaving the degassing station is substantially formed so that the matt has sufficient strength for a free release from the matt-forming belt onto the press-forming belt that water can also be sprayed on both sides of the matt, witho the need of carrier belts between the degassing and the compression stations.
  • the fiber can be milled or dissolved and/or wetted by different machines.
  • wing beater mills can be used, provided that an additional system is added for sprayi in the setting waters in the dry flow of fibers.
  • Solutions wit accelerators, binding agents (for example, starch) , diluted acids, and other additives can be added to the fibers along wit the water.
  • turbo mills For wet-processed waste paper fibers (e.g. from collected household waste paper) , reject fibers of pulp production, or thermomechanically refined wood fibers, turbo mills can be used Turbo mills operate without screens on the backup principle or the turbulence principle in which two-thirds of the disintegration is achieved by the turbulent interaction of the fibers against each other. At the same time, for dry paper or for additional moistening, water is sprayed into the turbo mill.
  • the wetted fibers are preferably layered onto a conveyor belt, and the gypsum is then layered onto the wetted fiber.
  • the thorough mixing of the wetted fibers and gypsum is preferably then carried out in vertical pinwheels.
  • the vertical mixing is best achieved with a particular device which account for the difficult characteristics of the moist fibers. This was accomplished by (horizontally) offset spiked disk rollers which permit a uniform mixing of the moist fibers without the formatio of balls. So-called turbulence disks which engage the spiked disk rollers keep the latter clean.
  • the preferred degassing station has at least one porous bel (and preferably two) installed downstream of, and directly following the last vertical mixers.
  • the formed matt is compressed to nearly desired thickness. To the extent that a springback does occur, the air absorbed thereby can be pressed out again without the formation of bubbles/separations when entering the main rollers of the compression station.
  • the principle applied is the one of a rolling press which is significantly less expensive than, for example, continuous, area specific presses (individual rollers or rods of very thin diameters and support surfaces, in all cases covered with steel bands for these pressure requirements) .
  • roller presses allow the increase of the pressing times to 2 - 3 min and allows the plaster to reach 80 - 90% of the wet strength through a maximum acceleration of the setting process inside the press. This maximum acceleration also significantly reduces- springback and minimizes the amount of compression needed in the calibration step. This facilitates the operation in the calibration statio and allows the creation of boards having a higher strength and smoother surfaces, as well as boards with small thickness tolerances which do not require subsequent sanding of the dry boards.
  • the present invention preferably uses at least two separat watering steps.
  • dry waste paper when dry waste paper is used, it can be moistened up to 150% of water without balling.
  • the fibers preferably are only moistened 80 - 100% and exposed to subsequent moistening which depends on the fiber contents of the preform.
  • the reduced moisture conten of the fibers creates less contamination of the apparatus in contact with the final mixture, especially the mixing heads.
  • F a board having a fiber content of 16% this corresponds to a water-calcined gypsum ratio of 18-22%, hence only slightly abov the stoichiometric amount of water required. It has been found that approximately 45% of water to the dry calcined gypsum shou be added, to ensure the optimum of strength. Therefore, about the same amount of water added to the fibers must be incorpora in a second step.
  • the preferred solution is the subsequent moistening of th degassed preform.
  • the premoistening and precompressed preform accepts water absorption at a substantially higher degree than still completely dry material.
  • the matt exiting the degassing station has sufficient strength for a free release o a parted forming belt in order to allow both the top and botto surfaces to be further moistened.
  • the materia absorbs water by suction during springback.
  • the water supplie onto the board may contain strongly effective accelerating age or other additives increasing the speed of setting, since the final compression is carried out immediately afterwards.
  • pulverous plaster or other materials
  • Such plast adheres well and improves the surface of the board with respec to appearance, availability and surface treatment, as well as fire resistance.
  • viscous fillers can be sprayed or applied by rollers on both sides of the preform between the gap of the forming belts.
  • the incorporation of the water is made possible by absorption.
  • the water preferably is added in the gap which fo between the degassing roller casing and preform and/or sprayed onto the matt during and/or after degassing, but, as represented in Fig. ID, it is also possible to release water through water- carrying belts, e.g. felt belts with further simultaneous degassing via pairs of rollers disposed downstream inside the degassing-screen fabric belt.
  • the amount of moisture added depends on the water necessary for the hydration of the dry calcined gypsum to an optimum of strength, the absorption capacity of the respective preform, and the composition of the initial material.
  • the second watering step may not achieve absolute uniform moistening for thick one-layer boards, this is not a significant disadvantage since a sufficient amount of water for the stoichiometric setting of the plaster (and some surplus water) often is already incorporated through the wetted fibers and since any strength reduction is in the middle or neutral zon where strength is less essential.
  • this potential lack of uniform moistening can be overcome in the manufacture of 3- layer boards which can have a high wetted low density porous particle, e.g., perlite, vermiculite, foamed glass or pumice content in the center layer. By moistening the perlite, it is possible to incorporate enough water for the plaster setting in the center layer so that only the covering layers need to be provided with additional water. Figs.
  • the end product can be a homogenous board (illustrated in Fig. 11) or a multilayered composite product (illustrated in Fig. 12) .
  • the homogeneous board is preferably a gypsum board reinforced by fiber, such as paper fiber.
  • the multilayered board can take many forms. In t preferred embodiment, the multilayered board has a core layer including lightweight materials, such as expanded perlite, and bottom and top surface layers of fiber gypsum.
  • the homogeneous board and the multilayered board of the present invention can be made according to the same basic proce and with a similar, if not identical, production line.
  • several layers of board forming materials are placed on each other before the board is fully formed, pressed, and dried.
  • each of the layers is identical in composition.
  • two or more different layers are used.
  • the production line include several general areas.
  • the various materials used to fo the board are prepared or held in preparation areas. Such preparation areas are shown in Figs. 1-5 which will be describe in more detail below.
  • the materials are combined and placed in layers on a moving conveyor, in a forming area, illustrated in Fig. 6.
  • the formed matt is then degassed, compressed and calibrated in a pressing area illustrated in Fig. 7.
  • the formed endless boards are then cut into individual boards in a cutting and conveying area (illustrated in Fig. 8) and then completely dried to a finished product in a dryer area (illustrated in Fig. 9) .
  • the dry boards are then cut and stacked in a finishing line (illustrated in Fig. 10) .
  • the production line for making a multilayered board, having perlite and fiber and gypsum for the middle core, will first be described.
  • the use of the methods and equipment to produce different boards according to the present invention will then be described.
  • Fig. 6 shows three forming lines.
  • Each forming line ha three preforming belts 3126, 3166 and 3146 on which the wetted fibers and dry calcined gypsum with additives for the surface layers and wetted perlite fibers and dry calcined gypsum for the core layer are formed.
  • wet fiber from the mills 2311, 2212 (shown in Fig. 5) is carried by a closed loop pneumatic conveyor 2511, 2512 to the forming station where the fibers are separated from the air by a cyclone. The separated fibers are deposited into shuttle conveyors on the top of fiber formers 3114, 3134.
  • the fiber formers spread via spreader heads 3115, 3135 a preselected amount of fiber, according to the weight ratio of a preferred recipe, onto the preforming belts 3126, 3136, forming a matt.
  • the spreader heads preferably include a plurality of rollers which cause a uniform layer of fibers to be placed onto the preforming belts.
  • scalper rolls 3117 and 3137 Immediately downstream of the spreader heads 3115 and 3135 are scalper rolls 3117 and 3137, respectively, which scrape off excess fiber and thereby equalize the thickness of the matt.
  • the scalper rolls can be adjusted in height to ensure that the deposited matt of fibers has a uniform weight, and a vacuum is applied at the rollers to pneumatically draw off excess fibers. Fibers scraped off by the scalper rolls are recycled pneumatically by pneumatic conveyors 2513 and 2507 into the same shuttle conveyors on the top of fiber formers 3114 and 3134.
  • the preforming belts operate at a constant speed.
  • the dry calcined gypsum additive mixture from distribution bin 2480 (shown in Fig. 4A) is fed to plaster forming bins 3124, 3144 (shown in Fig. 6) .
  • the plaster as explained below, is predominately calcined gypsum, although the plaster may include other additives (shown in Fig. 2) to control the chemical process.
  • the gypsum is metered from the forming bins by conventional means, such as conveyors, chutes, or rollers.
  • the bins have a variable speed bottom belt conveyor with an integrated matt scale 3125, 3145 to control the amount of plaster deposited on the preforming belt depending on the recipe.
  • the correct amount of plaster is added as a top layer onto the fiber matt.
  • the mixing heads comprise sets of spike rollers (shown in Figs. 16A and 16B) which thoroughly mix the fiber and plaster into a homogeneous composition and carry the mixture from the head of the preforming belt (infeed) to the outfeed of the mixing head onto the forming belt 4010.
  • a series of spike rolls controls the downward motion of the material.
  • Additional sets o turbulent rollers as shown in Fig. 16A, automatically clean the mixing rollers.
  • the core layer is formed in a similar manner to that of the surface layer.
  • less fiber is included in the core layer becaus a volume of expanded perlite is used in the core layer.
  • Expande perlite is included in the core layer to reduce the overall specific weight of the board. Expanded perlite also will carry more setting water for the plaster.
  • the mixture of wetted paper fibers and perlite particles are moisturized so tha they will carry all of the water necessary to hydrate the plaste to optimum strength added to form the core layer.
  • an adhesive preferably liqui starch, is first mixed with the water for moistening the perlite and the fibers are separately mixed with water. The wetted fibers and wetted perlite are then mixed together to form a uniform mixture.
  • a wetted perlite, starch and fiber mixture (from conveyor 3152, shown in Fig. 4) is deposited in fiber former 3154, which is identical in structure and operation to formers 3114, 3134.
  • the perlite, starch and fiber mixture is deposited onto preforming belt 3166 through spreader head 3155, in the same manner as the board surface layers.
  • Preforming belt 3166 layers the perlite, starch and fiber mixtur from fiber former bin 3154 with the plaster from forming bin 316 and delivers the components to a mixing head 3168.
  • Forming bin 3164 includes an integrated matt scale 3165.
  • the core layer forming line includes a scalper roller 3157, matt scales 3156, and a mixing head 3168 which operated in the same manner as the elements in the surface forming line.
  • the mixing heads 3128 and 3168 are precompressor rollers 3129 and 3169 which remove as much air as possible from the formed matt.
  • the three layered matt is pressed by a press line, shown in Fig. 7.
  • the forming belt 4010 is also part of the press line and extends through the press and calibrating sections.
  • the forming belt ends at th degassing station 4012 of the press line, so that there is an open gap between the degassing station and the compression station. Behind the last compressing roller of the degassing station, spraying nozzles are installed for adding additional water for moistening the surface layers of the matt from both sides.
  • the press line includes three main sections, the degassing station 4012, the compression station 4013, and the calibration station 4014. These stations can be adjusted to vary the spacin between the conveyor belts as well as the pressure being applied to the matt of gypsum, fibers, additives, and other materials. The adjustment of the station, therefore, allows the user to var the thickness of the board.
  • the matt is precompressed by the degassing station 4012 to remove air from the matt.
  • this station reduces the matt from a thickness of several inches close to the final thickness which can vary, e.g. from 3/8 to 3/ inch.
  • the degassed matt is pressed in compression station 4013 where the matt is subject to a high load and pressed to the final board thickness.
  • the matt then goes through calibration station section 4014 which holds the thickness of the board to allow the setting process to continue.
  • the boards After pressing and prior to drying, the boards are cut and prepared to enter the dryers. Referring to Fig. 8, the boards, which are formed and pressed endlessly, are pre-trimmed and cut into e.g. 24 foot long pieces. Two stationary and one traversin high pressure water jets 3171, 3172, 3173 cut and trim the boar Water jet 3171 and 3172 trims the length, while water jet 3173 cross cuts the board. While in the cutting area and immediatel prior to, the board is supported by an air cushion which lifts the board but does not provide forward motion. This air cushio is provided by air jets or similar means (not shown) which are well known in the art. Belt conveyors 3176, 3177 accelerate th board to a high conveying speed.
  • the dryer area 4210 shown in Fig. 9, is equipped with th setting zones before the first drying zone.
  • the drying sectio of the production line is well known in the art and therefore will not be discussed in any detail.
  • the present invention provides a method for producing gypsum boards and composite boards having a variety of preselected characteristi Generally, only a sufficient amount of water is included with wetted fiber to properly hydrate the gypsum to optimum strengt
  • three separate mixing lines a utilized, thereby providing three layers of the board. If each of the layers is made from the same materials, a homogeneous board is provided.
  • the layers can be of different materials. For example, a board can have the same outer layers and a lighter, inner lay according to the above description. A board with three differe layers also can be created.
  • a board could have an outer layer made of fiberglass, fibers and gypsum to provide increased strength and fire resistant, an intermediate layer of perlite, fiber and gypsum, and an outer decorative layer of textured fiber and gypsum.
  • the textured layer would be achieve by including a texturized belt on one side of the compression a calibration station.
  • a single mixing line can be utilized to form a uniform mat of selected materials.
  • the single matt could be a matt of fiber and gypsum; fiber, gypsum and starch; paper fiber, fiberglass, and starch.
  • more than three line can be utilized, thereby providing more than three layers.
  • five separate lines of conveyor belts, pinwheels, and mixers could be utilized. Regardless of whether a homogeneous 'composite board is desired, the forming, cutting and drying ste would be substantially the same, differing only to best accommodate the characteristics of the chosen layers.
  • the preferred equipment used to prepare wetted paper fiber is depicted in Fig. 1.
  • the paper, initially in bales, is fed into shredder 2001.
  • the paper used in this process preferably consists of discarded newspaper.
  • Number 6 newsprint has been found to be an excellent fiber for this process.
  • This paper consists of baled newsprint containing less than 5% of other papers.
  • Each shredder has a hydraulic cylinder which pushes th bale against a rotating cylinder equipped with teeth. The cylinder mills the bale into paper pieces, approximately 8 x 8 inches and several pages thick.
  • Belt conveyor 2401 are equipped with a permanent magnet an metal search coil. Any tramp metal which is large enough to be dangerous causes the belts to stop and the metal is removed manually.
  • Hammer mills 2101 reduce the paper pieces to about size of a stamp.
  • the clippings are then conveyed pneumaticall from the hammer mills via distribution conveyors 2403, 2404 to clipping bins.
  • the clipped paper is distributed to clipping b 3100 (Fig. 5) , to supply the surface layers of the board and t clipping bin 3050 (Fig. 4) for the core layer.
  • the mills 2301, 2311, 2212 produce the paper fibers with necessary fineness and mix water with the fibers prior to mixt of the wetted fibers with the plaster.
  • th absorbent lime is delivered to a dosing system 3053, 3111 and 3131 via distribution screw conveyors 2455, 2456, 2457 and fed into the mill with the paper clippings.
  • the paper clippings are dosed by weight belts 3051, 3110 and 3130.
  • the mills can be wing beater mills or turbo mills, depending upon the type of fibers used.
  • the wastepaper is fed into the bottom of the mill.
  • the mill has a coarse rotating wheel at the bottom an finer wheels toward the top.
  • a coarse rotating wheel first interacts with the paper and places it into a rotary motion.
  • Th paper begins to fractionate by interaction with the wheel and with itself and progresses upward toward a smaller rotating whee which interacts with the paper and passes it on to another rotating wheel.
  • the principle of milling in the turbo rotor is based on a high air throughput.
  • the airstream in the milling zone becomes extremely turbulent in between the rotating and fixed parts of the mill.
  • the particles of paper in the mill are constantly changing speed and direction of travel very rapidly due to the air turbulence.
  • the impact of the paper particles among each other causes the paper particles to fractionate and creates most of the milling action.
  • water is introduced as a fine spray into the milling chambers.
  • the water is preferably added to the fiber in the upper regions of the turbo mill.
  • the air turbulence and rotary motion of the fibers provides a very fine blending of the paper fibers and water, without any adverse balling of the fibers and water.
  • wing beater mills are used, the water is added as a spray at the exit of the mill. Dry fibers are moved through a screen in which the fibers fraction to decreasing size.
  • wing beater mills to create fibers is well known in the industry. However, the inventors have modified the mills and their use by adding spray nozzles at the chamber of the wing beater mill where the fibers come out of the screen of the mill to wet the exiting fibers.
  • the wetted fibers are loose, not balled and have a fluffy consistency.
  • the wetted fiber from mills 2311, 2212 is pneumatically conveyed to the fiber formers of the forming station of Fig. 6.
  • the sizes of the fibers preferably range fro minute particles to elongated fibers up to 2000 microns by scree test.
  • the plaster component of the board is prepared as shown in Fig. 2. If the natural raw gypsum is used in the process, it is first calcined via any conventional method before it is used in the process. In the process, the particles of gypsum are dehydrated from two molecules of water to one-half a molecule of water. Such a calcining process and the equipment for preparing the plaster are conventional in the art.
  • the calcined gypsum is stored in a day bin and from there metered into the production line.
  • the plaster passes a weightbelt 3000.
  • the signal from the weightbelt 3000 is used t control the flow of additives in a mixing screw 2451.
  • Additives from hopper 3011 and hopper 3021 can be added to the plaster to accelerate the setting and hydration.
  • potassium sulfate and ground gypsum can be added to th plaster to accelerate the setting and hydration.
  • a mixing screw 2451 is used to mix the plaster and additives into a homogeneous mixture having the proper amount o additives to the plaster, depending upon the recipe.
  • the perlite for the core layer of a composite board is prepared as shown in Figs. 3 and 4. Expanded perlite is stored in a bin with a controlled outfeed. The actual weight of the perlite is measured by a weightbelt 3070 (Fig. 4) which provide a signal used to add a liquid starch solution (from 3061) to a primary blender 2901.
  • the liquid starch solution is made from water and starch and is prepared at site 1900 as shown in Fig. 3
  • the starch solution is metered gravimetrically via starch stora vessel 3060 into starch weighing vessel 3061 and then is spraye by pump 3062 into blender 2901. In the blender 2901 the perlit and liquid starch are thoroughly mixed.
  • the wetted perlite leaving the blender 2901 is mixed with prewetted paper fiber.
  • the prewetted fiber is conveyed from a mill by a pneumatic conveyor 2505.
  • paper fibers and water are mixed together in the same manner as previously described with reference to mills 2311 and 2212. Since the mixed core layer includes expanded perlite and paper fibers, the amount of fiber used is less than that of the surface layers.
  • a conveyor 2409 (Fig. 4) runs the mixed material, via a distribution gate 3080 to the core layer fiber/perlite former 3154 in the forming station shown in Fig. 6. As previously described, this wetted perlite, fiber, starch and additive mixture is then mixed with dry gypsum to form the middle layer the composite board.
  • a uniform, homogeneous board 102 such as shown in Fig. 11 achieved.
  • This homogeneous board is made of a mixture of lignocellulose fibers, gypsum and additives, as previously explained.
  • the uniform, homogeneous board 102 can be provided with a variety of decorative surfaces 103.
  • smooth belts are used in t calibration station.
  • textured belts can be used in the compression and calibration stations, thereby providing textured designs on one or both surfaces of the gypsu board.
  • the fiber and perlite composite board made according to th above method is illustrated in Fig. 12.
  • the top layer 100 and the bottom layer 100 are fiber gypsum layers, while the middle layer 101 is a perlite, fiber and gypsum layer. Because perlit is included in the middle layer, the composite board is lighter in weight without significantly sacrificing any strength.
  • the surface layers have a waste paper fiber content of 30% of the surface layer of the finished board.
  • 10% CaO was added to the dry paper and 120% water was added to the fibers.
  • Natural gypsum fine milled and calcined to semihydrate was mixed with fine milled powders of 2% gypsum dehydrate, 1% potassium sulfate and 4% starch.
  • the core layers have a fiber content of 8% milled with 2% CaO and wetted with 60% water. 30% dry, expanded perlite (size: 90% of the material between 30 and 1000 mg by screen test) was mixed with the same amount of a 5% starch-water dispersion. The same gypsum-semihydrate-mixture was used. The material ratio of the surface to core is 1 : l.
  • a board made according to the above recipe meets the initially stated quality requirements regarding weight and strength. At 930 kg/m 3 density, the strength amounted to 8-12 N/mm 2 .
  • the covering layer can have a fiber contents of up to 30% and still meets, as a fire "shield", the ratings of the US “fire rating” requirements according to ASTM C 16 because of the effect of the center layer which has the high perlite and gypsum content.
  • Boards according to the present invention can be made of practically any size, and the boards can be formed or subsequently machined to have a variety of shapes.
  • the edges of the boards can be shaped as tongue and groove joints or the exterior of the boards can include decorative textures.
  • Boards made according to the present invention have excellent nail and screw holding properties, and the face of the wall board is already plaster. The board therefore can readily accept any conventional finishing materials, including wall paper.
  • the present invention also allows the production of gypsum board having strength and/or density not previously possible. Since the wetted fibers and plaster mix form a uniform mixture which is substantially dry, the mixture can be compressed as desired in the press shown in Fig. 7. The density and thickness of the resultant board therefore can be controlled within a considerable range.
  • the present invention can produce a board having densities within the range of 25 lbs per cubic foot (pcf) (400 kg/m 3 ) to 75 pcf (1200 kg/m 3 ) , or higher.
  • the type and size of fibers and the other materials included in the board can also be varied as desired.
  • the gypsum board can be a truly engineered product tailored to meet particular end use requirements.
  • Figs. 17 through 19 illustrate three embodiments of a gypsum and wood substrate board made according to the present invention.
  • he end product can be a board having a gypsum layer on one side (illustrated in Fig. 17) or a board having a gypsum layer on both sides (illustrated in Fig. 18) .
  • the layer of gypsum on the board is preferably a homogeneous gypsum layer reinforced by fiber, such as paper fiber.
  • the layer or layers of gypsum can take many forms.
  • the board has a wood substrate for its core and includes one or more layers of homogeneous fiber gypsum. A resin is used to bond the gypsum to the wood substrate.
  • the composite board includes a wood substrate 110 and a fiber gypsum overlay 112 which is bonded to the wood substrate 110.
  • the wood substrate 110 can take a variety of forms, including plywood, particle board, waferboard, wood laminants, and similar conventional wood or wood-like building products.
  • the fiber gypsum overlay 112 is securely bonded mechanically or adhesively using epoxy cement, for example, to the wood substrate 110 and is preferably a homogeneous layer of gypsum and fiber.
  • the gypsum fiber overlay is fire-resistant and smoke resistant and adds to the overall strength of the resultant composite board.
  • the composite board illustrated in Fig. 18 is similar to the embodiment shown in Fig. 17, except that both a top surface fiber gypsum overlay 112 and a bottom surface fiber gypsum overlay 114 are formed on the wood substrate 110.
  • the resultant board has fiber gypsum surfaces on both of its sides, thereby providing increased fire resistance.
  • such a board can provide a finished exterior surface, along with the increased strength provided by the wood substrate.
  • the exterior surface 113 of the fiber gypsum overlay 112 is embossed with a decorative surface.
  • a variety of decorative surfaces can be rolled or pressed into the fiber gypsum overlay while the overlay is being finished.
  • the fiber gypsum overlay 112 is composed of two separate layers of gypsum material.
  • the first layer 116 is a fiber, perlite and gypsum layer which provides a light weight core layer bonded to wood substrate 110.
  • the second layer 117 is a fiber gypsum layer which provides a smooth exterior surface to the panel and which binds to the ligh weight core layer.
  • the various embodiments of the composite board of the present invention can be made according to the same basic proces and with a similar, if not identical, production line to that previously disclosed.
  • a coating of a bonding agent such as resin is applied to the wood substrate.
  • one or more layers of fiber gypsum are deposited over the resin- coated substrate.
  • the resultant fiber gypsum layer and wood substrate are then pressed and dried, preferably in a continuous process.
  • the surface of the wood panel is preferably roughened by a surface cutter which will surface cut the side or sides of the panel to which the gypsum will be applied.
  • the cutting or roughing up of the surface of the wood substrate provides for better bonding of the gypsum overlay to the panel.
  • a special mineralic-fire resistant glue is then sprayed on the roughened surface.
  • One such glue is waterglass (sodium silicate which is available from Philadelphia Quartz.
  • Acceptable adhesives and resins include urea and phenol formaldehyde, urethane, and recorcinal type resins.
  • the method of the present invention can be used to produce fiber gypsum boards and composition boards that are made from various materials and additives.
  • Page 22 delete "belt” (first occurrence) and substitute — belts 151, 152 —.
  • Page 22 delete "belt” (second occurrence) and substitute — belts 155, 156 —.
  • Fig. 14 is a side view and Figs. 14 and 14B are schematic partial cutaways of a turbo mill for dissolving and wetting fibers according to the present invention.
  • Fig. 14 there is represented an absorbent intake pipe 170, a paper clippings intake pipe 171, water nozzles 173, and wetted fibers output pipe 172.
  • FIG. 14A which is a sectional view taken along line 14A- 14A of Fig. 14, there are represented a housing 174, stator plates 175, turbo plates 176 and turbulence chambers 177.
  • Fig. 14B which is a sectional view taken along line 14B-14B of Fig 14A, there are represented the housing 174, stator plates 175, disks 178, milling/turbo plates 176, turbulence chambers 177, rotor 179, drive 180, and shaft 181 and bearing 182. —.
  • Fig. 15 is a schematic side view of a mixing station of the present invention.
  • a preforming belt 185 There are represented a preforming belt 185, a fiber matt 186, a plaster layer 187, a distributing spike roller 188, transfer spike rollers 189, mixing spike rollers 190, guiding plates 191, forming belt 192, mixture 193 and cleaning brush 194.
  • Figs. 16A, 16A-1, and 16A-2 are side views of a vertical mixture and the mixing and cleaning disks, respectively. There are represented a housing 200, a drive 201, cleaning turbulence rollers 202, bearing 203, mixing spike rollers 204, guiding plate 205, mixing spike disks 206 and cleaning turbulence disks 207.
  • Figs. 16B and 16C are top and front views of the vertical mixer of Fig. 16A, also showing drive 208. —.

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Abstract

Procédé et appareil de fabrication de planches de plâtre. Le procédé consiste à mélanger une quantité prédéterminée de fibres, d'absorbant et d'eau afin de former un mélange de fibres humides, à mélanger les fibres humides à une quantité prédéterminée de plâtre cuit sec, à donner au mélange la forme d'un matelas à consistance sensiblement homogène, et à comprimer le matelas afin de former une planche constituée de fibres liées et de plâtre. La planche ainsi obtenue présente une surface lisse et peut être une planche homogène ou multicouche.
PCT/EP1991/002215 1991-11-25 1991-11-25 Planche de platre fibreux et son procede de fabrication WO1993011085A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/EP1991/002215 WO1993011085A1 (fr) 1991-11-25 1991-11-25 Planche de platre fibreux et son procede de fabrication

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994025234A1 (fr) * 1993-04-29 1994-11-10 Eternit-Werke Ludwig Hatschek Aktiengesellschaft Procedes et installations permettant de fabriquer des produits composes de fibres et d'un liant hydraulique
US5632848A (en) * 1989-10-12 1997-05-27 Georgia-Pacific Corporation Continuous processing equipment for making fiberboard
US5945182A (en) * 1995-02-14 1999-08-31 G-P Gypsum Corporation Fire-resistant members containing gypsum fiberboard
US5945208A (en) * 1989-10-12 1999-08-31 G-P Gypsum Corporation Fire-resistant gypsum building materials
WO2008049473A2 (fr) * 2006-10-23 2008-05-02 Vogl Erich R Plaque de placoplâtre avec additifs adsorbants
WO2022128041A1 (fr) * 2020-12-16 2022-06-23 Knauf Gips Kg Production de corps moulés en gypse sur une presse à cycle à l'aide de poussière de broyage

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DE3242598A1 (de) * 1982-11-18 1984-05-24 Gipsconsult Management und Beratungs AG, 8036 Zürich Verfahren zur herstellung von formkoerpern insbesondere platten unter verwendung von calciumsulfathaltigen bindemitteln
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US5632848A (en) * 1989-10-12 1997-05-27 Georgia-Pacific Corporation Continuous processing equipment for making fiberboard
US5945208A (en) * 1989-10-12 1999-08-31 G-P Gypsum Corporation Fire-resistant gypsum building materials
US6299970B1 (en) 1989-10-12 2001-10-09 Georgia-Pacific Gypsum Corporation Fire-resistant gypsum fiberboard
WO1994025234A1 (fr) * 1993-04-29 1994-11-10 Eternit-Werke Ludwig Hatschek Aktiengesellschaft Procedes et installations permettant de fabriquer des produits composes de fibres et d'un liant hydraulique
US5945182A (en) * 1995-02-14 1999-08-31 G-P Gypsum Corporation Fire-resistant members containing gypsum fiberboard
WO2008049473A2 (fr) * 2006-10-23 2008-05-02 Vogl Erich R Plaque de placoplâtre avec additifs adsorbants
WO2008049473A3 (fr) * 2006-10-23 2008-09-25 Erich R Vogl Plaque de placoplâtre avec additifs adsorbants
WO2022128041A1 (fr) * 2020-12-16 2022-06-23 Knauf Gips Kg Production de corps moulés en gypse sur une presse à cycle à l'aide de poussière de broyage

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