System and method for the production of gypsum board using starch pellets

Abstract

The present invention relates to a system and method for the production of gypsum board using starch pellets. In accordance with the present disclosure, the starch necessary for board formation is provided in the form of starch pellets. These pellets are mixed with a gypsum slurry in a mixer. The pellets are initially insoluble and do not dissolve. However, during subsequent drying stages, the pellets become soluble and dissolve into the gypsum phase. This both provides the desired starch component and also results in the formation of voids within the set gypsum.

Claims

1. A system for the production of lightweight gypsum board, the system comprising: a board production line having upstream and downstream ends, the production line including two supply rolls for first and second facing sheets; a first supply of starch pellets; a second supply of stucco; a mixer for combining the starch pellets and the stucco with water to form a slurry, the mixer blending the pellets and the slurry such that the pellets become fully encapsulated within the slurry, the mixer including an outlet for depositing the blended pellets and slurry between the first and second facing sheets to create a panel.

2. The system as described in claim 1 further comprising a series of board dryers located downstream of the production line for drying the panel.

3. The system as described in claim 2 wherein drying the panel within the dryers causes the pellets to dissolve and the gypsum slurry to set, whereby the dissolved pellets provide starch to the gypsum slurry and create voids within the set gypsum.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) For a fuller understanding of the nature and objects of the invention, reference should be had to the following detailed description taken in connection with the accompanying drawings in which:

(2) FIG. 1 is a flow chart illustrating the steps associated with the disclosed method.

(3) FIG. 2 is an elevational view of a board production line.

(4) FIG. 3A is a sectional view of a board taken from FIG. 2.

(5) FIG. 3B is a sectional view of a board taken from FIG. 5.

(6) FIG. 4 is an elevational view of the entrance to a board dryer.

(7) FIG. 5 is an elevational view of the exit from a board dryer.

(8) Similar reference characters refer to similar parts throughout the several views of the drawings.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

(9) The present invention relates to a system and method for the production of gypsum board using foamed starch beads. In accordance with the present disclosure, the starch needed for preferred board formation is provided in the form of individual foamed beads. These beads are dispersed within a gypsum slurry by way of a mixer. The pellets are initially insoluble and do not dissolve in the presence of the gypsum slurry. However, during subsequent heating in a dryer, the beads become soluble and dissolve into the gypsum phase. This dissolution provides the desired starch component to the gypsum while at the same time producing voids within the core.

(10) The preferred starch beads, or pellets, are formed by way of an extrusion process. During the process, air is combined with starch via an extruder. The resulting foamed pellets may be of an irregular size but generally have a diameter of between approximately 1/32 of an inch to 1/64 of an inch. A mix of different sized pellets can also be used. Other sizes can be produced depending upon the parameters of the extruder. Other processes can likewise be used for formation of the foamed starch pellets. For example, the pellets can be formed via known prilling processes. They can also be made into droplets similar to polystyrene manufacturing methods. In the preferred embodiment, the foamed pellets are hydrophobic at low temperatures and resist dissolving at temperatures below approximately 140 F.

(11) FIG. 1 is a flow chart illustrating the steps carried out in accordance with the present disclosure. In the first step 20, the foamed pellets are combined with stucco. In the preferred embodiment, the pellets make up between approximately 5 to 50% of the overall slurry by volume. Preferably, the pellets and stucco are combined prior to the mixer.

(12) At step 22, the pellets and stucco are mixed with water in a mixer to create a slurry. The mixer can be a conventional mixer typically found in board production lines. This blending step fully encapsulates the pellets within the resulting slurry. Again, however, the pellets remain insoluble at this point and the starch is not dissolved into the gypsum phase. The blended slurry is then deposited between opposing paper sheets to form a panel at step 24.

(13) The panel with the slurry and encapsulated pellets are then dried in a series of dryers at step 26. As the panel is dried, and the temperature of the board approaches 200 F., the pellets become soluble and dissolve into the gypsum phase as starch. The dissolved pellets leave behind voids within the board. The panel dries simultaneously with the starch dissolution. The result, as noted at step 28, is a set gypsum board that contains both the desired amount of starch and that has voids to reduce the weight of the board.

(14) The system of the present disclosure is carried out along a board production line 32 as noted in FIG. 2. A suitable product line is more fully described in commonly owned U.S. Pat. No. 6,524,679 to Hauber, the contents of which are fully incorporated herein. Production line 32 generally includes a mixer 34 with various outlets 34a, 34b, and 34c. These outlets can deposit slurry in varying densities in order to form a core with varying physical properties. Supplies of foamed pellets and stucco are also included (36 and 38, respectively). These supplies feed into a container 42 where the pellets and stucco are initially combined. In the preferred embodiment, the foamed pellets and stucco are mixed while dry. Water is subsequently added at mixer 34 to form a slurry and begin the re-hydration process. As noted, the pellets and slurry are preferably combined at a ratio of between approximately 5-50% by volume.

(15) Container 42, in turn, feeds into mixer 34. This can be a conventional mixer currently used in a gypsum board manufacture. As noted, mixer 34 is used in blending the pellets and stucco with water. This blending converts the stucco to slurry and ensures that the individual pellets are encapsulated by slurry. Additional additives can be added to the mixer as needed depending upon the requirements of the gypsum board.

(16) The production line further includes two or more large wound rolls of paper 44. In one embodiment, two rolls are included for forming the upper and lower paper sheets (46 and 48, respectively) of the gypsum board 52. Additional rolls can be provided for including fibrous mats or other sheets depending upon the intended use of the resulting board. Mixer 34 deposits the gypsum slurry between sheets 46 and 48 upon a forming table 54. The majority of the slurry is preferably dispensed at outlet 34b. If desired, a small amount of denser slurry can be applied to bottom paper sheet 46 at outlet 34a. A denser slurry can likewise be applied to upper paper sheet at outlet 34c. Outlets 34a, 34b, and 34c can all deliver blended slurry with pellets from mixer 34. Alternatively, the blended gypsum with pellets can be limited to outlet 34b, with outlets 34a and 34c supplying gypsum slurry without pellets.

(17) In either alternative, top sheet 48 is applied over the deposited gypsum with blended pellets immediately prior to a pinch point 56. Thereafter, the resulting panel 52 is passed through a hinge plate 58 and extrusion plate 62 to ensure that the panel 52 as the desired thickness. With reference now again to FIG. 3A, it is seen that following extruder 62, a panel 52 is a composite that includes a bottom paper sheet 46, the blended gypsum core 64 with encapsulated pellets 66, and a top paper sheet 48. Moreover, the individual foamed pellets 66 are distributed throughout the thickness of the gypsum core 64. At this stage, the pellets are undissolved, only slightly soluble, and fully encased within the core 64 of unset slurry. Prior to entering the board dryers 68, the gypsum core sets in accordance with the following equation:
CaSo.sub.4.Math.H.sub.2O+1H.sub.2O.fwdarw.CaSo4.Math.2H.sub.2O

(18) Thereafter, the composite panel is cut into desired lengths at cutting stations (not shown) and then delivered via belts to a series of board dryers 68. FIG. 4 illustrates the composite panels being delivered to the entrance of board dryer 68, whereas FIG. 5 illustrates the composite panels exiting board dryer 68. During the drying phase, the panel is exposed to temperatures in excess of 140 F. and generally in the neighborhood of 200 F. As is known in the art, the dryers 68 are used to dry the gypsum slurry. However, in accordance with the present disclosure, the excess temperatures also cause the individual pellets 66 encapsulated within the gypsum to become very soluble. After becoming soluble, pellets dissolve 66 whereby the starch is dissolved into the gypsum phase of core 64. This starch, when combined with the gypsum, provides the necessary degree of board strength and can also improve the bond between the facing paper and the core.

(19) Upon dissolving, the individual foamed pellets 66 leave behind voids 72 which, like pellets 66, are distributed throughout the thickness of the set gypsum core 64 (note FIG. 3b). The result is a gypsum building panel 52 with a core 64 of set gypsum. This set gypsum has the needed starch by virtue of the dissolution of the foamed pellets 66. Additionally, voids 72 that are left behind function to both reduce the overall weight of panel 52 and provide added strength. Each individual void also includes a peripheral lining. The starch dissolution is such that the starch concentration is higher at the void lining than in the remaining core body.

(20) The present disclosure includes that contained in the appended claims, as well as that of the foregoing description. Although this invention has been described in its preferred form with a certain degree of particularity, it is understood that the present disclosure of the preferred form has been made only by way of example and that numerous changes in the details of construction and the combination and arrangement of parts may be resorted to without departing from the spirit and scope of the invention.