1. Field of the Invention
This invention relates to the production of gypsum board. More particularly, the present invention relates to the use of foamed starch pellets in the production of lightweight gypsum board.
2. Description of the Background Art
Gypsum board is one of the most widely used and versatile building materials in the world. The general construction of gypsum board includes a core of calcium sulfate dihydrate that is sandwiched between opposing paper sheets. The core is initially deposited in the form of a slurry; namely, calcium sulfate hemihydrate (CaSO4.½H2O) in water. Once the slurry is deposited, it is rehydrated to form gypsum. The hemihydrate is initially prepared in a mill via the following reaction:
CaSO4.2H2O+heat→CaSO4.½H2O+1½H2O(steam)
The dehydrated calcium sulfate is known as calcined gypsum, stucco, or plaster of Paris. Gypsum has a number of desirable physical properties that make it suitable for use as a building material. These properties include fire resistance, compressive strength and neutral pH. Gypsum is also a beneficial building material because it can be formed into various shapes and is inexpensive and plentiful.
It is also known in the art to use additives with gypsum. One such additive is starch. Starch can be added prior to rehydration. Starch functions as a binder within a set gypsum and yields boards with higher compressive and flexural strength. It also strengthens the edges of the resulting board and improves paper bond to the core.
It is further known in the art to form voids with the interior of gypsum board as a means for reducing the board weight. The background art includes several examples of void formation. One technique is described in U.S. Pat. No. 6,706,128 to Sethuraman. Sethuraman '128 discloses a method for adding air bubbles of different relative stabilities, whereby the air bubbles do not rupture before the slurry sets sufficiently to prevent the slurry from filing the void spaces left behind by ruptured bubbles. The result is a gypsum board with reduced weight.
Another example is illustrated in U.S. Pat. No. 1,776,325 to Robinson. Robinson '325 discloses a method of making a cellular wall board by incorporating an aerated starch into a slurry. As a result of the aerated starch, the slurry is given a desired porosity and forms a cellular core.
Finally, U.S. Pat. No. 5,643,510 to Sucech discloses a method for producing foamed gypsum board using a foaming agent blend. The ratio between a first and second foaming agent are controlled to adjust the sizes of foam voids within a gypsum core.
Although each of the above referenced inventions achieves its individual objective, they all suffer from common drawbacks. Namely, the voids are formed via the use of foaming agents require additional chemicals to be added to the gypsum. Void formation added via aeration likewise requires additional machinery. Moreover, in both methods the control of the associated machinery is difficult. In prior methods of void formation it is also difficult to form voids of the correct size.
One of the advantages of the disclosed method is that it results in void formation within gypsum building board.
Another advantage is that void formation can be increased without adding additional foaming agents.
Still yet another advantage is that void size can be controlled and/or specified.
Still another advantage is that the disclosed pellets provide the desired starch component to the board while at the same time providing voids within the core.
Another advantage is that the provided starch enhances the wall structure of the voids that are created upon the dissolution of the starch, as a fraction of the starch is retained at the void/solid interface.
Yet another advantage of the disclosed system and method is that it provides for the production of gypsum board that is both strong and lightweight.
These and other advantages are accomplished by a system and method that involves providing a mixture of stucco and foamed starch beads along a board production line. The starch pellets are slightly soluble at temperatures below 140° F. The stucco/foamed beads slurry is then deposited between opposing sheets to form a composite panel. The set wet board is then transferred to a dryer. Dryers are then used to dry the panel. The heating causes the starch to dissolve, whereby the dissolved beads provide starch to the gypsum core and/or bond area of the paper. The dissolving beads also create a fairly uniform bubble structure within the core. The pellets thereby produce voids within the set board.
The foregoing has outlined rather broadly the more pertinent and important features of the present invention in order that the detailed description of the invention that follows may be better understood so that the present contribution to the art can be more fully appreciated. Additional features of the invention will be described hereinafter which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and the specific embodiment disclosed may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims.
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:
Similar reference characters refer to similar parts throughout the several views of the drawings.
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.
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.
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.
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.
The system of the present disclosure is carried out along a board production line 32 as noted in
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.
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.
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 has the desired thickness. With reference now again to
CaSo4.½H2O+1½H2O→CaSo4.2H2O
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.
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 (note
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.