The present disclosure generally relates to a method and apparatus for preparing gypsum products from starting materials including calcined gypsum and water, and more particularly relates to an improved apparatus for use in conjunction with a slurry mixer used in supplying agitated gypsum slurry to a wallboard production line.
It is well known to produce gypsum products by dispersing calcined gypsum in water to form a slurry, then casting the slurry into a desired shaped mold or onto a surface, and allowing the slurry to set to form hardened gypsum by reaction of the calcined gypsum (calcium sulfate hemihydrite or anhydrite) with the water to form hydrated gypsum (calcium sulfate dihydrate). It is also well known to produce a lightweight gypsum product by mixing an aqueous foam into the slurry to produce air bubbles. This will result in a desired distribution of voids in the set gypsum product if the bubbles do not escape from the slurry before the hardened gypsum forms. The voids lower the density of the final product, which is often referred to as “foamed gypsum.”
Prior apparatus and methods for addressing some of the operational problems associated with the production of foamed gypsum are disclosed in commonly-assigned U.S. Pat. Nos. 5,638,635; 5,643,510; 6,494,609; and 6,874,930; all of which are incorporated by reference. The present invention relates generally to mixers used in the formulation of gypsum slurries in the production of gypsum wallboard.
A gypsum wallboard mixer typically includes a housing defining a mixing chamber with inlets for receiving sources of calcined gypsum and water, among other additives well known in the art. The mixer includes an impeller or other type of agitator for agitating the contents to be mixed into a mixture or slurry. Such mixers typically have a rectangular discharge gate or slot with a cutoff block or door. The discharge gate controls the flow of slurry from the mixer, but is difficult to adjust to change slurry flow when product requirements change, such as when thicker or thinner wallboard is desired.
Foam and/or other additives are typically added through a foam injection port on an outer side wall of the discharge gate through which aqueous foam or other desired additives, such as retarders, accelerators, dispersants, starch, binders, and strength-enhancing products including poly-phosphates, sodium trimetaphosphate, and the like, after the slurry has been substantially mixed. To promote more uniform mixing of foam or other additives into the gypsum slurry, designers have the goal of preventing the foam and/or additives from flowing backwards and entering into the mixing chamber to prematurely mix with the gypsum slurry.
An inlet opening of the discharge gate for receiving the mixed slurry is typically equipped with lump bars or grating for preventing slurry lumps from entering into the discharge gate. As a result, in some applications, the inlet opening is configured to be large and oversized, and causes slurry flow problems when the foam and/or additives are injected into a cavity of the discharge gate. Specifically, the large inlet opening of the discharge gate makes it difficult to match the cavity area to the volume of mixed slurry flowing through from the inlet opening to an outlet opening of the discharge gate. If the grate is not full, lumps can form from eddy patterns created by the slurry flow in the mixer.
Thus, several factors combine to provide a gypsum wallboard mixer that operates properly, and these include the size of the discharge gate, whether or not lump bars obscure the gate opening, the volume of slurry in the mixer, and the point of introduction of foam into the slurry.
Therefore, there is a need for an improved discharge gate having the injection port that provides the desired 90° injection angle, and the cavity area that matches the volume of mixed slurry flowing through the mixer.
The present disclosure provides an apparatus that promotes an improved slurry flow and mixture inside the discharge gate, and provides an improved injection port configuration. In the prior art mixers, the foam is introduced to the slurry after the slurry exits the gate. An important aspect of the present discharge gate is that the gate has an injection port that is positioned at a 90° angle relative to a running or flow direction of the mixed slurry flow through the gate. The injection point or points are preferably located in upper and/or lower walls of the gate. Further, it is known in the art that very small adjustments to an injection location and orientation creates significant performance implications. The 90° angle orientation of the injection port in the discharge gate has been discovered to be very beneficial in promoting desired distribution of foam throughout the slurry.
Also, it is important to keep the cavity of the discharge gate full of slurry as the slurry flows from the mixing chamber for enhancing foam and slurry blending in the discharge gate. While the mixing dynamics of the foam and the slurry are somewhat unpredictable, it is important to achieve uniform mixing of the foam with the moving slurry as it exits the gate. In the present mixer gate, a gate filler block is installed inside the gate for more readily filling the gate with slurry. As such, the foam injected into the gate is more uniformly mixed with the slurry.
In one embodiment, a discharge gate for a gypsum slurry mixer is provided, and includes a lower member having an inlet opening configured for receiving the slurry, and an outlet opening configured for delivering the slurry to a dispensing device. An upper member attached to the lower member, at least one of the upper and lower members having at least one opening for accommodating insertion of an injection port for introducing the foam to the slurry. A cavity is defined in the gate and is configured for mixing the foam and slurry, and is defined by inner surfaces of the lower member and the upper member.
In another embodiment, a gypsum wallboard slurry mixer discharge gate is provided. Included in the discharge gate is a lower member having an inlet opening configured for receiving the slurry, and an outlet opening configured for delivering the slurry. Also included in the discharge gate is an upper member attached to the lower member, wherein at least one of the upper and lower members has at least one opening for accommodating insertion of an injection port for introducing the foam to the slurry. In the preferred embodiment, the injection port is oriented generally perpendicular to a direction of flow of slurry through the discharge gate. A cavity is constructed and arranged for mixing the foam and slurry in the discharge gate, and is defined by inner surfaces of the lower member and the upper member. A gate filler block having an inlet side and an outlet side is inserted into the cavity, wherein the inlet side has an inclined ramp continuously following along a contour of the inlet opening of the discharge gate.
Referring now to
An agitator 30 is disposed in the mixing chamber 16 and has a generally vertical drive shaft 32 positioned concentrically with the vertical axis 18 and extends through the upper radial wall 20. The shaft 32 is connected to a conventional drive source, such as a motor, for rotating the shaft at whatever speed is appropriate for agitating the agitator 30 to mix the contents of the mixing chamber 16. Speeds in the range of 275-300 rpm are common. This rotation directs the resulting aqueous slurry in a generally centrifugal direction, such as in a clockwise outward spiral indicated by the arrow A. The direction of rotation is a function of the mixer and gate design and/or construction, and may vary to suit the application. It should be appreciated that this depiction of an agitator is relatively simplistic and meant only to indicate the basic principles of agitators commonly employed in gypsum slurry mixing chambers known in the art. Alternative agitator designs, including those employing pins or paddles, are contemplated. In addition, the present gate design is contemplated for use with pinless mixers used for agitating gypsum slurries.
At a mixer outlet 34, a discharge gate 36 is attached to the peripheral wall 24 of the mixer 12 for the discharge of the major portion of the well-mixed slurry into a dispensing apparatus 38 via a conduit 40 in a direction indicated by the arrow B. As is known in the art, the ultimate destination of the slurry emitted by the dispensing apparatus is a gypsum wallboard production line, including a moving conveyor belt. While the geometry of the outlet 34 is shown as rectangular in cross-section, other suitable shapes are contemplated depending on the application. Also, while it is contemplated that the specific configuration of the mixer 12 may vary, it is preferred that the present mixer is of the centrifugal type commonly used in the manufacture of gypsum wallboard, and also of the type in which the outlet 34 dispenses the slurry tangentially to the housing 14. A cutoff block 42 is integrally formed with the discharge gate 36 to mechanically adjust the flow of slurry for the desired thickness of wallboard, typically ranging from ¼″ to 1″.
During operation, the cutoff block 42 often creates a site for the premature setting of gypsum, resulting in slurry buildup and eventual clogging and disruption of the production line. Further, when the discharge gate 36 is set for thick wallboard and a conversion is made to thin wallboard, insufficient backpressure is provided in the mixing chamber 16, which in some cases results in an incomplete and nonuniform mixing of slurry constituents. Also, the inadequate backpressure results in dead spots or slow spots in the centrifugal internal flow in the mixing chamber 16, causing premature setup of the slurry and unwanted lumps in the mixture. In such instances, the wallboard line must be shut down for maintenance, causing inefficiencies in production. As explained in greater detail below, the present discharge gate 36 provides solutions to these operational problems.
Referring now to
Included in the lower member 44 are an inlet opening 52 configured for receiving the mixed slurry from the mixing chamber 16, and an outlet opening 54 configured for delivering the mixed slurry to the dispensing apparatus 38 (
An important feature of the present discharge gate 36 is that a gate filler block 62 having a predetermined thickness T (
Referring now to
An exemplary angle α (
This configuration of the gate filler block 62 allows that a volumetric area of the cavity 48 is matched to the volume of mixed slurry flowing through therein, and that the foam is distributed and filled evenly and uniformly for providing a desired mixture of the foam and slurry. While the gate filler block 62 is shown that is installed on the inner bottom surface 64 of the lower member 44, it is also contemplated that the gate filler block is optionally installed on an inner top surface 74 (
Referring now to
As illustrated in
Referring now to
An important aspect of the present injection port 80 is that the port is attached to the upper member 46 in fluid communication with the opening 76 such that the foam passes through the port, and is injected into the moving slurry in the cavity 48 at an approximately 90° angle relative to the running direction of the slurry flow in the discharge gate 36. The flared end 84 of the injection port 80 is preferably substantially flush with the inner top surface 74 of the upper member 46 inside the cavity 48. This configuration of the injection port 80 achieves the desired form injection angle of 90 degrees relative to the slurry flow, and prevents the form and/or additives from flowing back and entering into the mixing chamber 16 (
It has been found that the present mixer gate configuration, particularly with the gate filler block, has facilitated the dispensing of gypsum slurries from mixers with reduced lumps, and while maintaining desired flow volumes. Also, the introduction of the foam into the slurry is performed so that there is less risk of foam being reintroduced into the mixer. The present gate is also usable with conventional gate bars provided to reduce the flow of lumps into the slurry downstream of the mixer.
While a particular embodiment of the present discharge gate has been shown and described, it will be appreciated by those skilled in the art that changes and modifications may be made thereto without departing from the present disclosure in its broader aspects.
The present application claims priority under 35 USC 119(e) based on U.S. Provisional Application No. 62/000,244 filed May 19, 2014.
Number | Date | Country | |
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62000244 | May 2014 | US |