GYPSUM SLURRY MIXER OUTPUT CANISTER

Abstract

A gypsum slurry mixer output canister is provided, including a canister housing having an upper end, an opposite lower end and defining a canister interior, a cover secured to the upper end, a slurry inlet in operational relationship to the upper end, a spiral block associated with the upper end, and having a helical flow surface depending into the interior. A flow distributor is secured to the lower end and is in fluid communication with the interior, and a slurry outlet is defined by the lower canister housing end.

Claims

1. A gypsum slurry mixer output canister, comprising: a canister housing having an upper end, an opposite lower end and defining a canister interior; a cover secured to said upper end; a slurry inlet in operational relationship to said upper end; a spiral block associated with said upper end, and having a helical flow surface depending into said interior; a flow distributor secured to said lower end and being in fluid communication with said interior; and a slurry outlet defined by said lower canister housing end.

2. The canister of claim 1, wherein said upper end has a radially extending flange for accommodating mounting of said cover.

3. The canister of claim 1, wherein said slurry inlet has a non-circular cross-section where said inlet meets said housing.

4. The canister of claim 3, wherein said slurry inlet has a rectangular cross-section where said inlet meets said housing.

5. The canister of claim 1, wherein said spiral block is secured to an underside of said cover.

6. The canister of claim 1, wherein said spiral block has a vertical inlet wall in fluid communication with said slurry inlet, and forming an end of said helical flow surface. 7 The canister of claim 1, wherein said helical flow surface defines a 360 arc.

8. The canister of claim 1, wherein said spiral block has a vertical height of approximately 4.5 inches, 1 inch.

9. The canister of claim 1, wherein said housing has a vertical height of approximately 8.5 inches 1 inch.

10. The canister of claim 1, wherein said housing has a vertical height of approximately 10 inches 1 inch.

11. The canister of claim 1, wherein said flow distributor defines an outlet aperture having a plurality of lobes in fluid communication with a central opening.

12. The canister of claim 1, wherein said flow distributor includes a plurality of radially inwardly projecting teeth defining a plurality of lobe-shaped recesses in communication with a central opening.

13. The canister of claim 12, wherein said teeth define a radially inwardly tapered internal geometry such that tips of said teeth form an innermost circumference of said central opening.

14. The canister of claim 1, wherein said flow distributor has a vertical height of approximately 3.0 inches, 1 inch.

15. The canister of claim 1, wherein said spiral block takes up approximately 50% of a vertical height of said housing.

16. A gypsum slurry mixer output canister, comprising: a canister housing having an upper end, an opposite lower end and defining a canister interior; a cover secured to said upper end; a slurry inlet secured to said upper end; a spiral block associated with said upper end, and having a helical flow surface depending into said interior; a flow distributor secured to said lower end and being in fluid communication with said interior; a slurry outlet defined by said lower canister housing end; and said spiral block having a vertical height taking up approximately 50% of a height of said housing, and said flow distributor having a vertical height of approximately 3 inches.

17. The canister of claim 16, wherein said vertical height of said housing is approximately 8.5 inches, and said vertical height of said spiral block is approximately 4.5 inches.

18. The canister of claim 16, wherein a flow chamber defined between the spiral block and the flow distributor has a vertical height of approximately 1.0 inch.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0016] FIG. 1 is an exploded top perspective view of a first embodiment of the present mixer canister;

[0017] FIG. 2 is a side elevation of the canister of FIG. 1;

[0018] FIG. 3 is a cross-section taken along the line 3-3 of FIG. 2 and in the direction generally indicated;

[0019] FIG. 4 is a top plan view of the canister of FIG. 1;

[0020] FIG. 5 is a front view of the canister of FIG. 1;

[0021] FIG. 6 is an inverted top perspective view of the spiral block of the canister of FIG. 1;

[0022] FIG. 7 is a front view of the spiral block of FIG. 6;

[0023] FIG. 8 is a top perspective view of the flow distributor of the canister of FIG. 1;

[0024] FIG. 9 is a top plan view of the flow distributor of FIG. 8;

[0025] FIG. 10 is a cross-section taken along the line 10-10 of FIG. 9 and in the direction generally indicated;

[0026] FIG. 11 is an exploded perspective view of another embodiment of the present canister;

[0027] FIG. 12 is a side elevation of the canister of FIG. 11;

[0028] FIG. 13 is a cross-section taken along the line 13-13 of FIG. 12 and in the direction generally indicated;

[0029] FIG. 14 is a cross-section taken along the line 14-14 of FIG. 12 and in the direction generally indicated;

[0030] FIG. 15 is a top plan view of the canister of FIG. 11;

[0031] FIG. 16 is a front view of the canister of FIG. 11;

[0032] FIG. 17 is an inverted top perspective view of the spiral block of the canister of FIG. 11;

[0033] FIG. 18 is a side elevation of the spiral block of FIG. 17;

[0034] FIG. 19 is a top perspective view of the flow distributor of the canister of FIG. 11;

[0035] FIG. 20 is a top plan view of the flow distributor of FIG. 19; and

[0036] FIG. 21 is a cross-section taken along the line 21-21 of FIG. 20 and in the direction generally indicated.

DETAILED DESCRIPTION

[0037] Referring now to FIGS. 1-5, a first embodiment of the present slurry mixer output canister is generally designated 10. The canister 10 is constructed and arranged for connection between, and fluid communication with, a mixer output hose 12 and a mixer boot inlet 14. A suitable mixer outlet boot is disclosed in U.S. Pat. No. 8,475,762, which is incorporated by reference. A flow direction of gypsum slurry from the mixer, and intermixed foam, is indicated by arrows A.

[0038] Included in the canister 10 is a canister housing 16 which is preferably cylindrical and tubular, however other tubular shapes are contemplated, including but not limited to polygonal. An upper end 18 of the housing 16 is opposite a lower end 20, and a canister interior 22 is defined within the housing. A radially extending flange 24 is preferably provided to the upper end 18 for accommodating secure mounting of a cover 26. Attachment of the cover 26 to the flange 24 is achieved by fasteners 28, preferably threaded bolts or the like as are well known in the art.

[0039] Located vertically below the flange 24 is a slurry inlet 30 in operational relationship to the upper end 18 of the canister housing 16. At a free end 32, the slurry inlet 30 has a circular cross-section 34 for connection to the mixer output hose 12. However, as the inlet 30 progresses towards its connection to the canister housing 16, the inlet has a non-circular cross-section 36 where said inlet meets said housing. Also, the inlet 30 has an arcuate edge 38 where the inlet joins the preferably cylindrical canister housing 16. Thus, the inlet 30 is in fluid communication with an aperture 40 in the canister housing 16. In the preferred embodiment, the slurry inlet 30 is secured to the canister housing 16 by welding, fasteners and/or chemical adhesive as is well known in the art. Another feature of the canister housing 16 is at least one mounting bar 42 secured to an exterior 44 of the housing for facilitating the mounting of the canister 10 to corresponding mixer infrastructure (not shown).

[0040] Referring now to FIGS. 1, 3, 6 and 7, an important feature of the present canister 10 is a spiral block 46 that depends into the canister interior 22 to create a slurry flow path that follows an interior profile of the housing 16. Also, the spiral block 46, preferably fastened to an underside 48 of the cover 26 by fasteners or the like, fills the canister interior 22 above the aperture 40, or the area between the cover and the aperture. Thus, the presence of the spiral block 46 prevents the unwanted collection of stray slurry that might prematurely set, creating lumps in the resulting wallboard panels.

[0041] More specifically, the spiral block 46 has a generally cylindrical mounting end 50 configured for attachment to the underside 48 of the cover 26. Opposite the mounting end is a helical flow surface 52 that preferably extends a full 360 arc, although with portions of the surface vertically displaced from others. Upon the spiral block 46 being attached to the cover 26 as seen in FIG. 1, the block depends into the canister interior 22.

[0042] As seen in FIG. 6, the spiral block 46 has a vertical inlet wall 54 in fluid communication with the slurry inlet 30 and with the housing aperture 40. Also, the inlet wall 54 forms an end of the helical flow surface 52. An upper edge 56 of the wall 54 defines an upper vertical limit of the helical flow surface 52 as seen in FIG. 6, which actually is the lowest limit of the surface once the spiral block 46 is inverted and inserted into the canister interior 22. Also, the vertical inlet wall 54 is aligned with one edge of the aperture 40 (FIG. 3). Incoming slurry passes through the aperture 40, is directed by the vertical inlet wall 54, and begins a circular or spiral flow in the interior 22 due to the configuration of the helical flow surface 52 of the depending spiral block 46.

[0043] Referring now to FIGS. 2 and 8-10, another component of the present mixer canister 10 is a flow distributor 60 constructed and arranged to accommodate the generally circular or spiral flow created by the spiral block 46 and reorient the flow to be more linear or laminar. The latter flow is more desirable as the slurry is emitted from the boot and flows upon the moving face paper on the wallboard production conveyor, as is well known in the art.

[0044] In the preferred embodiment, the flow distributor 60 is securely located at the lower end 20 of the canister housing 16, and defines a slurry outlet 62. An annular groove 64 on the flow distributor 60 is engaged by at least one fastener 66 such as a set screw (FIG. 2) to secure the flow distributor to the canister housing 16. Also, the flow distributor 60 is in fluid communication with the canister interior 22.

[0045] More specifically, the flow distributor 60 is an integrally formed part, as by machining, casting or the like, and defines an outlet aperture 68 having a plurality of circumferentially arranged lobes 70 in fluid communication with a central opening 72. The lobes 70 are defined by a plurality of radially inwardly projecting teeth 74 (FIG. 9), with each lobe located between two adjacent teeth. Also, the teeth 74 define a radially inwardly tapered internal geometry such that tips 76 of the teeth form an innermost circumference of the central opening 72. As seen in FIG. 10, a wall 78 of the flow distributor 60 defines a generally wedge-shaped cross-section, with the tips 76 of the teeth 74 forming the tip of the wedge. Also, the teeth 74 are formed from upper and lower plate portions 80, 82 that taper towards the tips 76. In the preferred embodiment, the flow distributor 60 has a vertical height defined by the wall 78, and is preferably 3.0 inches tall, 1 inch.

[0046] Referring now to FIGS. 11-21, an alternate embodiment of the present slurry mixer output canister is generally designated 100. Components shared with the canister 10 are marked with identical reference numbers. One main distinction between the two canisters 10, 100 is that the canister housing 16 in the canister 10 has a vertical height of approximately 10 inches 1 inch. However, in the canister 100, a canister housing 102 has a vertical height of approximately 8.5 inches 1 inch. Also, a spiral block 104 has a vertical height of approximately 4.5 inches 1 inch, so that the spiral block has a vertical height taking up approximately 50% of a height of the housing 102.

[0047] Another feature of the canister 100 is that since the flow distributor 60 has a vertical height of approximately 3.0 inches 1 inch, there is approximately 1.0 inch remaining in the canister interior 22. As such, a flow chamber 106 (FIG.13) is defined in the canister interior 22 between the spiral block 104 and the flow distributor 60 has a vertical height of approximately 1.0 inch. It has been found that this arrangement of components within the housing 102 has resulted in enhanced performance, including slurry velocity through the canister 100, in that the flow of slurry through the canister is expedited, and slurry volume is maintained so that unwanted clumping or premature setting is significantly reduced compared to conventional slurry dispensers in wallboard production lines.

[0048] While a particular embodiment of the present gypsum slurry mixer output canister has been described herein, it will be appreciated by those skilled in the art that changes and modifications may be made thereto without departing from the invention in its broader aspects and as set forth in the following claims.