Apparatus for solids blending

• US 4,042,220 A
• Filed: 08/17/1976
• Issued: 08/16/1977
• Est. Priority Date: 10/02/1975
• Status: Expired due to Term

• Current Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Original Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Inventors: Marshall, Donald Raymond, Humkey, Robert Garnett, Ryan, Donald James
• Primary Examiner(s): Jenkins, Robert W.
• Application Number:
  US05/714,997
• Time in Patent Office: 364 Days
• Field of Search: 259/95, 259/4, 259/180, 259/150, 259/DIG. 17, 259/18, 259/36, 259/60
• US Class Current: 366/101
• CPC Class Codes: B01F 33/40511 with a central conduit or a central set of conduits

Abstract

Apparatus for the blending of a bed of particulate solids operating cyclically by selectively regulated downward gravity flow of a fraction of the solids, fluidized mixing outside of the bed, followed by recycle to the top of the bed.

Claims

1. A particulate solids blending apparatus comprising, in combination, a vessel containing a settled bed of particulate solids to be blended consisting of an upright top section to which is joined a funnel type bottom section, a draft tube vertically disposed with respect to said top section with lower end in open communication with said funnel type bottom section and upper end in open communication with the top of said top section, means fluidizing a well-mixed fraction of about 0.01 to 0.20 of said solids in the region adjacent said lower end of said draft tube, means entraining solids upwardly through said draft tube, and solids flow-constricting means spaced inwardly from the inside wall of said upright top section disposed in the gravity flow paths of solids contained within said bed maintaining different residence times of separate weight fractions of said solids within said settled bed having residence time ratios in the range of about 1.5 to 5.0 while withdrawing said solids in downward gravity flow from said settled bed to said region adjacent said lower end of said draft tube provided with said means fluidizing solids.

2. A particulate solids blending apparatus comprising, in combination, a vessel containing a settled bed of particulate solids to be blended consisting of an upright cylindrical top section to which is joined an inverted frusto-conical bottom section, a draft tube disposed substantially coaxially with respect to said cylindrical section with lower end in open communication with said frusto-conical bottom section and upper end in open communication with the top of said cylindrical section, means fluidizing a well-mixed fraction of about 0.01 to 0.20 of said solids in the region adjacent said lower end of said draft tube, means entraining solids upwardly through said draft tube, and solids flow-constricting means spaced inwardly from the inside wall of said upright top section disposed in the gravity flow paths of solids contained within said bed maintaining different residence times of separate weight fractions of said solids within said settled bed having residence time ratios in the range of about 1.5 to 5.0 while withdrawing said solids in downward gravity flow from said settled bed to said region adjacent said lower end of said draft tube provided with said means fluidizing solids.

3. A particulate solids blending apparatus according to claim 2 wherein the lower end of said draft tube is enlarged to form an antechamber of increased cross-section wherein fluidization of said solids occurs.

4. A particulate solids blending apparatus according to claim 3 wherein said solids flow-constricting means comprises radially adjustable valve means disposed substantially coaxially of said inverted frusto-conical bottom section and radially disposed solids cross-flow prevention baffles spaced circumferentially at predetermined intervals with respect to said inverted frusto-conical bottom section.

5. A particulate solids blending apparatus according to claim 3 wherein said solids flow-constricting means comprises a multiplicity of orifices of preselected diameters arranged with axes substantially coparallel with elements defining said inverted frusto-conical bottom section and radially disposed solids cross-flow prevention baffles spaced circumferentially at predetermined intervals with respect to said inverted frusto-conical bottom section.

6. A particulate solids blending apparatus according to claim 3 wherein said solids flow-constricting means comprises a plate disposed substantially radially of said draft tube across the interspace defined by the inside surface of said frusto-conical bottom section and the lower outside surface of said antechamber, said plate having a projected planar shape throttling solids flow past said plate in a circumferential pattern effecting withdrawal at preselected different flow rates of separate weight fractions of solids from said bed to said region adjacent said lower end of said antechamber provided with said means fluidizing solids and radially disposed solids cross-flow prevention baffles spaced circumferentially at predetermined intervals with respect to said inverted frusto-conical bottom section.

7. A particulate solids blending apparatus according to claim 3 wherein said antechamber constitutes two opposed frusto-conical sections joined end to end at the large diameter ends with the junction line of said frusto-conical sections disposed within said inverted frusto-conical bottom section.

8. A particulate solids blending apparatus according to claim 3 wherein said solids flow-constricting means comprises a plurality of solids discharge chutes wherein the bottom walls have preselected inward inclinations with respect to the horizontal greater than the angle of repose of said solids and define openings between the chute terminal ends and the entrance end of said antechamber preselected in area to secure predetermined rates of solids discharge therethrough.

9. A particulate solids blending apparatus according to claim 2 wherein said solids flow-constricting means comprise helically formed plates disposed coaxially of said draft tube within the annular space defined by the inside wall of said cylindrical top section and the outside wall of said draft tube.

10. A particulate solids blending apparatus according to claim 2 wherein said solids flow-constricting means comprise planar baffles inclined at an angle to the vertical greater than the normal angle of repose of said solids being blended disposed within the annular space defined by the inside wall of said cylindrical top section and the outside wall of said draft tube.