Radial flow electrostatic filter
AssigneeGulf Research & Development Company
InventorsJames H. Crissman, G. Ray Fritsche, Frederick B. Hamel, Lloyd W. Hilty
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AssigneeGulf Research & Development Company
InventorsJames H. Crissman, G. Ray Fritsche, Frederick B. Hamel, Lloyd W. Hilty
Estimating the term…
A filter for separating finely divided solid particles that may be electrically conducting from electrically nonconducting liquids has means for directing the liquid to be filtered in a radial flow pattern through a filter bed of glass beads to which a high-voltage gradient is applied. A central tubular electrode that serves as a conduit for the liquid extends longitudinally through the filter bed within a concentric cylindrical outer electrode spaced between the central electrode and the casing wall of the filter. After filtering until the electrical current through the filter bed exceeds a predetermined maximum, the voltage gradient is discontinued and the filter backflushed by flowing liquid upwardly through the filter at a rate that expands the filter and causes movement of the beads relative to one another and to the cylindrical outer electrode to remove deposited solids from the beads and from the electrode. The radial flow pattern allows a greatly increased flow rate as compared to longitudinal flow with a highly efficient separation of the solid particles.
A filter for removal of finely divided solid particles from liquids of low electrical conductivity comprising a vertical cylindrical casing, a particulate filter bed of substantially spherical, smooth-surfaced, nondeformable particles of high electrical resistivity within the casing, a central electrode extending vertically through at least a portion of the filter bed, a vertical cylindrical perforated outer electrode extending longitudinally in the filter bed concentric with the central electrode, means for applying a voltage gradient in the range of 5 to 20 kv per inch between the central electrode and outer electrode, and inlet and outlet means constructed and arranged to direct liquid to be filtered radially through the particulate bed.
A filter for the separation of finely divided solid particles from a liquid of low electrical conductivity comprising a cylindrical casing, a particulate filter bed resting on the lower end of the casing comprising glass beads having a size in the range of approximately 1/8 inch to approximately 1/4 inch and a depth of approximately 75 percent of the length of the casing, a tubular central perforated electrode extending from one end of the casing vertically through at least a portion of the filter bed, said central electrode being perforated over an interval within the filter bed, a perforated cylindrical outer electrode concentric with the central electrode, a perforated cylindrical liner within the casing and joined at its upper and lower ends to the casing, conductors extending through the casing and supporting the outer electrode at a midpoint between the central electrode and the liner in the filter bed with its upper end below the top of the filter bed and its lower end above the bottom of the filter bed, bushings supporting the conductors and insulating said conductors from the casing, inlet means constructed and arranged to deliver liquid to be filtered into the central electrode, an outlet through the wall of the casing between the upper and lower ends of the liner, means for grounding the central electrode, means for connecting the conductors to an electric power source for applying a voltage gradient of 5 to 20 kv per inch between the electrodes, a backflush inlet opening through the lower end of the casing, a backflush outlet at the upper end of the casing, and valve means to control flow of liquid through the filter during backflushing and filtering.
A method of filtering finely divided solid particles from a liquid of low electrical conductivity comprising flowing the liquid radially through a cylindrical particulate filter bed of substantially spherical, smooth-surfaced, nondeformable particles of low electrical conductivity in a vertical cylindrical casing, maintaining a voltage gradient through the filter bed of 5 to 20 kv per inch between a central electrode in the filter bed and an outer cylindrical electrode in the filter bed concentric with the central electrode, periodically interrupting the voltage gradient and radial flow of liquid to be filtered, and flowing a backflush liquid upwardly through the filter bed and out of the upper end of the casing at a rate to remove deposited solids from the filter bed while the voltage gradient is interrupted.
A filter for removal of finely divided solid particles from liquids of low electrical conductivity comprising a vertical cylindrical casing, a particulate filter bed of nondeformable solid particles of high electrical resistivity and a size in the range of 3 to 6 mesh within the casing, a central electrode extending vertically through at least a portion of the filter bed, a vertical cylindrical outer electrode extending longitudinally in the filter bed concentric with the central electrode at substantially the elevation of the central location, means for applying a voltage gradient in the range of 5 to 20 kv per inch between the central electrode and outer electrode, and inlet and outlet means constructed and arranged to direct liquid to be filtered radially through the particulate bed.
A filter for removal of finely divided solid particles from liquids of low electrical conductivity comprising a vertical cylindrical casing, a particulate filter bed of gravel having a size of approximately 3 to 6 mesh within the casing, a central electrode extending vertically through at least a portion of the filter bed, a vertical cylindrical outer electrode extending longitudinally in the filter bed concentric with the central electrode, means for applying a voltage gradient in the range of 5 to 20 kv per inch between the central electrode and outer electrode, and inlet and outlet means constructed and arranged to direct liquid to be filtered radially through the particulate bed.
A filter for the separation of finely divided solid particles from a liquid of low electrical conductivity comprising a vertical cylindrical casing, a particulate filter bed within the casing comprising substantially spherical, smooth-surfaced, nondeformable particles of high electrical resistivity having a size in the range of approximately 3 mesh to 6 mesh, a tubular central electrode extending vertically through at least a portion of the filter bed, said central electrode being perforated only in the interval within the filter bed, a vertical cylindrical perforated liner within the casing adjacent but spaced from the wall of the casing to provide an annular passage adjacent the wall of the casing, means closing the upper and lower ends of the annular passage, the perforations in the liner being of a size to prohibit passage of particles of the filter bed therethrough, said liner defining the outer boundary of the filter bed, a perforated cylindrical outer electrode concentric with the central electrode supported vertically at a midpoint between the central electrode and the liner with its upper end below the top of the filter bed and its lower end above the bottom of the filter bed, liquid inlet means constructed and arranged to deliver liquid to be filtered into the central electrode, an outlet through the casing communicating with the annular passage, means for grounding the central electrode, the casing and the liner, means connecting the outer electrode to an electric power source adapted to apply a voltage gradient of 5 to 20 kv per inch between the central electrode and the outer electrode and between the outer electrode and the liner, a backflush inlet constructed and arranged to deliver backflush liquid into the lower end of the filter bed, a backflush outlet at the upper end of the casing above the filter bed, and valve means to control flow of liquid through the filter during backflushing and filtering.
Dependencies are inferred from the claim text.