Backwash method and apparatus

• US 4,405,466 A
• Filed: 05/03/1982
• Issued: 09/20/1983
• Est. Priority Date: 05/03/1982
• Status: Expired due to Fees

• Current Assignee: Ecodyne Corp. (Berkshire Hathaway Incorporated)
• Original Assignee: Ecodyne Corp. (Berkshire Hathaway Incorporated)
• Inventors: Flynn, George C., Giannelli, Joseph F., Ryan, Leo F.
• Primary Examiner(s): Hart, Charles N.
• Assistant Examiner(s): Czaja, John W.
• Application Number:
  US06/374,350
• Time in Patent Office: 505 Days
• Field of Search: 210/797, 210/798, 210/108, 210/323.2, 210/333.01, 210/333.1, 210/332, 210/411, 210/791, 210/792, 210/793, 210/794
• US Class Current: 210/798
• CPC Class Codes: B01D 2201/0438 mounted substantially vertically on plates at the lower side of the filter elements
• CPC Class Codes: B01D 29/114 arranged for inward flow filtration B01D29/15, B01D29/33 take precedence
• CPC Class Codes: B01D 29/52 in parallel connection
• CPC Class Codes: B01D 29/661 by using gas-bumps
• CPC Class Codes: B01D 36/001 Filters in combination with devices for the removal of gas, air purge systems
• CPC Class Codes: B01D 37/02 Precoating the filter medium; Addition of filter aids to the liquid being filtered devices for feeding reagents C02F1/685 and sub-groups; filter aids

Abstract

The method and apparatus for filtering a liquid including a filter vessel divided into an upper filter compartment and a lower plenum compartment. An external vessel is positioned at or below the elevation of the tops of the filter element fittings in the plenum compartment. A pressurized gas is supplied to the upper portion of the external vessel forcing backwash liquid from the external vessel into the lower portion of the plenum compartment backwashing filter elements within the filter compartment.

Claims

1. A method for cleaning a plurality of filter elements having inner cores vertically positioned within a filter vessel which has a tube sheet dividing the filter vessel into an upper filter compartment and a lower plenum compartment, said filter elements being positioned within said filter compartment and having fittings which extend through said tube sheet downwardly into said plenum compartment, said method comprising:

draining at least a portion of the liquid from the filter vessel, establishing a low flow rate of backwash liquid through a backwash inlet line into the plenum compartment continuing through the filter elements; and

intermittently directing gas under pressure through a gas supply line in communication with an external vessel containing a volume of cleaning liquid for forcing a predetermined volume of the cleaning liquid from the external vessel under gas pressure at a high flow rate into the plenum compartment and through the filter elements such that the total volume of cleaning liquid directed through the filter elements during each cycle is in the range of 1.0 to 3.0 times the total filter element core void volume.

2. The method as defined in claim 1 wherein the volume of cleaning liquid is intermittently cycled through the filter elements a plurality of times.

3. The method as defined in claim 1 wherein each cycle of cleaning liquid lasts in the range of one to six seconds.

4. The method as defined in claim 1 wherein a portion of the volume of cleaning liquid cycled from the external vessel is directed through a gas surge line in communication with a lower portion of the external vessel and an upper portion of the plenum compartment above the elevation of the lower ends of the fittings and the remaining portion of the volume of cleaning liquid cycled from the external vessel is directed through a connecting line in communication with a lower portion of the external vessel and a lower portion of the plenum compartment such that a gas-liquid interface in the gas surge line reaches the plenum compartment before a gas-liquid interface in the connecting line reaches the plenum compartment.

5. The method as defined in claim 4 wherein the volume of cleaning liquid which is directed through the filter elements during each cycle is equal to 0.2 to 0.8 times the total filter element core void volume at such time as the gas-liquid interface in the gas surge line reaches the plenum compartment.

6. The method as defined in claim 4 wherein the level of liquid within the cores of the filter elements during each cycle is below the tops of the filter elements at such time as the gas-liquid interface in the gas surge line reaches the plenum compartment.

7. The method as defined in claim 6 wherein the sum of the volume of liquid directed into the filter element cores prior to the gas-liquid interface in the gas surge line reaching the plenum compartment plus the available plenum liquid volume in the plenum compartment is at least 1.0 times the total filter element core void volume.

8. Apparatus for filtering liquids comprising:

a filter vessel;

a tube sheet dividing said vessel into an upper filter compartment and a lower plenum compartment;

a plurality of filter element fittings extending through said tube sheet and downwardly into said plenum compartment;

a plurality of filter elements vertically mounted on said fittings in said filter compartment;

an external vessel positioned outside of said filter vessel at an elevation at or below the elevation of the tops of said fittings;

a gas supply line in communication with an upper portion of said external vessel;

a backwash liquid inlet line in communication with a lower portion of said plenum compartment and a lower portion of said external vessel; and

a gas surge line in communication with a lower portion of said external vessel and an upper portion of said plenum compartment.

9. The apparatus as defined in claim 8 wherein the elevation of one end of said gas surge line is selectively adjustable within said external vessel.

10. The apparatus as defined in claim 8 wherein the volume of said external vessel plus the volume of said plenum chamber above the lower ends of said fittings minus the internal and material volume of said fittings is equal to 1.0 to 3.0 times the total filter element core void volume.

11. The apparatus as defined in claim 10 wherein the diameter of said gas surge line is substantially smaller than the diameter of said backwash line.