U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Backwash control for constant volume-pressure filtration system

Patent 4482461 Issued on November 13, 1984. Estimated Expiration Date: Icon_subject December 20, 2002. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

3452586

Filtration system and flow control method therefor
Patent #: 3957637
Issued on: 05/18/1976
Inventor: Morey

Filter with axially shiftable rotating backwash selector
Patent #: 4059518
Issued on: 11/22/1977
Inventor: Rishel

Method and apparatus for automatic control of filtrate quality
Patent #: 4107037
Issued on: 08/15/1978
Inventor: Cavanaugh ,   et al.

Treatment facility with backwash control system
Patent #: 4187175
Issued on: 02/05/1980
Inventor: Roberts ,   et al.

Cleaning process control method for textile barrier filter material Patent #: 4277255
Issued on: 07/07/1981
Inventor: Apelgren

Inventors

Assignee

Application

No. 06/451086 filed on 12/20/1982

US Classes:

210/741, Pressure sensing210/108, Backwash or blowback210/143, AUTOMATIC CONTROL210/791Rehabilitating or regenerating filter medium

Examiners

Primary: Fisher, Richard V.
Assistant: Czaja, John W.

Attorney, Agent or Firm

International Classes

B01D 29/11 (20060101)
B01D 29/50 (20060101)
B01D 29/52 (20060101)

Abstract

In a system having a fluid filter that is automatically backwashed each time the differential pressure thereacross reaches a predetermined value, the desired base rate at which the drop across the filter should increase during its initial filtering sequence (i.e., before backwash) is determined and stored in digital format in a process controller along with a preset maximum differential pressure at which backwash is set to occur. During use of the filter the actual rate of change of the pressure drop thereacross is monitored continuously and compared with the rate that is stored in the controller. Whenever the actual rate of change of the pressure drop across the filter differs from the base rate, which is the usual case, the present backwashing pressure is automatically adjusted--usually downwardly. This reduction continues until the actual drop across the filter finally reaches the adjusted value of the preset backwashing pressure, at which time backwashing of the filter is automatically commenced. In a preferred embodiment, the adjustment is based upon the time differential at a given instant between the actual filter time and the desired or base curve time, and the difference is used to reduce the preset pressure in accordance with the inverse of the base curve rate. In another embodiment the difference between the actual differential pressure across a filter and the desired differential pressure at any instant is determined and subtracted from the preset backwashing pressure.

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