Filtration monitoring and control system

• US 6,077,435 A
• Filed: 01/12/1998
• Issued: 06/20/2000
• Est. Priority Date: 03/15/1996
• Status: Expired due to Term

• Current Assignee: Evoqua Water Technologies LLC (Xylem, Inc.)
• Original Assignee: USF Filtration and Separations Group, Inc. (Siemens AG)
• Inventors: Johnson, Warren Thomas, Kensett-Smith, Brett, Drummond, Humphrey John Jardine, Maxwell, Ian Andrew, Beck, Thomas William
• Primary Examiner(s): Drodge, Joseph W.
• Application Number:
  US08/913,901
• Time in Patent Office: 890 Days
• Field of Search: 210/90, 210/103, 210/108, 210/134, 210/135, 210/138, 210/139, 210/140, 210/141, 210/142, 210/143, 210/257.1, 210/257.2, 210/321.69, 210/333.01, 210/500.3 , 210/636, 210/637, 210/650, 210/739, 210/741, 210/791, 210/96.1, 210/96.2, 73/38, 73/40, 96/421, 96/422, 96/425, 96/428, 95/19, 95/20, 95/23
• US Class Current: 210/636
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 37/046 by pressure measuring
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/102 Detection of leaks in membranes

Abstract

A method and apparatus for determining the fouling effect of a feedstream on a filter having known characteristics disclosed. The method comprises passing the feedstream through a filter (5) having known characteristics; determining the change in resistance to flow of the feedstream across the filter, either continuously or over a number of time intervals and from this data, calculating a feed fouling index (FFI) representative of the fouling characteristics of the feedstream with respect to the filter. A method and apparatus for monitoring the operation of a filtration system is also disclosed the method comprising sampling system parameter values at selected locations within the filtration system at a predetermined sampling rate; generating a parameter profile characteristic from the sampled parameter values at predetermined intervals of time; and analysing the parameter profile characteristic to determine correct operation of the filtration system. A further method and apparatus of monitoring and controlling a filtering system based on backwash efficiency is also disclosed, the method comprising determining resistance values of filtering elements used in the filtering system at predetermined times during the backwash cycle of the system by monitoring a number of operating parameters of the system; calculating a backwash efficiency value representative of the efficiency of the backwash cycle of the filtering system using the resistance values determined; and controlling the operation of the filtering system in dependence on the value of the backwash efficiency calculated.

Claims

1. A method of determining the fouling effect of a feedstream on a filter having known characteristics, said method comprising the steps of:

i) passing the feedstream through a filter having known characteristics;

ii) determining the change in resistance to flow of the feedstream across the filter, either continuously or over a number of time intervals; and

iii) using the information determined from step ii), calculating a feed fouling index (FFI) representative of fouling characteristics of the feedstream with respect to the filter, where ##EQU6## with FFI=Feed Fouling Index, Δ

R=change in resistance, V=volume of feedstream filtered and, Δ

(V/A)=change in the ratio of volume of feedstream filtered to filter area.

2. A method according to claim 1, wherein the change in resistance across the filter is plotted as a function of volume filtered and the FFI is calculated as the gradient of a curve so plotted at a point or interval where the curve approaches a straight line.

3. A method according to claim 2, wherein the change in resistance is measured by taking readings of the cumulative volume of feedstream passing through the filter over time.

4. A method according to claim 2, wherein the filter is a membrane and pressure sensing devices are positioned on either side of the filter to relate resistance changes in terms of trans-membrane pressure (TMP) drop.

5. An on-line method of monitoring and controlling a filtering system, said method comprising the steps of:

i) determining a resistance value of filtering elements used in the filtering system by monitoring a number of operating parameters of the system;

ii) calculating a feed fouling index (FFI) representative of the fouling characteristics of the feedstream with respect to the filtering system using the resistance value determined in i), where ##EQU7## with FFI=Feed Fouling Index, Δ

R=change in resistance, V=volume of feedstream filtered and Δ

(V/A)=change in the ratio of volume of feedstream filtered to filter area; and

iii) controlling operations of the filtering system in dependence on the value of the feed fouling index calculated.

6. An off-line method of determining the potential fouling effect of a feedstream, said method including the steps of:

i) passing a sample of the feedstream at a predetermined pressure through a filter having known characteristics;

ii) determining a change in resistance to flow of the feedstream across the filter, either continuously or over a number of time intervals; and

iii) using the information determined from step ii), calculating a feed fouling index (FFI) representative of fouling characteristics of the feedstream sample on the known filter, where ##EQU8## with FFI=Feed Fouling Index, Δ

R=change in resistance, V=volume of feedstream filtered and Δ

(V/A)=change in the ratio of volume of feedstream filtered to filter area.

7. The method according to claim 6 wherein the filter is a membrane and further including the step of correlating the FFI with a second FFI calculated for a membrane filter for use in a filtration unit.

8. The method according to claim 6, wherein the change in resistance across the filter is plotted as a function of volume filtered and the FFI is calculated as the gradient of a curve so plotted at a point or interval where the curve approaches a substantially straight line.

9. The method according to claim 6 wherein the change in resistance of the filter is measured by recording, at a number of predetermined points in time, the cumulative volume of feedstream having passed through the filter.

10. The method according to claim 6 wherein pressure sensing devices are used to measure or estimate changes in resistance across the filter over time.

11. The method according to claim 6 wherein the FFI is calculated by a computer in response to entry of the resistance or pressure data.

12. The method according to claim 11 wherein the computer extrapolates from the entered data to provide a more accurate calculation of FFI.

13. An apparatus for use in determining the potential fouling effect of a feedstream comprising:

a filter having known properties;

means to pass a sample of the feedstream through said filter at a predetermined pressure;

means for measuring the change in resistance to flow of the feedstream through the filter over time; and

means for calculating quantitatively a feed fouling index (FFI) indicative of potential fouling effect of the feedstream on the filter based on the measured change in resistance to flow, where ##EQU9## with FFI=Feed Fouling Index, Δ

R=change in resistance, V=volume of feedstream filtered and Δ

(V/A)=change in the ratio of volume of feedstream filtered to filter area, so as to estimate the potential fouling effect of the feedstream on other known filters.

14. Apparatus according to claim 13 wherein the means to pass the feedstream sample through the filter includes a container for holding the sample, and means for pressurising the sample within the container for delivery of the sample to the filter at a preselected pressure.

15. Apparatus according to claim 14 wherein the pressurising means is a manually operated pump.

16. Apparatus according to claim 13 or 14 wherein the container and pressurising means are provided in the form of a modified manually operated garden-spraying apparatus.

17. Apparatus according to claim 14 wherein the filter uses a filter element of the cellulose acetate type.

18. Apparatus according to claim 14 wherein one or more manually operable valves are provided to allow for priming and cleaning of the apparatus.

19. A method of monitoring the operation of a filtration system comprising the following steps:

a) sampling system parameter values at selected locations within the filtration system at a predetermined sampling rate;

b) generating a parameter profile characteristic from the sampled parameter values at predetermined intervals of time;

c) determining the change in resistance to flow of the feedstream across the filter, either continuously or over a number of time intervals, where ##EQU10## with R=resistance, Δ

P=change in pressure across the filter, A=filter area, η

=viscosity of the feedstream and Q=flow across the filter; and

d) determining optimal operations of the filtration system using the information determined from steps a) to c).

20. A method according to claim 19 wherein the analysing step includes comparing the generated profile characteristic against a desired characteristic and identifying regions within the generated profile where the profile characteristic diverges from the desired characteristic.

21. An apparatus for monitoring the operation of a filtration system comprising:

a) means for sampling system parameter values at selected locations within the filtration system at a predetermined sampling rate;

b) means for generating a parameter profile characteristic from the sampled parameter values at predetermined intervals of time;

c) means for determining the change in resistance to flow of the feedstream across the filter, either continuously or over a number of time intervals, where ##EQU11## with R=resistance, Δ

P=change in pressure across the filter, A=filter area, η

=viscosity of the feedstream and Q=flow across the filter; and

d) means for determining optimal operations of the filtration system using the information determined from means a) to c).

22. Apparatus according to claim 21 wherein the means for analysis includes means for comparing the generated profile characteristic against a desired characteristic and identifying regions within the generated profile where the profile characteristic diverges from the desired characteristic.

23. Apparatus according to claim 22 wherein as a result of the comparison, the analysis means indicates likely faults causing the divergence and suggests possible solutions so that the faults may be corrected or circumvented.

24. Apparatus according to claim 23 wherein a user is provided with an interactive display of the generated profile characteristic and the user can indicate an area of the generated profile characteristic the user is interested in and obtain details as to faults and solutions in regard to analysis of the area of the generated profile characteristic.

25. A method of monitoring and controlling a filtering system, said method comprising the steps of:

i) determining resistance values of filtering elements used in the filtering system at predetermined times during the backwash cycle of the system by monitoring a number of operating parameters of the system;

ii) calculating a backwash efficiency value representative of the efficiency of the backwash cycle of the filtering system using the resistance values determined in i), where ##EQU12## and BWE=backwash efficiency, and R_i =resistance at time i; and

iii) controlling operations of the filtering system in dependence on the values of the backwash efficiency calculated.

26. A method according to claim 25 wherein the predetermined times during the backwash cycle are just after a previous backwash, just before a next backwash and just after said next backwash.

27. Apparatus for monitoring and controlling a filtering system comprising:

i) means for determining resistance values of filtering elements used in the filtering system at predetermined times during the backwash cycle of the system by monitoring a number of operating parameters of the system;

ii) means for calculating a backwash efficiency value representative of the efficiency of the backwash cycle of the filtering system using the resistance values determined in i), where ##EQU13## and BWE=backwash efficiency, and R_i =resistance at time i; and

iii) means for controlling operations of the filtering system in dependence on the values of the backwash efficiency calculated.

28. Apparatus according to claim 27 wherein the predetermined times during the backwash cycle are just after a previous backwash, just before a next backwash and just after said next backwash.