Method for regulating a membrane filtering installation

• US 20050258098A1
• Filed: 12/04/2001
• Published: 11/24/2005
• Est. Priority Date: 12/13/2000
• Status: Abandoned Application

• Current Assignee: Ondeo Services (Veolia Environnement SA)
• Original Assignee: Ondeo Services (Veolia Environnement SA)
• Inventors: Cabassud, Michel, Cabassud, Corrine, Vincent, Nathalie, Laine, Jean-Michel, Durand-Bourlier, Laurence
• Application Number:
  US10/450,381
• Publication Number:
  US 20050258098A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2321/02 Forward flushing
• CPC Class Codes: B01D 2321/2058 by vibration of the membrane, e.g. with an actuator
• 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 65/08 Prevention of membrane fouling or of concentration polarisation
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration

Abstract

The invention concerns a method for avoiding irreversible membrane clogging while maximising productivity, whatever the quality of the fluid at the installation intake. It consists in automatically controlling the installation operating parameters by performances induced by the quality of the fluid to be treated, based on predictions concerning the evolution of the membrane clogging carried out by modelling with a neuron network so as to simulate the long term operating conditions of the membrane filtering installation, the model enabling, on the basis of the quality of the in-flowing fluid and on the state of the membranes during a given cycle, to calculate the evolution of the clogging state of said membranes on a time basis, on a specific horizon, said calculation being performed for a simulated in-flowing quality, constant or variable, on said horizon (H) and to control and adjust the installation operating parameters.

Claims

1. Method of regulating a membrane filtration plant, especially in a potable water production station, designed so as to prevent irreversible clogging of the membranes while maximizing the productivity, whatever the quality of the fluid entering the plant, characterized in that it consists in slaving the plant operating parameters to the performance characteristics induced by the quality of the fluid to be treated, according to the predictions about the change in membrane clogging made by neural network modelling so as to simulate the long-term operation of the membrane filtration plant, the model making it possible:

according to the quality of the incoming fluid and the state of the membranes during a given cycle, to calculate the change in the state of clogging of the said membranes as a function of time, over a defined horizon, the said calculation being carried out for a simulated quality of the incoming fluid, the said quality being constant or varying, over this horizon (H), and

to monitor and adjust the plant operating parameters.

2. Method according to claim 1, characterized in that a clogging level limit is imposed, the regulation being carried out in such a way that the plant operates with a clogging level equal to or less than this limit.

3. Method according to claim 2, characterized in that, at each production cycle:

the experimental values of all the quality parameters and operating conditions are determined on the plant;

the parameters are entered as input into the clogging prediction model based on neural networks, which calculates the change in the clogging over a prediction horizon (H), thereby making it possible to predict the permeability after H production cycles;

the net flow rate imposed is decreased when the permeability after H cycles is less than the permeability limit (Lp_c); and

the net flow rate imposed is increased when the permeability after H cycles is greater than the permeability limit (Lp_c) by varying the permeate flow rate and/or the filtration time.

4. Method according to claim 3, characterized in that the respective values of the permeate flow rate-filtration time pair are slaved in such a way that the permeability after H cycles is equal to or greater than the permeability limit (Lp_c) and that the net flow rate is as high as possible.

5. Method according to claim 3, characterized in that the respective values of one or more of the following operating parameters are slaved:

permeate flow rate or transmembrane pressure, depending on whether the operation is carried out, in production, at constant pressure or at constant flow rate;

filtration time;

circulation flow rate, with possible switching from a recirculation mode to a transverse mode;

purge flow rate of the circulation loop;

backwashing time;

backwashing pressure or backwashing flow rate, depending on whether the operation is carried out at constant pressure or at constant flow rate for the backwashing;

concentration of dissolved chlorine or any other additive in the backwashing water; and

injection/dosing parameters for an additive during the filtration cycle.