Method of operating and monitoring a group of filter membrane modules, and a group of modules implementing the method

• US 6,001,254 A
• Filed: 12/08/1997
• Issued: 12/14/1999
• Est. Priority Date: 04/14/1995
• Status: Expired due to Term

• Current Assignee: Aquasource Incorporated (Essential Utilities, Inc.)
• Original Assignee: Aquasource Incorporated (Essential Utilities, Inc.)
• Inventors: Saux, Franc, Espenan, Jean-Michel
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US08/930,803
• Time in Patent Office: 736 Days
• Field of Search: 210/650, 210/257.2, 210/333.1, 210/333.01, 210/636, 210/90, 210/195.2
• US Class Current: 210/636
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/12 Use of permeate
• CPC Class Codes: B01D 61/12 Controlling or regulating
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration

Abstract

A method of operating and monitoring a group of filter membrane modules connected in parallel and with the modules being periodically backwashed, in which:

raw water to be treated is injected at a regulated pressure and the permeate outlet pressure is regulated to less than the inlet pressure;

the group is provided with a water meter (60) on the raw water inlet duct and with three pressure sensors, one on the raw water inlet, one on the permeate outlet, and one on the backwash circuit, the meter and the sensors (100) delivering signals to a controller;

each module is backwashed in succession with permeate from the other modules, with each module being individualized at that moment, thereby making it possible with aid of the water meter and of the pressure sensors to determine the permeability (150) in backwashing specific to the module as individualized in this way, and also to determine the production permeability of the remainder of the modules; and

the values determined in this way are compared with reference values in order to modify the periodicity of backwashes and to proceed with module cleaning, and also to detect any anomaly in operation.

Claims

1. A method of operating and monitoring a group of filter membrane modules connected in parallel with the modules being backwashed periodically, wherein:

raw water to be treated is injected into the group of modules at a regulated pressure and the outlet pressure of the premeate (filtered water) is regulated to a value that is lower than that of the inlet pressure, but nevertheless sufficient to enable backwashing operations;

the group of modules is provided with a water meter on the raw water inlet duct and with three pressure sensors, a first on the raw water inlet, a second on the permeate outlet, and a third on the backwashing circuit, the meter and the sensors delivering signals to a controller;

the modules are backwashed successively one after another, using the permeate from the other modules, thereby individualizing each module while it is being backwashed, thus making it possible with the water meter and the pressure sensors to determine the permeability in backwashing specific to the module thus individualized, and also determine the production permeability of the remaining modules; and

the permeability values obtained in this way are compared with ideal values, with threshold values, and/or with values from earlier cycles so that, depending on the diagnosis obtained, the periodicity of backwashing is modified, the group of modules is cleaned, or an operating anomaly is detected, thereby enabling it to be corrected.

2. A method according to claim 1, wherein the group of modules is cleaned and the circuit is chlorinated during prolonged stops in production from the group of modules, a common pump on the permeate circuit providing circulation in the cleaning circuit or circulation in the chlorination circuit.

3. A method according to claim 2, wherein by setting into motion said common pump and opening valves of the cleaning circuit, a cleaning substance is caused to be sucked into the cleaning circuit and through the filter membranes.

4. A method according to claim 1, wherein the pressure signals and the meter signal are provided to an operator who calculates the permeabilities, compares them with specified reference values, and proceeds with cleaning when necessary.

5. A method according to claim 1, wherein the pressure sensors and the meter signal are delivered to a controller which includes a microprocessor whose software computes the permeabilities, compares them with specified reference values, and proceeds in automatic manner with cleaning when necessary.

6. A water treatment installation comprising a plurality of filter membrane modules (M₁, . . . , M_n) connected in parallel,

individual ducts (21, . . . , 28)for feeding said modules, said individual ducts branching from a first common duct (1:

2) fitted with a water meter (C₁), with a downstream pressure regulator (VR₁), and with an inlet pressure sensor (P₁),

means for conveying the permeate from each module to a second common duct (4) fitted with an outlet pressure sensor (P₂) and with an upstream pressure regulator (VR₂);

a backwash circuit comprising a common backwash water feed duct (5) configured to feed each module (M_i) in succession with backwash water constituted by the permeate delivered by the other modules (-M_i), a valve (EV₁₁) of the backwash water inlet duct (5_i) configured to deliver said backwash water while the other valves (EV_1n) of the other duct (5_n) are closed, and an outlet duct (6_i) for backwash water leading to a common drain duct (6); and

the common backwash water feed duct (5) is fitted with a pressure sensor (P₃),

means for computing the permeability at each module based on data from the pressure sensors and the water meter, means for comparing the permeability with specified reference values to determine when cleaning is necessary, and means to effect cleaning of the individual modules by automatically operating said valves so as to direct backwash from the other modules through each module in succession.

7. An installation according to claim 6, wherein a cleaning circuit includes a cleaning substance pan (BO) connected by a duct (7) provided with a valve (V₉) for feeding raw water to at least one module and to the drain duct (6) via a valve (V₈), a duct (71) provided with a valve (V₇) for taking permeate from the common backwash water feed duct (5) and a chlorination circuit which includes a chlorine dispenser (D₂) on said common feed duct (5);

a duct (60) fitted with a circulation pump (C) connecting the common backwash water feed duct (5) and the common permeate drain duct (4) in such a manner that the chlorination circuit and the cleaning circuit use the same circulation pump (C).

8. An installation according to claim 7, wherein opening the cleaning circuit valves (V₇, V₉) and putting the circulation pump (C) into operation give rise to cleaning substance being sucked from the cleaning substance pan (BO) and through the membranes of the modules (M₁, . . . , M₈).

9. An installation according to claim 6, wherein each of the individual raw water feed ducts (21, . . . , 28) for the modules (M₁, . . . , M₈) include respective bypass branches (21a, . . . , 28a) each connected to a second end of the corresponding module.

10. An installation according to claim 9, wherein said bypass branch ducts (21a, . . . , 28a) are fitted with respective recirculating pumps (P₁₀, . . . , P₈₀).

11. An installation according to claim 6, wherein the chlorine dispenser (D₂) of the chlorination circuit is a static chlorine dispenser.

12. An installation according to claim 6, wherein the valves are selected from manually-controlled valves, electrically-controlled valves, hydraulically-controlled valves, pneumatically-controlled valves, and combinations thereof.