METHOD FOR CONTROLLING FOULING OF A MEMBRANE FILTER

• US 20080277340A1
• Filed: 05/07/2007
• Published: 11/13/2008
• Est. Priority Date: 05/07/2007
• Status: Active Grant

• Current Assignee: I. Kruger Inc. (Veolia Environnement SA)
• Original Assignee: I. Kruger Inc. (Veolia Environnement SA)
• Inventors: DiMassimo, Richard W., Hong, Sun-Nan, Zhao, Hong W.
• Granted Patent: US 7,459,083 B1
• Time in Patent Office: Days
• US Class Current: 210/620
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/02 Forward flushing
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation
• CPC Class Codes: C02F 2209/006 comprising a software program or a logic diagram
• CPC Class Codes: C02F 2209/03 Pressure
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: C02F 3/30 Aerobic and anaerobic processes
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A membrane bioreactor system includes one or more biological reactors and one or more membrane tanks with each membrane tank having one or more membrane filters. To control membrane fouling, various process control variables are employed. First, the membrane filters are cleaned by an air scouring process where bubbles are moved upwardly adjacent the membrane filters and clean the same in the process. To control membrane fouling, a process is utilized that dynamically varies the air scouring flow rate (V) as a function of transmembrane pressure (TMP). In addition, the process entails allowing permeation to start and stop which results in a series of cycles where each cycle includes a permeation phase and a relaxation phase. The duration of the relaxation phase (TR) and the duration of the permeation phase (TP) is varied from cycle to cycle as a function of one or more process variables including the change in TMP over a selected period within a membrane phase, or the change in TMP over a selected time period spanning at least two membrane phases.

Claims

1-33. -33. (canceled)

34. A method for controlling fouling of a membrane filter in a biological wastewater treatment process, comprising:

directing wastewater influent into one or more reactors and treating the wastewater;

directing the wastewater into and through one or more membrane tanks having one or more membrane filters therein;

filtering the wastewater by directing the wastewater through the membrane filters and producing a permeate;

cleaning the membrane filters with air scouring;

measuring trans-membrane pressures and a liquid level in at least one of the membrane tanks;

executing multiple control cycles to control scouring air flow rate, flux, permeation phase duration, and relaxation phase duration;

in at least one of the control cycles, optionally adjusting each of scouring air flow rate and flux as a function of the measured trans-membrane pressures and of the measured liquid level in the membrane tank;

in at least one of the control cycles, optionally adjusting each of relaxation phase duration and flux as a function of the measured trans-membrane pressures and of the measured liquid level in the membrane tank; and

in at least one of the control cycles, optionally adjusting each of flux and permeation phase duration as a function of the measured liquid level in the membrane tank.

35. The method of claim 34 including:

measuring trans-membrane pressure at a first point in a permeation phase;

measuring trans-membrane pressure at a second point in the permeation phase;

calculating the difference in the trans-membrane pressure measured at the first point in the permeation phase and the trans-membrane pressure measured at the second point in the permeation phase and determining the rate of change of the trans-membrane pressure over a selected period of time; and

adjusting the scouring air flow rate or the flux as a function of the rate of change of the trans-membrane pressure and the measured liquid level in the membrane tank.

36. The method of claim 35 including:

selecting a pair of set point values such that one set point value is larger than the other set point value;

in the event that the rate of change of the trans-membrane pressure is between the selected pair of set point values, adjusting neither the scouring air flow rate nor the flux in response to the difference;

in the event that the rate of change of the trans-membrane pressure is less than the smaller of the selected set point values, decreasing the scouring air flow rate if the velocity is not at a maximum allowable flow rate value; and

in the event that the rate of change of the trans-membrane pressure is greater than the larger of the selected set point values, increasing the scouring air flow rate if the scouring air flow rate is not at the maximum allowable flow rate value or decreasing the flux if the measured liquid level is not at a maximum allowable liquid level value.

37. The method of claim 34 including:

measuring trans-membrane pressure at a first point in a first permeation phase and measuring trans-membrane pressure at a second point in a second permeation phase;

determining the difference between the trans-membrane pressure measured at the first point and the trans-membrane pressure measured at the second point; and

adjusting the relaxation phase duration or the flux as a function of the difference in trans-membrane pressure and the measured liquid level in the membrane tank.

38. The method of claim 37 including:

selecting a pair of set point values such that one set point value is larger than the other set point value;

in the event that the difference in trans-membrane pressure is between the pair of selected set point values, adjusting neither the relaxation phase duration nor the flux in response to the difference;

in the event that the difference in trans-membrane is less than the smaller of the selected set point values, decreasing the relaxation phase duration if the duration is not at a minimum allowable relaxation phase duration value; and

in the event that the difference in trans-membrane pressure is greater than the larger of the selected set point values, increasing the relaxation phase duration if the duration is not at a maximum allowable relaxation phase duration value or decreasing the flux if the measured liquid level is not at a maximum allowable liquid level value.

39. The method of claim 34 including:

in the event the measured liquid level in the membrane tank is not at a minimum allowable liquid level value, adjusting neither then permeation phase duration nor the flux in response to the measured liquid level;

in the event the measured liquid level in the membrane tank is at the minimum allowable liquid level value, decreasing the permeation phase duration if the duration is not at a minimum allowable permeation phase duration value, or decreasing the flux if the permeation phase duration is at a minimum allowable phase duration value; and

in the event the measured level in the membrane tank is above the maximum allowable liquid level value increasing the permeation phase duration if the permeation phase duration is not at a maximum allowable phase duration, or increasing the flux if the permeation phase duration is at the maximum allowable phase duration.

40. A method for controlling fouling of a membrane filter in a biological wastewater treatment process, comprising:

directing wastewater influent into one or more reactors and treating the wastewater;

directing the wastewater into and through one or more membrane tanks having one or more membrane filters therein;

filtering the wastewater by directing the wastewater through the membrane filters and producing a permeate;

cleaning the membrane filters with air scouring;

measuring a liquid level in a membrane tank;

executing one or more control cycles to control one or more control variables; and

in at least one control cycle, adjusting one control variable selected from the group including scouring air flow rate, flux, permeation phase duration, and relaxation phase duration as a function of the measured liquid level.

41. A method for controlling fouling of a membrane filter in a biological wastewater treatment process, comprising:

directing wastewater influent into one or more reactors and treating the wastewater;

directing the wastewater into and through one or more membrane tanks having one or more membrane filters therein;

filtering the wastewater by directing the wastewater through the membrane filters and producing a permeate;

cleaning the membrane filters with air scouring;

measuring a first change in trans-membrane pressure during a permeation phase, measuring a second change in trans-membrane pressure from the start of a first permeation phase to the start of a second permeation phase, and measuring liquid level in the membrane tank;

executing a hierarchy of control cycles to control one or more control variables;

in a first control cycle, adjusting a control variable selected from the group including scouring air flow rate and flux as a function of the measured first change in trans-membrane pressure and of the measured liquid level;

in a second control cycle, adjusting a control variable selected from the group including relaxation phase duration and flux as a function of the second measured change in trans-membrane pressure and of measured the liquid level; and

in a third control cycle, adjusting a control variable selected from the group including permeation phase duration and flux as a function of the measured liquid level.

42. A method for controlling fouling of a membrane filter in a biological wastewater treatment process, comprising:

directing wastewater influent into one or more reactors and treating the wastewater;

directing the wastewater into and through one or more membrane tanks having one or more membrane filters therein;

filtering the wastewater by directing the wastewater through the membrane filters and producing a permeate;

cleaning the membrane filters with air scouring;

executing a series of filtration cycles, each filtration cycle including a permeation phase and a relaxation phase wherein a membrane filter undergoes permeation during the permeation phase followed by relaxation during the relaxation phase;

measuring a first trans-membrane pressure at a first point in the permeation phase of a first filtration cycle;

measuring a second trans-membrane pressure at a second point in the permeation phase of a second filtration cycle;

measuring a third trans-membrane pressure at a third point in the permeation phase of the second filtration cycle;

measuring a liquid level in a membrane tank;

executing control logic that includes a hierarchy of control levels to optionally adjust scouring air flow rate, flux, permeation phase duration, and relaxation phase duration for a third filtration cycle;

in a first control level, optionally adjusting each of scouring air flow rate and flux as a function of the first measured trans-membrane pressure, the second measured trans-membrane pressure, and the measured liquid level in the membrane tank;

in a second control level, optionally adjusting each of relaxation phase duration and flux as a function of the second measured trans-membrane pressure, the third measured trans-membrane pressure, and the measured liquid level in the membrane tank; and

in a third control level, optionally adjusting each of flux and permeation phase duration as a function of the measured liquid level in the membrane tank.