IP Library Patent Application 12096279
Patent Application
App. No. 12/096,279

Reduced Backwash Volume Process

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Patent No.
US None
App. No.
12/096,279
Abstract

A method of backwashing a membrane filtration module, where the module includes one or more membranes located in a feed-containing vessel. The membranes having a permeable wall which is subjected to a filtration operation wherein feed liquid containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall. The method includes the steps of suspending the filtration operation; aerating the membrane surface with gas bubbles to dislodge fouling materials therefrom; recommencing the filtration operation while suspending the flow of feed liquid to the feed-containing vessel for a predetermined period; again suspending the filtration operation; performing a liquid backwash of the membrane wall to dislodge fouling materials therefrom; removing at least some of the liquid containing the dislodged contaminant matter from the feed-containing vessel; and then recommencing the filtration operation.

Claims (41)

1 : A method of backwashing a membrane filtration module, said module including one or more membranes located in a feed-containing vessel, the membranes having a permeable wall which is subjected to a filtration operation wherein feed liquid containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall, the method comprising the steps of:

a) suspending the filtration operation;

b) aerating the membrane surface with gas bubbles to dislodge fouling materials therefrom;

c) recommencing the filtration operation while suspending the flow of feed liquid to the feed-containing vessel for a predetermined period;

d) suspending the filtration operation;

e) performing a liquid backwash of the membrane wall to dislodge fouling materials therefrom;

f) removing at least some of the liquid containing the dislodged contaminant matter from the feed-containing vessel; and

g) recommencing the filtration operation.

2 : A method according to claim 1 wherein the predetermined period of step c) is determined by a required level of feed relative to said membranes.

3 : A method according to claim 1 wherein step c) includes controlling the flow of filtrate from the system such that transmembrane pressure across said membrane wall remains below a predetermined value during said predetermined period.

4 : A method according to claim 3 wherein the transmembrane pressure remain substantially constant.

5 : A method according to claim 1 wherein the removing step f) includes performing a sweep or drain-down of the feed-containing vessel.

6 : A method of backwashing a membrane filtration module, said module including one or more membranes located in a feed-containing vessel, the membranes having a permeable wall which is subjected to a filtration operation wherein feed liquid containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall, the method comprising the steps of:

a) suspending the filtration operation;

b) aerating the membrane surface with gas bubbles to dislodge fouling materials therefrom;

c) recommencing the filtration operation for a predetermined period;

d) suspending the filtration operation;

e) removing at least a portion of the liquid in the module or feed-containing vessel;

f) performing a liquid backwash of the membrane wall to dislodge fouling materials therefrom;

g) removing at least some of the liquid containing the dislodged contaminant matter from the feed-containing vessel; and

h) recommencing the filtration operation.

7 : A method according to claim 6 wherein the predetermined period of step c) is determined by a required level of feed liquid relative to said membranes.

8 : A method according to claim 6 wherein step c) includes controlling the flow of filtrate from the system such that transmembrane pressure across said membrane wall remains below a predetermined value during said predetermined period.

9 : A method according to claim 8 wherein the transmembrane pressure remain substantially constant.

10 : A method according to claim 6 wherein the removing step e) includes performing a sweep or drain-down of the feed-containing vessel.

11 : A method according to claim 6 wherein the removing step g) includes performing a sweep or drain-down of the feed-containing vessel.

12 : A method according to claim 6 wherein steps d) and e) are reversed in order.

13 : A method of backwashing a membrane filtration module, said module including one or more membranes located in a feed-containing vessel, the membranes having a permeable wall which is subjected to a filtration operation wherein feed liquid containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall, the method comprising the steps of:

a) suspending the provision of feed liquid to the feed containing vessel while continuing the filtration operation for a predetermined period;

b) suspending the filtration operation;

c) aerating the membrane surface with gas bubbles to dislodge fouling materials therefrom;

d) recommencing the filtration operation while continuing to suspend the flow of feed liquid to the feed-containing vessel for a further predetermined period;

e) suspending the filtration operation;

f) performing a liquid backwash of the membrane wall to dislodge fouling materials therefrom;

g) removing at least some of the liquid containing the dislodged contaminant matter from the feed-containing vessel; and

h) recommencing the filtration operation.

14 : A method according to claim 13 wherein the removing step g) includes performing a sweep or drain-down of the feed-containing vessel.

15 : A method according to claim 13 wherein the predetermined period of step a) is determined by a required level of feed liquid relative to said membranes.

16 : A method according to claim 13 wherein the further predetermined period of step d) is determined by a required level of feed liquid relative to said membranes.

17 : A method according to claim 13 , wherein step d) includes controlling the flow of filtrate from the system such that transmembrane pressure across said membrane wall remains below a predetermined value during said predetermined period.

18 : A method according to claim 17 wherein the transmembrane pressure remain substantially constant.

Assignments (9)
RELEASE OF SECURITY INTEREST (REEL/FRAME 032126/0430) Recorded Apr 6, 2021
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 055845/0311 →
RELEASE OF SECURITY INTEREST (REEL/FRAME 032126/0487) Recorded Apr 6, 2021
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 055845/0245 →
CHANGE OF NAME Recorded Feb 7, 2014
From: SIEMENS WATER TECHNOLOGIES LLC
To: EVOQUA WATER TECHNOLOGIES LLC
Reel/Frame 032173/0401 →
INTELLECTUAL PROPERTY SECURITY AGREEMENT (FIRST LIEN) Recorded Jan 24, 2014
From: WTG HOLDINGS III CORP.; WTG HOLDINGS II CORP.; SIEMENS TREATED WATER OUTSOURCING CORP.; SIEMENS WATER TECHNOLOGIES LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
Reel/Frame 032126/0487 →
INTELLECTUAL PROPERTY SECURITY AGREEMENT (SECOND LIEN) Recorded Jan 24, 2014
From: WTG HOLDINGS III CORP.; WTG HOLDINGS II CORP.; SIEMENS TREATED WATER OUTSOURCING CORP.; SIEMENS WATER TECHNOLOGIES LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
Reel/Frame 032126/0430 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 13, 2013
From: SIEMENS INDUSTRY, INC.
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 031396/0155 →
MERGER Recorded Apr 15, 2011
From: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
To: SIEMENS INDUSTRY, INC.
Reel/Frame 026138/0605 →
MERGER Recorded Apr 12, 2011
From: SIEMENS WATER TECHNOLOGIES CORP.
To: SIEMENS WATER TECHNOLOGIES HOLDING CORP.
Reel/Frame 026111/0973 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 11, 2008
From: JOHNSON, WARREN THOMAS
To: SIEMENS WATER TECHNOLOGIES CORP.
Reel/Frame 021080/0498 →