IP Library Granted Patent US 11,298,661
Granted Patent B2
US 11,298,661 · App. 16/314,571 · Granted Apr 12, 2022

Cleaning method of a water-filtration system under operation

Inventors: Jérôme Anfray (Pau, FR); Pierre Pedenaud (Lescar, FR); Graeme Skivington (Glasgow, GB); Thomas Delaplace (Clichy, FR)
Assignees: TOTAL SA; VEOLIA WATER SOLUTIONS TECHNOLOGIES SUPPORT; SAIPEM S.A.
B01D65/02B01D61/04B01D61/16B01D65/08C02F1/441C02F1/442C02F1/444B01D2311/06B01D2311/08B01D2311/12B01D2311/24B01D2311/25B01D2315/06B01D2315/10B01D2321/16B01D2321/162B01D2321/164B01D2321/168B01D2321/205B01D2321/40
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Quick Facts
Patent No.
US 11,298,661
App. No.
16/314,571
Granted
Apr 12, 2022
Kind
B2
Abstract

The present invention is a filtration system and a method for cleaning a filtration system. The filtration system comprising a hydraulic circuit Cp recycling the permeate stream to the feed side of the membrane and/or a hydraulic circuit Cr recycling the retentate stream to the feed side of said membrane. The method injects an amount of a chemical product into the filtration system in the hydraulic circuit Cp or in the hydraulic circuit Cr or upstream of the cross-flow filtration membrane, setting the proportion of recycled permeate stream or recycled retentate stream collected in the hydraulic circuit Cp and/or Cr to enable the recycling of a significant amount of unreacted chemical product having passed through the cross-flow filtration membrane to the feed side of said cross-flow filtration membrane.

Claims (15)

1. A method for cleaning a filtration system under operation, said filtration system comprising:

a cross-flow filtration membrane having:

a feed side fed with a feed stream,

a permeate side wherein a permeate stream is recovered and

a retentate side wherein a retentate stream is recovered,

a hydraulic circuit Cp being provided with a valve connecting the permeate side of said cross-flow filtration membrane to the feed side of said cross-flow filtration membrane, said hydraulic circuit Cp allowing recycling of a proportion of the permeate stream to the feed side of said cross-flow filtration membrane,

said method comprising:

measuring a difference in pressure between the feed side and the permeate side of the membrane, ΔP membrane, and/or measuring a difference in pressure between the feed side and the retentate side of the membrane, ΔP longitudinal,

injecting an amount of a chemical product into the filtration system which is under operation directly in the hydraulic circuit Cp when at least one of ΔP membrane and ΔP longitudinal reaches a predetermined value which is 10% higher than ΔP longitudinal initial or ΔP membrane initial,

setting a proportion of permeate stream collected in the hydraulic circuit Cp that is recycled to the feed side of said cross-flow filtration membrane with the valve to enable recycling of a significant amount of unreacted chemical product passing through said cross-flow filtration membrane, the significant amount of unreacted chemical product meaning that said unreacted chemical product is present in the recycled permeate stream at a concentration of at least 70% of initial concentration of chemical product injected directly into the hydraulic circuit Cp.

2. The method according to claim 1 , wherein the cross-flow filtration membrane is a microfiltration membrane, an ultrafiltration membrane, a nanofiltration membrane or a reverse osmosis membrane.

3. The method according to claim 1 , wherein the cross-flow filtration membrane is a ceramic membrane or an organic membrane.

4. The method according to claim 1 , wherein the chemical product is a biocide, an acid, a base, a cleaning agent such as surfactant agent, a detergent, a complexation agent or a scale dissolver, or a mixture thereof.

5. The method according to claim 1 , wherein the proportion of permeate stream collected in the hydraulic circuit Cp that is recycled to the feed side of the filtration a membrane is at least 10% relative to the flow rate of permeate stream collected ire the hydraulic circuit Cp.

6. The method according to claim 1 , wherein the filtration system under operation is located under water.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE NAME OF THE ASSIGNEE PREVIOUSLY RECORDED AT REEL: 67096 FRAME: 87. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jun 26, 2024
From: TOTALENERGIES SE (PREVIOUSLY TOTAL SA THEN TOTAL SE)
To: TOTALENERGIES ONETECH
Reel/Frame 068051/0530 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 12, 2024
From: TOTALENERGIES SE (PREVIOUSLY TOTAL SA THEN TOTAL SE)
To: TOTALENERGIES ONETECH (PREVIOUSLY TOTALENERGIES ONE TECH)
Reel/Frame 067096/0087 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 16, 2019
From: ANFRAY, JÉRÔME; PEDENAUD, PIERRE; SKIVINGTON, GRAEME; DELAPLACE, THOMAS
To: TOTAL SA; VEOLIA WATER SOLUTIONS & TECHNOLOGIES SUPPORT; SAIPEM S.A.
Reel/Frame 048034/0698 →
Continuity (1)
Related Publication 20190168166A1 · Jun 6, 2019