Multi-stage sweeping gas membrane distillation system and process

Patent metadata

Field	Value
Publication number	US-2025083105-A1
Application number	US-202418955422-A
Country	US
Kind code	A1
Filing date	Nov 21, 2024
Priority date	Aug 22, 2022
Publication date	Mar 13, 2025
Grant date	—

Abstract

A multi-stage sweeping gas membrane distillation (MS-SGMD) system and a method of use are provided. The MS-SGMD includes a plurality of modules, wherein each module includes a feed chamber fluidically coupled to a feed line and a carrier gas line, wherein the feed line introduces a liquid feed into the feed chamber from a liquid feed tank, and wherein the carrier gas line introduces a carrier gas into the feed chamber. Each module includes a sweeping gas chamber fluidically coupled to a sweeping gas line and a sweeping gas return line, wherein a sweeping gas is passed through the sweeping gas chamber. Each module further includes a membrane separating the feed chamber from the sweeping gas chamber, wherein the membrane allows transportation of vapor from the feed chamber to the sweeping gas chamber while blocking liquid from moving from the feed chamber to the sweeping gas chamber.

First claim

What is claimed is:

1 . A method for purifying a liquid using a multi-stage sweeping gas membrane distillation (MS-SGMD) system, comprising:
feeding a liquid to a feed chamber in each of a plurality of modules, wherein the liquid in the feed chamber is at a temperature of greater than about 50° C.; feeding a carrier gas through the liquid in the feed chamber of each of the plurality of modules to form a humidified carrier gas; feeding a sweeping gas through a sweeping gas chamber in each of the plurality of modules, wherein the sweeping gas chamber is separated from the feed chamber in each module by a membrane, and wherein the membrane allows vapor to pass across the membrane while blocking liquid flow across the membrane; and condensing, by a condenser a purified liquid from the vapor and the humidified carrier gas.

2 . The method of claim 1 , comprising heating the liquid before feeding the liquid to the feed chamber.

3 . The method of claim 1 , comprising heating the liquid in the feed chamber.

4 . The method of claim 1 , comprising feeding the liquid to a feed chamber of a first module of the plurality of modules, then feeding the liquid exiting the feed chamber of the first module of the plurality of modules to a second module of the plurality of modules.

5 . The method of claim 1 , comprising feeding the sweeping gas to the sweeping gas chamber of a first module of the plurality of modules, then feeding the sweeping gas from the first module to the sweeping gas chamber of a second module of the plurality of modules.

6 . The method of claim 1 , comprising feeding the carrier gas through a feed chamber of a first module of the plurality of modules, then feeding the carrier gas exiting the feed chamber of the first module of the plurality of modules to a feed chamber of a second module of the plurality of modules.

7 . The method of claim 1 , comprising coupling the plurality of modules in series to a feed line, wherein a liquid input to the feed chamber of a first module in the series is fluidically coupled to the feed line, a liquid outlet of the feed chamber of a last module in the series is fluidically coupled to a feed return line, and each intervening module between the first module and the last module is fluidically coupled by line from a liquid outlet on the feed chamber of the intervening module to a liquid inlet on the feed chamber of the next module.

8 . The method of claim 1 , comprising coupling the plurality of modules in series to a sweeping gas feed line, wherein the sweeping gas feed line is fluidically coupled to an inlet of the sweeping gas chamber on a first module in the series, a sweeping gas return line is fluidically coupled to an outlet from a last module in the series, and each intervening module between the first module and the last module is fluidically coupled by a line from an outlet of the sweeping gas chamber of the intervening module to an inlet of the sweeping gas chamber of the next module in the series.

9 . The method of claim 1 , comprising coupling the plurality of modules in series to a carrier gas line, wherein a carrier gas inlet on the feed chamber of a first module in the series is fluidically coupled to the carrier gas line, a carrier gas outlet of the feed chamber of a last module in the series is fluidically coupled to a carrier gas outlet line, and each intervening module between the first module and the last module is fluidically coupled by line from the carrier gas outlet of the feed chamber of the intervening module to a carrier gas inlet of the feed chamber of the next module.

Assignees

• Saudi Arabian Oil Co
• Univ King Fahd Pet & Minerals

Inventors

• Lawal Dahiru Umar
• Baroud Turki Nabieh
• Al Abdulgader Hasan

Classifications

• B01D61/366

  Apparatus therefor · CPC title

• B01D2311/13

  Use of sweep gas · CPC title

• C02F2301/08

  Multistage treatments, e.g. repetition of the same process step under different conditions · CPC title

• B01D2317/022

  Reject series · CPC title

• C02F1/447

  by membrane distillation (distillation and evaporation without the use of membranes C02F1/04) · CPC title