Hollow fiber membrane module and method of making and using same

Patent metadata

Field	Value
Publication number	US-2023191331-A1
Application number	US-202117556079-A
Country	US
Kind code	A1
Filing date	Dec 20, 2021
Priority date	Dec 20, 2021
Publication date	Jun 22, 2023
Grant date	—

Abstract

A membrane module includes a housing. The housing includes a housing, comprising: a first plurality of porous hollow fiber membranes, and a second plurality of porous hollow fiber membranes different from the first plurality of porous hollow fiber membranes. The first plurality of porous hollow fiber membranes has a first length, and the second plurality of porous hollow fiber membranes has a second length that is at least 1.1 times greater than the first length. The membrane module can be used in separation methods, such as membrane distillation methods.

First claim

What is claimed is:

1 . A system, comprising:
a first source configured to provide a first gas; a second source configured to provide a first liquid; a third source configured to provide a fluid; and a membrane module, comprising:
a housing, comprising:
a first inlet port;
a second inlet port different from the first inlet port;
a third inlet port different from the first and second inlet ports;
a first plurality of porous hollow fiber membranes; and
a second plurality of porous hollow fiber membranes different from the first plurality of porous hollow fiber membranes,

wherein:
each of the first plurality of porous hollow fiber membranes comprises an interior and an exterior;
each of the second plurality of porous hollow fiber membranes comprises an interior and an exterior; and
the first source is configured to provide the first gas to the interiors of the second plurality of porous hollow fiber membranes via the first inlet port; and
pores in the second plurality of porous hollow fiber membranes are configured so that, during use of the system, some of the first gas within the interiors of the first plurality of porous hollow fiber membranes flows out of the second plurality of porous hollow fiber membranes via the pores in the second plurality of porous hollow fiber membranes.

2 . The system of claim 1 , wherein the system is configured so that, after flowing out of the second plurality of porous hollow fiber membranes via the pores in the second plurality of porous hollow fiber membranes, the first gas is between the exteriors of the first plurality of porous hollow fiber membranes and the exteriors of the second plurality of porous hollow fiber membranes.

3 . The system of claim 2 , wherein:
the second source is configured to provide the first liquid to the exteriors of the first plurality of porous hollow fiber membranes and to the exteriors of the second plurality of porous hollow fiber membranes via the second inlet port; and the first gas between the exteriors of the first plurality of porous hollow fiber membranes and the exteriors of the second plurality of porous hollow fiber membranes is in the form of bubbles of the first gas which are disposed in the first liquid.

4 . The system of claim 3 , wherein the third source is configured to provide the fluid to the interiors of the first plurality of porous hollow fiber membranes via the third inlet.

5 . The system of claim 4 , wherein the fluid comprises a second liquid.

6 . The system of claim 5 , further comprising a heater configured to heat the first liquid so that, within the module, the first liquid is hotter than the second liquid.

7 . The system of claim 6 , wherein the first liquid comprises water, and the second comprises water, and the second liquid has a higher purity than the first liquid.

8 . The system of claim 4 , further comprising a pump configured to reduce a pressure of the fluid within the interiors of the first plurality of porous hollow fiber membranes.

9 . The system of claim 1 , wherein the system is configured to transfer water from the first liquid to the fluid with the module.

10 . The system of claim 1 , wherein the second plurality of porous hollow fiber membranes is longer than the first plurality of porous hollow fiber membranes.

11 . The system of claim 1 , wherein the system is configured so that:
the first gas has a flow path through the module; the first liquid has a flow path through the module that is different from the flow path of the first gas through module; and the fluid has a flow path through the module that is different from both the flow path of the first gas through module and the flow path of the first liquid through the module.

12 . A system, comprising:
a first source configured to provide a first gas; a second source configured to provide a first liquid; a third source configured to provide a fluid; and a membrane module, comprising:
a housing, comprising:
a first inlet port;
a second inlet port different from the first inlet port;
a third inlet port different from the first and second inlet ports;
a first plurality of porous hollow fiber membranes; and
a second plurality of porous hollow fiber membranes different from the first plurality of porous hollow fiber membranes,

wherein the system is configured so that:
the first gas has a flow path through the module;
the first liquid has a flow path through the module that is different from the flow path of the first gas through module; and
the fluid has a flow path through the module that is different from both the flow path of the first gas through module and the flow path of the first liquid through the module.

13 . The system of claim 12 , wherein:
each of the first plurality of porous hollow fiber membranes comprises an interior and an exterior; each of the second plurality of porous hollow fiber membranes comprises an interior and an exterior; the first source is configured to provide the first gas to the interiors of the second plurality of porous hollow fiber membranes via the first inlet port; the second source is configured to provide the first liquid to the interiors of the first plurality of porous hollow fiber membranes via the second inlet port; and the third source is configured to provide the fluid to the exteriors of the first plurality of porous hollow fiber membranes via the third inlet port.

14 . The system of claim 13 , wherein:
the housing further comprises a first outlet port and a second outlet port different from the first outlet port; and the system is configured so that during use of the system:
a first portion of the gas exits the module via the first outlet port; and
a second portion of the gas exits the module via the second outlet port.

15 . The system of claim 14 , wherein:
the housing further comprises a third outlet port different from the first and second outlet ports; and the system is configured so that during use of the system:
the first liquid exits the module via the second outlet; and
the fluid exits the module via the third outlet.

16 . The system of claim 12 , wherein the second plurality of porous hollow fiber membranes is longer than the first plurality of porous hollow fiber membranes.

17 . A method, comprising:
simultaneously introducing three different fluids into porous hollow fiber membranes of a membrane module so that each of the three fluids simultaneously contact some of the same porous hollow fiber membranes so that water is transferred across the simultaneously contacted porous hollow fiber membranes from a first fluid of the three fluids to a second fluid of the three fluids, wherein each of the three different fluids has a different flow path within the membrane module.

18 . The method of claim 17 , wherein:
the first fluid comprises a liquid; a third fluid of the three fluids comprises a gas; and the method forms bubbles of the gas in the first liquid so that the first liquid contains the bubbles of the gas when the three fluids simultaneously contact the same porous hollow fiber membranes.

19 . The method of claim 17 , wherein the first fluid comprises produced water or waste water.

20 . The method of claim 17 , wherein the method is a water desalination method.

Assignees

• Saudi Arabian Oil Co

Inventors

• Choi Seung-Hak
• Al Abdulgader Hasan

Classifications

• B01D2313/22

  Cooling or heating elements · CPC title

• C02F1/447 Primary

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

• B01D61/364

  Membrane distillation · CPC title

• B01D63/04 Primary

  comprising multiple hollow fibre assemblies · CPC title

• B01D2313/26

  Specific gas distributors or gas intakes · CPC title