Membrane filter element with multiple fiber types

Patent metadata

Field	Value
Publication number	US-9630141-B2
Application number	US-70610510-A
Country	US
Kind code	B2
Filing date	Feb 16, 2010
Priority date	Feb 20, 2009
Publication date	Apr 25, 2017
Grant date	Apr 25, 2017

Abstract

A natural gas stream is passed through a single membrane element that is fabricated with two or more distinct types of membrane fibers. The membrane fibers have different characteristics in order to reduce the number of membrane elements required for gas separation and to improve gas separation performance due to changing gas composition because of permeation as the gas travels through the membrane element.

First claim

What is claimed is:

1. A membrane element for treating a natural gas stream having an amount of acid gas content, the membrane element comprising:
a perforated non-permeate pipe having a central longitudinal axis; and
a first cylindrical-shaped zone having a height spanning the membrane element top-to-bottom and a first bundle depth arranged coaxial to the central longitudinal axis of the perforated non-permeate pipe, the first cylindrical-shaped zone defined by a plurality of first hollow fibers, the plurality of first hollow fibers fabricated to provide, for a first composition and volume of the natural gas stream, a selected first acid gas selectivity and permeability performance throughout the first cylindrical-shaped zone and arranged so a first acid-gas permeate exits the top and the bottom of the membrane element;
a second cylindrical-shaped zone having a height spanning the membrane element top-to-bottom and a second bundle depth arranged coaxial to the central longitudinal axis of the perforated non-permeate pipe, the second cylindrical-shaped zone defined by a plurality of second hollow fibers, the plurality of second hollow fibers fabricated to provide, for a second, different composition and volume of the natural gas stream, a selected second, different acid-gas selectivity and permeability performance throughout the second cylindrical-shaped zone and arranged so a second acid-gas permeate having a different composition than the first acid-gas permeate exits the top and the bottom of the membrane element and mixes, respectively, with the first acid-gas permeate that exited the first cylindrical-shaped zone at the top and the bottom of the membrane;
said selected first and second, different selectivity and permeability performances selected to provide the natural gas stream in a single stage of processing having a reduced amount of the acid-gas content, the second cylindrical-shaped zone surrounding the perforated non-permeate pipe, the first cylindrical-shaped zone surrounding the second cylindrical-shaped zone.

2. A membrane element according to claim 1 wherein the first and second hollow fibers are fabricated to provide, relative to one another, a different target CO 2 selectivity and permeability performance.

3. A membrane element according to claim 1 wherein the plurality of first and second hollow fibers are fabricated to provide, relative to one another, at least one of a different target water dew pointing and a different target hydrocarbon dew pointing performance.

4. A membrane element according to claim 1 wherein the plurality of first and second hollow fibers are fabricated to provide, relative to one another, a different target H 2 S selectivity and permeability performance.

5. A membrane element according to claim 1 wherein the second cylindrical-shaped zone represents one portion of a total bundle depth of the membrane element and the first cylindrical-shaped zone represents the remaining portion of the total bundle depth.

6. A membrane element for treating a natural gas stream having an amount of acid gas content, the membrane element being a divided membrane element comprising:
a first circumferential zone spanning a total height of the membrane element and defined by a plurality of first hollow fibers fabricated to provide, for a first composition and volume of the natural gas stream, a selected first acid-gas selectivity and permeability and arranged so a first acid-gas permeate exits from the top and the bottom of the membrane element; and
a second circumferential zone spanning a total height of the membrane element and defined by a plurality of second hollow fibers fabricated to provide, for a second, different composition and volume of the natural gas stream, a selected second, different acid-gas selectivity and permeability and arranged so a second acid-gas permeate exits from the top and the bottom of the membrane element;
the second circumferential zone surrounding a perforated non-permeate pipe, the first circumferential zone surrounding the second circumferential zone.

7. A membrane element according to claim 6 wherein the plurality of first and second hollow fibers are fabricated to provide, relative to one another, a different target CO 2 selectivity and permeability performance to a respective circumferential zone.

8. A membrane element according to claim 6 wherein the plurality of first and second hollow fibers are fabricated to provide, relative to one another, a different target H 2 S selectivity and permeability performance to a respective circumferential zone.

9. A membrane element according to claim 6 wherein the plurality of first and second hollow fibers are fabricated to provide, relative to one another, at least one of a different target water dew pointing and a different target hydrocarbon dew pointing performance to a respective circumferential zone.

10. A membrane element according to claim 6 wherein the second circumferential zone represents one portion of the bundle depth of the membrane element and the first circumferential zone represents the remaining portion of the bundle depth.

11. A membrane element according to claim 6 wherein the membrane element provides the natural gas stream in a single stage of processing having a reduced amount of the acid-gas content.

12. A membrane filter element for use in removing acid gas from a natural gas stream, the membrane filter element including a first and a second circumferential zone, the first circumferential zone spanning a predetermined bundle depth of the membrane filter element and surrounding the second circumferential zone, the second circumferential zone spanning a different predetermined bundle depth of the membrane filter element, hollow fibers in the first circumferential zone being hollow fibers selected to possess a first selectivity and permeability, hollow fibers in the second circumferential zone being hollow fibers selected to possess a second different selectivity and permeability, each circumferential zone spanning an entire height of the membrane filter element and arranged so an acid gas permeate exits a top and a bottom of the circumferential zone.

Assignees

• Peters Richard D
• Mahley Iii George E
• Morisato Atsushi
• Karim Fatimah Binti A
• Hassan Hatarmizi Bin
• Ali Zalina Binti
• Zakaria Wan Atikahsari Wan
• Isa Faudzi Mat
• Fadzillah Faizal Bin Mohamad
• Cameron Solutions Inc
• Petronas Carigali Sdn Bhd

Inventors

• Peters Richard D
• Mahley Iii George E
• Morisato Atsushi
• Karim Fatimah Binti A
• Hassan Hatarmizi Bin
• Ali Zalina Binti
• Zakaria Wan Atikahsari Wan
• Isa Faudzi Mat
• Fadzillah Faizal Bin Mohamad

Classifications

• Y02C10/10

  Cross-Sectional Technologies · mapped topic

• B01D2257/304

  Hydrogen sulfide · CPC title

• B01D2258/06

  Polluted air · CPC title

• B01D63/043

  with separate tube sheets · CPC title

• B01D63/04 Primary

  comprising multiple hollow fibre assemblies · CPC title