Gas separation membrane module for reactive gas service

Patent metadata

Field	Value
Publication number	US-9962659-B2
Application number	US-201615195056-A
Country	US
Kind code	B2
Filing date	Jun 28, 2016
Priority date	Jun 30, 2015
Publication date	May 8, 2018
Grant date	May 8, 2018

Abstract

A gas separation membrane module includes a seal between a higher pressure gas and a lower pressure gas. The seal includes a compressible sealing member in between sealing surfaces. At least one of the sealing surfaces has corrosion-resistant cladding provided over either low alloy steel or high alloy steel. The cladding reduce the possibility of a seal failure due to corrosion of low alloy or high alloy steel exposed to acid gases or condensed moisture containing acid gases dissolved therein while at the same not requiring that all surfaces of the membrane module exposed to acid gases be provided with cladding.

First claim

What is claimed is:

1. An acid gas-service gas separation membrane module, comprising:
a hollow pressure vessel open at first and second ends made of carbon steel or a low alloy steel, the pressure vessel having a first end face at said first end and a second end face at said second end;
a first end cap made of carbon steel or a low alloy steel, sealing said first end of said pressure vessel at said first end face, said first end cap including a feed gas port formed therein;
a second end cap made of carbon steel or a low alloy steel, sealing said second end of said pressure vessel at said second end face, said second end cap including a residue port formed therein, said pressure vessel having a permeate port formed therein;
a plurality of gas separation membranes disposed within the pressure vessel arranged as a bundle, the plurality of membranes being encased in a solid polymer at end of the bundle in sealing fashion to provide first and second tubesheets, each of said membranes having a first side and a second side, each of said membranes being adapted and configured to separate an acid gas-containing feed gas fed to a first side thereof through permeation of gases through the membrane to a second side thereof so as to provide a lower pressure permeate gas on the second side and a higher pressure residue gas on the first side, the permeate gas being enriched in one or more gases compared to the residue gas;
a feed gas port tube made of a high alloy steel fluidly communicating between the feed gas port and one of the membranes' first sides and the membranes' second sides;
a residue port tube made of a high alloy steel fluidly communicating between the residue port and the other of the membranes' first sides and the membranes' second sides; and
at least two compressible sealing elements comprising first and second compressible sealing elements, wherein:
said first compressible sealing element is compressed between an inner surface of the pressure vessel adjacent the first tubesheet and an outer surface of the first tubesheet, said pressure vessel inner surface being provided with a corrosion-resistant cladding;
said second compressible sealing element being compressed between an inner surface of the pressure vessel adjacent the second tubesheet and an outer surface of the second tubesheet, the pressure vessel inner surface being provided with a corrosion-resistant cladding.

2. The membrane module of claim 1 , wherein:
said first compressible sealing element is a first O-ring installed in a groove formed in an inner surface of the pressure vessel; and
said second compressible sealing element is a second O-ring installed in a groove formed in an inner diameter of the pressure vessel.

3. The membrane module of claim 1 , wherein the membranes are configured as hollow fiber membranes or spiral-wrapped membranes.

4. The membrane module of claim 1 , wherein the membranes are made of a glassy polymer or a rubbery polymer.

5. The membrane module of claim 1 , wherein the pressure vessel is made of ASME SA333 Grade 6 seamless pipe.

6. The membrane module of claim 1 , wherein the low alloy steel of the first and second end caps is SA350 LF2 Class 2, or ASTM 105N.

7. The membrane module of claim 1 , wherein each of the compressible seals is an O-ring, gasket, or cup seal.

8. A method for the separation of an acid gas-containing feed gas, comprising the steps of:
providing the membrane module of claim 1 ;
feeding an acid gas-containing feed gas to the membrane module via the feed gas port;
withdrawing a permeate gas from the membrane module via the permeate port; and
withdrawing a residue gas from the membrane module via the residue port.

9. The method of claim 8 , wherein the acid gas is sour natural gas containing at least 5% vol H 2 S.

Assignees

• Air Liquide Advanced Tech Us Llc
• Air Liquide
• Saudi Arabian Oil Co
• Air Liquide

Inventors

• Kulkarni Sudhir S
• Beers Karl S
• Ballaguet Jean-Pierre R
• Vaidya Milind M
• Duval Sebastien A

Classifications

• B01D53/22

  by diffusion (manufacturing semi-permeable membranes B01D67/00; form, structure or properties of semi-permeable membranes B01D69/00; material for semi-permeable membranes B01D71/00) · CPC title

• B01D63/02 Primary

  Hollow fibre modules · CPC title

• B01D2256/24

  Hydrocarbons · CPC title

• B01D2313/20

  Specific housing · CPC title

• B01D63/12

  comprising multiple spiral-wound assemblies · CPC title