Multi-stage membrane systems with polymeric and microporous zeolitic inorganic membranes for gas separations

US11033856B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11033856-B2
Application numberUS-201816009126-A
CountryUS
Kind codeB2
Filing dateJun 14, 2018
Priority dateJun 14, 2018
Publication dateJun 15, 2021
Grant dateJun 15, 2021

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

A multistage membrane system and a process for treating a gas stream is provided in which the multistage membrane system comprises at least two membrane units wherein a first stage membrane unit comprises a polymeric membrane and a second membrane unit comprises a microporous zeolitic inorganic membrane or a combination of a microporous zeolitic inorganic membrane and a polymeric membrane.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for treating a gas stream comprising: sending said gas stream through a two-stage membrane system having two membrane units wherein a first membrane unit comprises a polymeric membrane and a second membrane unit comprises a micoporous zeolitic inorganic membrane or a combination of a micoporous zeolitic inorganic membrane and a polymeric membrane, wherein said gas stream first contacts said first membrane unit to separate said gas stream into a first permeate stream and a first residue stream; sending said first residue stream to a product stream; compressing the first permeate stream in an interstage compressor to pressurize the first permeate stream to about 100 psig; sending said compressed first permeate stream to said second membrane unit to be separated into a second permeate stream and a second residue stream; and compressing the second residue stream in a second stage residue compressor to pressurize said second residue stream. 2. The process of claim 1 wherein said second permeate stream is a waste stream. 3. The process of claim 1 wherein said second residue stream is recycled to said gas stream post compression in said second stage residue compressor. 4. The process of claim 1 wherein said compressed second residue stream is sent to said product stream. 5. The process of claim 1 wherein the polymeric membrane is selected from the group consisting of polysulfones, polyethersulfones, sulfonated polysulfones, sulfonated polyether sulfones, polyetherimides, cellulosic polymers, polyimides, polyamide/imides, polyketones, polyether ketones, poly(arylene oxides), poly(benzobenzimidazole), polyhydrazides, polyoxadiazoles, polybenzoxazoles, polytriazoles, poly(benzimidazole), polycarbodiimides, polyphosphazines, microporous polymers, and mixtures thereof. 6. The process of claim 1 wherein the micoporous zeolitic inorganic membrane comprises a selective layer of a microporous aluminosilicate, a silicate zeolite, a silicoaluminophosphate (SAPO), a metalloaluminophosphate (MeAPO), a metallosilicoaluminophosphate (MeAPSO), a metal-organic framework (MOF), a zeolitic imidazolate framework (ZIF), or a covalent organic framework (COF). 7. The process of claim 1 wherein both the first membrane unit and the second membrane unit comprise the same polymeric membrane or a different polymeric membrane. 8. The process of claim 1 wherein the micoporous zeolitic inorganic membrane comprises a structure selected from the group consisting of AlPO-14, AlPO-18, AlPO-34, SAPO-34, SSZ-13, DD3R, ITQ-12, CDS-1, UZM-25, MOF-5, ZIF-8, ZIF-67, and mixtures thereof. 9. The process of claim 1 wherein said gas stream is natural gas. 10. The process of claim 1 wherein said gas stream is a pair of gases selected from the group consisting of CO 2 /CH 4 , H 2 S/CH 4 , N 2 /CH 4 , H 2 /CH 4 , and He/CH 4 . 11. The process of claim 1 wherein the process is applied in the separation application selected from the group consisting of: (i) H 2 from N 2 , CH 4 , and Ar in ammonia purge gas streams, (ii) H 2 recovery in refineries, (iii) CO 2 removal and olefin recovery from ethylene oxide or ethylene glycol plants, (iv) olefin/paraffin separations, (v) liquid natural gas separations, and (vi) C 2 + hydrocarbon recovery. 12. The process claim 1 , further comprising at least one of: sensing at least one parameter of the process and generating a signal from the sensing; sensing at least one parameter of the process and generating data from the sensing; generating and transmitting a signal; and generating and transmitting data.

Assignees

Inventors

Classifications

  • Polyetherketone, polyetheretherketone, or polyaryletherketone · CPC title

  • Polyether-imides · CPC title

  • Polyphenylene oxide, phenyl ether polymers or polyphenylethers · CPC title

  • Zeolites · CPC title

  • Use of membranes of different materials or properties within one module · CPC title

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What does patent US11033856B2 cover?
A multistage membrane system and a process for treating a gas stream is provided in which the multistage membrane system comprises at least two membrane units wherein a first stage membrane unit comprises a polymeric membrane and a second membrane unit comprises a microporous zeolitic inorganic membrane or a combination of a microporous zeolitic inorganic membrane and a polymeric membrane.
Who is the assignee on this patent?
Uop Llc
What technology area does this patent fall under?
Primary CPC classification B01D53/228. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jun 15 2021 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 2 related publications on this page (citations in our corpus or others sharing the same primary CPC).