Multistage membrane separation and purification process and apparatus for separating high purity methane gas
US-10047310-B2 · Aug 14, 2018 · US
US11033856B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11033856-B2 |
| Application number | US-201816009126-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 14, 2018 |
| Priority date | Jun 14, 2018 |
| Publication date | Jun 15, 2021 |
| Grant date | Jun 15, 2021 |
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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.
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.
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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