US5282969A
Expired / Lapsed
US
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High pressure feed membrane separation process
Assignee: Permea Inc
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Filing: 1993-04-29
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Granted: 1994-02-01
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Expires: 2013-04-29
Abstract
Abstract A process is set forth for the separation of one or more, more permeable components from one or more, less permeable components in a feed stream. The process suggests three membrane separation stages in series and is suitable for high pressure feed applications.
Inventors
- 👤 Jianguo Xu
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 09:55
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/58; B01D53/00; B01D53/22; B01D53/225; B01D53/226; B01D61/02; B01D61/025; B01D61/027
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
380 words
A process comprising: separating one or more, more permeable components from one or more, less permeable components in a feed stream comprising recovering either or both of the permeable and non-permeable components at predetermined purities while using an optimum combination of power and membrane area by: (a) introducing the feed stream into a first membrane separation module comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of the more permeable component(s) wherein the feed stream is more specifically introduced into the high pressure side of the first module; (b) withdrawing from the high pressure side of the first module a first non-permeate stream which is enriched in the less permeable component(s); (c) introducing the first non-permeate stream into a second membrane separation module comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of the more permeable component(s) wherein the first non-permeate stream is more specifically introduced into the high pressure side of the second module; (d) withdrawing from the high pressure side of the second membrane separation module a second non-permeate stream which is further enriched in the less permeable component(s); (e) withdrawing from the low pressure side of the second module a first permeate stream enriched in the more permeable component(s); (f) compressing the first permeate stream and introducing the compressed first permeate stream into a third membrane separation module comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of the more permeable component(s) wherein the compressed first permeate stream is more specifically introduced into the high pressure side of the third module; (g) withdrawing from the low pressure side of the first membrane separation module a second permeate stream which is further enriched in the more permeable component(s); (h) introducing the second permeate stream into the low pressure side of the third module; (i) withdrawing from the high pressure side of the third module a third non-permeate stream which is recycled to the feed stream; and finally (j) withdrawing from the low pressure side of the third module a third permeate stream which is yet further enriched in the more permeable component(s).
Claim 2
Dependent Claim
380 words
A process comprising: separating one or more, more permeable components from one or more, less permeable components in a feed stream comprising recovering either or both of the permeable and non-permeable components at predetermined purities while using an optimum combination of power and membrane area by: (a) introducing the feed stream into a first membrane separation module comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of the more permeable component(s) wherein the feed stream is more specifically introduced into the high pressure side of the first module; (b) withdrawing from the high pressure side of the first module a first non-permeate stream which is enriched in the less permeable component(s); (c) introducing the first non-permeate stream into a second membrane separation module comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of the more permeable component(s) wherein the first non-permeate stream is more specifically introduced into the high pressure side of the second module; (d) withdrawing from the high pressure side of the second membrane separation module a second non-permeate stream which is further enriched in the less permeable component(s); (e) withdrawing from the low pressure side of the second module a first permeate stream enriched in the more permeable component(s); (f) compressing the first permeate stream and introducing the compressed first permeate stream into a third membrane separation module comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of the more permeable component(s) wherein the compressed first permeate stream is more specifically introduced into the high pressure side of the third module; (g) withdrawing from the low pressure side of the first membrane separation module a second permeate stream which is further enriched in the more permeable component(s); (h) introducing the second permeate stream into the low pressure side of the third module; (i) withdrawing from the high pressure side of the third module a third non-permeate stream which is recycled to the feed stream; and finally (j) withdrawing from the low pressure side of the third module a third permeate stream which is yet further enriched in the more permeable component(s).
Claim 3
Dependent Claim
16 words
The process of claim 1 wherein steps (a) through (g) are operated as a continuous cycle.
Claim 4
Dependent Claim
39 words
The process of claim 1 wherein the selectivity towards the more permeable component(s) of the semi-permeable membrane in the first module is different than the selectivity towards the more permeable component(s) of the semi-permeable membrane in the second module.
Claim 5
Dependent Claim
40 words
The process of claim 1 wherein one or more of the modules is divided into a plurality of stages such that the permeate stream from one stage is compressed before being introduced as a sweep stream to the next stage.
References Cited (Backward Citations)
No citation records indexed.
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1997-01-31 | 1997-08-02 | 1998-02-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2001-01-31 | 2001-08-02 | 2002-02-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2005-01-31 | 2005-08-02 | 2006-02-01 | $7700.00 | Window Closed / Lapsed |