Patent US5240472A successfully refreshed from Google Patents.
US5240472A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Moisture removal from a wet gas
Assignee: Air Products and Chemicals Inc
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Filing: 1992-05-29
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Granted: 1993-08-31
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Expires: 2012-05-29
Abstract
Abstract This invention pertains to an improved process for the removal of moisture from a moisture laden gas stream such as air utilizing a membrane dryer unit. The membrane dryer unit is equipped such that it incorporates a selective surface flow adsorbent membrane consisting essentially of an inorganic membrane material selected from the group consisting of alumina and silica gel membranes wherein the membrane has a thickness of approximately 0.5 to 50 microns with a mean pore size of less than about 15 A and preferably within about 4 to 10 A. In the cryogenic separation of air, an air stream contaminated with moisture and carbon dioxide is passed through the membrane dryer unit in countercurrent flow to a dry purge gas, wherein the water is selectively removed from the air stream. The partially dried air stream then is conveyed to an adsorption system operated under thermal swing or pressure swing conditions wherein the residual water and carbon dioxide are removed.
Inventors
- 👤 Shivaji Sircar
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 19:04
CPC Classifications
B; B01; B01D; B01D67/00; B01D67/0039; B01D67/0048; B01D53/00; B01D53/22; B01D53/229; B01D53/26; B01D53/268; B01D69/00; B01D69/02; B01D71/00; B01D71/02; B01D2323/00; B01D2323/08; B01D2323/081; Y; Y02; Y02C; Y02C20/00; Y02C20/40
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
125 words
An improved process for the production of a dry gas stream from a moisture laden stream in which a membrane system is used to selectively remove moisture from the gas stream, the improvement comprising: passing a gas stream containing moisture to a membrane dryer unit capable of selectively permeating water present therein, said membrane dryer unit incorporating a selective surface flow adsorbent membrane consisting essentially of an organic material selected from the group consisting of γ-alumina and silica gel, said selective surface flow adsorbent membrane having pores which are predominantly less than 15 Å in diameter; recovering a dry non-permeate gas from the membrane dryer unit; and removing water vapor as a permeate gas from a low pressure permeate side of the membrane dryer unit.
Claim 2
Dependent Claim
125 words
An improved process for the production of a dry gas stream from a moisture laden stream in which a membrane system is used to selectively remove moisture from the gas stream, the improvement comprising: passing a gas stream containing moisture to a membrane dryer unit capable of selectively permeating water present therein, said membrane dryer unit incorporating a selective surface flow adsorbent membrane consisting essentially of an organic material selected from the group consisting of γ-alumina and silica gel, said selective surface flow adsorbent membrane having pores which are predominantly less than 15 Å in diameter; recovering a dry non-permeate gas from the membrane dryer unit; and removing water vapor as a permeate gas from a low pressure permeate side of the membrane dryer unit.
Claim 3
Dependent Claim
24 words
The process of claim 1, wherein a dry purge gas is passed in countercurrent relationship to the moisture laden gas to the membrane unit.
Claim 4
Dependent Claim
18 words
The process of claim 1, wherein the membrane has a thickness of from about 1 to 50 microns.
Claim 5
Dependent Claim
24 words
The process of claim 3 wherein the average pore size within the selective surface flow adsorbent membrane is from about 4 to 10 A.
Claim 6
Dependent Claim
168 words
An improved process for the production of a dry, high purity nitrogen and/or oxygen from air comprising: passing a moisture laden feed air to a membrane dryer system capable of selectively permeating water therefrom and forming a partially dried feed air; said membrane dryer system incorporating a selective surface flow adsorbent membrane consisting essentially of an inorganic material selected from the group consisting of γ-alumina and silica gel, said selective surface flow adsorbent membrane having pores which are predominantly less than 15 Å in diameter; passing the partially dried feed air to a thermal swing adsorption system capable of selectively adsorbing residual water and carbon dioxide from the dry feed air; passing the dry, prepurified feed air from said thermal swing adsorption system to a cryogenic air separation system for the cryogenic rectification of air, and the production of dry, high purity nitrogen and dry oxygen containing gas; and recovering the dry, high purity nitrogen and high purity oxygen gas from said from said cryogenic air separation system.
Claim 7
Dependent Claim
168 words
An improved process for the production of a dry, high purity nitrogen and/or oxygen from air comprising: passing a moisture laden feed air to a membrane dryer system capable of selectively permeating water therefrom and forming a partially dried feed air; said membrane dryer system incorporating a selective surface flow adsorbent membrane consisting essentially of an inorganic material selected from the group consisting of γ-alumina and silica gel, said selective surface flow adsorbent membrane having pores which are predominantly less than 15 Å in diameter; passing the partially dried feed air to a thermal swing adsorption system capable of selectively adsorbing residual water and carbon dioxide from the dry feed air; passing the dry, prepurified feed air from said thermal swing adsorption system to a cryogenic air separation system for the cryogenic rectification of air, and the production of dry, high purity nitrogen and dry oxygen containing gas; and recovering the dry, high purity nitrogen and high purity oxygen gas from said from said cryogenic air separation system.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1996-08-30 | 1997-03-01 | 1997-08-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2000-08-30 | 2001-03-01 | 2001-08-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2004-08-30 | 2005-03-01 | 2005-08-31 | $7700.00 | Window Closed / Lapsed |