EP0147277A2
Expired / Lapsed
EP
⏱️ 0.0 years remaining
Process for separating a feed stream gas mixture using pressure swing adsorption
Assignee: Calgon Carbon Corp
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Filing: 1984-12-04
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Granted: —
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Expires: 2004-12-04
Abstract
Abstract A molecular sieve, pressure swing adsorption process employing two adsorbers for generating an enriched gas from a feed stream gas mixture is claimed, wherein each adsorber repeatedly passes through sequential steps comprising: (a) high pressure adsorption; (b) cocurrent partial depressurization by pressure equalization: (c) countercurrent venting to atmosphere: (d) regeneration using a product gas purge: (e) partial repressurization using product gas; (f) cocurrent partial repressurization by pressure equalization; and (g) feed gas repressurization to the adsorption pressure.
Inventors
- 👤 Toan P. Vo
Bibliographic Details
Application Number
—
Jurisdiction
EP
Data Source
google_patents
Last Synchronized
2026-10-24 21:24
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2253/00; B01D2253/10; B01D2253/116; B01D2253/25; B01D2256/00; B01D2256/10; B01D2256/16; B01D2256/24; B01D2256/245; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/40013; B01D2259/40015; B01D2259/40035; B01D2259/40037; B01D2259/40043; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40066; B01D2259/40067; B01D2259/402; B01D2259/403; B01D2259/404; B01D53/0473; Y; Y02; Y02C; Y02C20/00; Y02C20/20
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
281 words
A molecular sieve, pressure swing adsorption process employing two adsorbers for generating enriched gas from a feed stream gas mixture, wherein a first of said two adsorbers repeatedly passes through sequential steps comprising: (a) cocurrently passing said feed stream gas mixture through said first of two adsorbers at an adsorption pressure greater than atmospheric pressure, thereby producing an enriched product gas; (b) cocurrently partially depressurizing said first adsorber by venting it to the second of said two adsorbers until the pressures of said first and second adsorbers are equalized; thereby simultaneously partially repressurizing said second adsorber; (c) countercurrently depressurizing said first adsorber to atmosphere, thereby reducing the pressure of said first adsorber to atmospheric pressure; (d) regenerating said first adsorber by purging said first adsorber with enriched product gas, thereby causing adsorbate in the pores of said molecular sieve adsorber to be desorbed; (e) partially repressurizing said first adsorber by adding enriched product gas to said first adsorber; (f) cocurrently partially repressurizing said first adsorber by cocurrently venting said second adsorber to said first adsorber until the pressures of said first and second adsorbers are equalized, thereby simultaneously partially depressurizing said second adsorber; and (g) repressurizing said first adsorber to said adsorption pressure using said feed stream gas mixture; and wherein said second of said two adsorbers repeatedly passes through Steps(a) through (g) above, treating the second adsorber as the first adsorber and vice versa, and wherein the operating sequences for said first adsorber and said second adsorber align so that Step (a) for said first adsorber occurs simultaneously with Step (g) for said-second adsorber and Step (a) for said second adsorber occurs simultaneous with Step (g) for said first adsorber.
Claim 2
Dependent Claim
281 words
A molecular sieve, pressure swing adsorption process employing two adsorbers for generating enriched gas from a feed stream gas mixture, wherein a first of said two adsorbers repeatedly passes through sequential steps comprising: (a) cocurrently passing said feed stream gas mixture through said first of two adsorbers at an adsorption pressure greater than atmospheric pressure, thereby producing an enriched product gas; (b) cocurrently partially depressurizing said first adsorber by venting it to the second of said two adsorbers until the pressures of said first and second adsorbers are equalized; thereby simultaneously partially repressurizing said second adsorber; (c) countercurrently depressurizing said first adsorber to atmosphere, thereby reducing the pressure of said first adsorber to atmospheric pressure; (d) regenerating said first adsorber by purging said first adsorber with enriched product gas, thereby causing adsorbate in the pores of said molecular sieve adsorber to be desorbed; (e) partially repressurizing said first adsorber by adding enriched product gas to said first adsorber; (f) cocurrently partially repressurizing said first adsorber by cocurrently venting said second adsorber to said first adsorber until the pressures of said first and second adsorbers are equalized, thereby simultaneously partially depressurizing said second adsorber; and (g) repressurizing said first adsorber to said adsorption pressure using said feed stream gas mixture; and wherein said second of said two adsorbers repeatedly passes through Steps(a) through (g) above, treating the second adsorber as the first adsorber and vice versa, and wherein the operating sequences for said first adsorber and said second adsorber align so that Step (a) for said first adsorber occurs simultaneously with Step (g) for said-second adsorber and Step (a) for said second adsorber occurs simultaneous with Step (g) for said first adsorber.
Claim 3
Dependent Claim
36 words
The process of Claim 1, wherein said molecular sieve is a carbon molecular sieve, wherein said feed stream gas mixture is air and wherein said enriched gas is at least 90 percent inert gas, by volume.
Claim 4
Dependent Claim
15 words
The process of Claim 2, wherein said adsorption pressure is from 1.0 to 30.0 bars.
Claim 5
Dependent Claim
15 words
The process of Claim 3, wherein said adsorption pressure is from 4.0 to 9.0 bars.
Claim 6
Dependent Claim
18 words
The process of Claim 2, wherein said enriched gas is at least 95 percent inert gas, by volume.
Claim 7
Dependent Claim
18 words
The process of Claim 5, wherein said enriched gas is at least 97 percent inert gas, by volume.
Claim 8
Dependent Claim
18 words
The process of Claim 6, wherein said enriched gas is at least 99 percent inert gas, by volume.
Claim 9
Dependent Claim
42 words
The process of Claim 1, wherein said molecular sieve is a carbon molecular sieve, and wherein said feed stream gas mixture comprises methane and carbon dioxide; or methane and air; or hydrogen, carbon dioxide and hydrocarbon gases; or hydrogen and hydrocarbon gases.
Claim 10
Dependent Claim
133 words
A molecular sieve pressure swing adsorption process employing three or four adsorbers for generating enriched gas from a feed stream gas mixture, wherein each adsorber repeatedly passes through sequential steps comprising: (a) cocurrent adsorption, thereby producing an enriched product gas; (b) cocurrent partial depressurization by venting to another adsorber until the pressure of the other adsorber is equal to the pressure of the adsorber being depressurized; (c) countercurrent vent to atmosphere, thereby reducing the pressure to atmospheric pressure; (d) regeneration by purging with enriched product gas; (e) partial repressurization by addition of enriched gas; (f) cocurrent partial repressurization by venting from another adsorber until the pressure of the other adsorber is equal to the pressure of the adsorber being repressurized; and (g) repressurization to the adsorption pressure using the feed stream gas mixture.
Claim 11
Dependent Claim
133 words
A molecular sieve pressure swing adsorption process employing three or four adsorbers for generating enriched gas from a feed stream gas mixture, wherein each adsorber repeatedly passes through sequential steps comprising: (a) cocurrent adsorption, thereby producing an enriched product gas; (b) cocurrent partial depressurization by venting to another adsorber until the pressure of the other adsorber is equal to the pressure of the adsorber being depressurized; (c) countercurrent vent to atmosphere, thereby reducing the pressure to atmospheric pressure; (d) regeneration by purging with enriched product gas; (e) partial repressurization by addition of enriched gas; (f) cocurrent partial repressurization by venting from another adsorber until the pressure of the other adsorber is equal to the pressure of the adsorber being repressurized; and (g) repressurization to the adsorption pressure using the feed stream gas mixture.
References Cited (Backward Citations)
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