US4406674A
Expired / Lapsed
US
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Method for separating gas mixtures by means of a pressure changing technique
Assignee: Bergwerksverband GmbH
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Filing: 1982-06-01
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Granted: 1983-09-27
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Expires: 2002-06-01
Abstract
Abstract Method for separating gas mixtures resulting from direct flow loading of adsorption reactors by means of a pressure change technique in a two stage adsorption reactor consisting of a prefilter and a separating filter, whereby strongly adsorbable impurities from the gas mixture are adsorbed in the prefilter and the remainder of the undesirable gas components are adsorbed in the separating reactor. Thereby, product gas flows off at the end of the separating reactor shortly before the passage therethrough of a non-desirable gas component. Thereafter, the prefilter and the separating reactor are disconnected and the prefilter is partially relieved by a gas counter flow and the separating reactor is partially relieved by direct gas flow. After reconnection of prefilter and separating reactor the unit is further released in the counter current, subsequently rinsed and is again brought to charge pressure in the direct or counter current. The prefilter can be prerinsed before the gas like reconnection with the separating reactor. During rinsing and pressure build up one can use relieve gas. Preferably, four coupled two stage adsorption reactors are used as well as an additional prefilter.
Inventors
- 👤 Karl Knoblauch
- 👤 Ekkehard Richter
- 👤 Klaus Giessler
- 👤 Werner Korbacher
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 23:23
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D53/047; B01D2253/00; B01D2253/10; B01D2253/116; B01D2253/25; B01D2253/30; B01D2253/302; B01D2253/304; B01D2253/306; B01D2253/34; B01D2256/00; B01D2256/16; B01D2257/00; B01D2257/10; B01D2257/102; B01D2257/50; B01D2257/502; B01D2257/504; B01D2257/70; B01D2257/702; B01D2257/7022; B01D2257/7025; B01D2259/00; B01D2259/40; B01D2259/40011; B01D2259/40028; B01D2259/4003; B01D2259/40032; B01D2259/40043; B01D2259/40045; B01D2259/4005; B01D2259/40052; B01D2259/40058; B01D2259/40064; B01D2259/404; Y; Y02; Y02C; Y02C20/00; Y02C20/20; Y02C20/40
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
182 words
A method for separating gas mixtures by means of pressure changing techniques in a two stage absorption reactor consisting of a prefilter and a separation reactor by direct flow loading of the adsorption reactor at increased pressure wherein at least higher hydrocarbon aromatics and naphthenes present in the mixture are adsorbed in the prefilter and the remaining undesired gas components are adsorbed in the separation reactor whereby the product gas is discharged at the end of the separation filter which comprises (a) completing the adsorption process before the prefilter and separation reactor are disconnected; (b) partially reducing the gas pressures in the prefilter and separation reactor using direct and counter current gas flows respectively before reconnecting the prefilter and separation reactor; (c) after said reconnection when necessary again reducing the gas pressures in said prefilter and separation reactor employing counter flow of gas; (d) thereafter rinsing the prefilter and separation reactor employing counter flow of rinsing gas; and (e) thereafter increasing the gas pressures in the rinsed prefilter and separation reactor to reach load pressures using direct and counter gas flow respectively.
Claim 2
Independent Claim
182 words
A method for separating gas mixtures by means of pressure changing techniques in a two stage absorption reactor consisting of a prefilter and a separation reactor by direct flow loading of the adsorption reactor at increased pressure wherein at least higher hydrocarbon aromatics and naphthenes present in the mixture are adsorbed in the prefilter and the remaining undesired gas components are adsorbed in the separation reactor whereby the product gas is discharged at the end of the separation filter which comprises (a) completing the adsorption process before the prefilter and separation reactor are disconnected; (b) partially reducing the gas pressures in the prefilter and separation reactor using direct and counter current gas flows respectively before reconnecting the prefilter and separation reactor; (c) after said reconnection when necessary again reducing the gas pressures in said prefilter and separation reactor employing counter flow of gas; (d) thereafter rinsing the prefilter and separation reactor employing counter flow of rinsing gas; and (e) thereafter increasing the gas pressures in the rinsed prefilter and separation reactor to reach load pressures using direct and counter gas flow respectively.
Claim 3
Dependent Claim
40 words
The method of claim 1 wherein a portion of the rinsing gas is fed between the prefilter and the separation reactor and is employed in counter flow rinsing of the prefilter before the prefilter is reconnected to the separation reactor.
Claim 4
Dependent Claim
40 words
Method in accordance with claim 1 or 2 which comprises that at least one part of the flow of relief gas in the separating reactor is used for the counter current flow rinsing of the separating reactor and the prefilter.
Claim 5
Dependent Claim
45 words
Method in accordance with claim 1 or 2 characterized in that at least one part of the direct current relief gas in the separating reactor is used for at least a partial pressure buildup of the prefilter and the separating reactor in the counter flow.
Claim 6
Dependent Claim
35 words
Method in accordance with claim 1 or 2 characterized in that the product gas is used for at least a partial pressure build up of the prefilter and the separating reactor in the counter flow.
Claim 7
Dependent Claim
33 words
Method in accordance with claim 1 and 2, characterized by using initial gas mixture at least for the concluding pressure build up to change the pressure of the prefilter and the separating reactor.
Claim 8
Dependent Claim
34 words
Method in accordance with claim 1 or 2, characterized by the use of at least four two stage adsorption reactors with known connecting lines and valves for the coupling of the individual method steps.
Claim 9
Dependent Claim
66 words
Method in accordance with claim 1 or 2 wherein after the adsorption process in the prefilter and separation reactor is completed and the prefilter and reactor are disconnected about 1/50 and 1/2 of the total relief time is utilized in counter flow within the reactor and/or prefilter and that the relief gas or gases are used for a partial rinsing stage of the prefilter and/or reactor.
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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) | 1986-09-26 | 1987-03-28 | 1987-09-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-09-26 | 1991-03-28 | 1991-09-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-09-26 | 1995-03-28 | 1995-09-27 | $7700.00 | Window Closed / Lapsed |