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Adsorption-desorption separation process with integrated light and heavy desorbents
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1981-04-22
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Granted: 1983-04-26
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Expires: 2001-04-22
Abstract
Abstract An improved adsorption-desorption separation process is disclosed for separating close boiling fractions or isomers of a hydrocarbon feedstream containing mixed hydrocarbon fractions or isomers.
Inventors
- 👤 Roger Wylie
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 14:41
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/11; Y; Y10; Y10S; Y10S203/00; Y10S203/20
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
172 words
In an adsorption-desorption process for separating close boiling materials or isomers in which a liquid desorbent is used to produce an extract of desired materials in said desorbent and also a raffinate of byproduct materials in said desorbent, the improvement which comprises: carrying out an adsorption-desorption step in a first unit with a desorbent lower boiling than the feedstream to be separated to obtain a light extract and a light raffinate; carrying out an adsorption-desorption step in a second unit with a desorbent higher boiling than said feedstream to obtain a heavy extract and a heavy raffinate; passing light raffinate and heavy raffinate into a fractionating column and separating the same by fractionation into light desorbent, heavy desorbent and byproduct raffinate materials; passing light extract and heavy extract into a second fractionating column and separating the same by fractionation into light desorbent, heavy desorbent and product extracted materials; and recycling light desorbent streams from both fractionators to said first unit and recycling heavy desorbent streams from both fractionators to said second unit.
Claim 2
Dependent Claim
172 words
In an adsorption-desorption process for separating close boiling materials or isomers in which a liquid desorbent is used to produce an extract of desired materials in said desorbent and also a raffinate of byproduct materials in said desorbent, the improvement which comprises: carrying out an adsorption-desorption step in a first unit with a desorbent lower boiling than the feedstream to be separated to obtain a light extract and a light raffinate; carrying out an adsorption-desorption step in a second unit with a desorbent higher boiling than said feedstream to obtain a heavy extract and a heavy raffinate; passing light raffinate and heavy raffinate into a fractionating column and separating the same by fractionation into light desorbent, heavy desorbent and byproduct raffinate materials; passing light extract and heavy extract into a second fractionating column and separating the same by fractionation into light desorbent, heavy desorbent and product extracted materials; and recycling light desorbent streams from both fractionators to said first unit and recycling heavy desorbent streams from both fractionators to said second unit.
Claim 3
Dependent Claim
13 words
The process of claim 1 wherein the close boiling materials are aromatic compounds.
Claim 4
Dependent Claim
13 words
The process of claim 1 wherein the isomers are meta-, ortho-, and para-xylene.
Claim 5
Dependent Claim
18 words
The process of claim 1 wherein the lower boiling desorbent is a hydrocarbon compound having seven carbon atoms.
Claim 6
Dependent Claim
17 words
The process of claim 1 wherein the higher boiling desorbent is a hydrocarbon containing ten carbon atoms.
References Cited (Backward Citations)
DE2856051A1
Cited
US4246073A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-04-25 | 1986-10-25 | 1987-04-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-04-25 | 1990-10-25 | 1991-04-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-04-25 | 1994-10-25 | 1995-04-26 | $7700.00 | Window Closed / Lapsed |