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Process for extractive distillation of plural hydrocarbon mixtures

Assignee: Zeon Corp
•
Filing: 1983-02-01
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Granted: 1983-12-20
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Expires: 2003-02-01
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Abstract

Abstract A process of extractive distillation for separating components easily soluble in a polar solvent from at least two hydrocarbon mixtures having different contents of the easily soluble components by extractive distillation using said polar solvent, which comprises feeding a hydrocarbon mixture containing a larger amount of the easily soluble components, as a gas, into the middle or lower portion of an extractive distillation column, feeding a hydrocarbon mixture containing a smaller amount of the easily soluble components, as a liquid, to the upper portion of the extractive distillation column, and subjecting them to extractive distillation.

Inventors

  • 👤 Shunichiro Ogura

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 06:06
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/04; C07C7/05; C07C7/08; B; B01; B01D; B01D3/00; B01D3/34; B01D3/40; Y; Y10; Y10S; Y10S203/00; Y10S203/09

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 95 words
A process of extractive distillation for separating components easily soluble in a polar solvent from at least two hydrocarbon mixtures having different contents of the easily soluble components by extractive distillation using said polar solvent, which comprises feeding a hydrocarbon mixture containing a larger amount of the easily soluble components, as a gas, into the middle or lower portion of an extractive distillation column, feeding a hydrocarbon mixture containing a smaller amount of the easily soluble components, as a liquid, to the upper portion of the extractive distillation column, and subjecting them to extractive distillation.
Claim 2
Dependent Claim 95 words
A process of extractive distillation for separating components easily soluble in a polar solvent from at least two hydrocarbon mixtures having different contents of the easily soluble components by extractive distillation using said polar solvent, which comprises feeding a hydrocarbon mixture containing a larger amount of the easily soluble components, as a gas, into the middle or lower portion of an extractive distillation column, feeding a hydrocarbon mixture containing a smaller amount of the easily soluble components, as a liquid, to the upper portion of the extractive distillation column, and subjecting them to extractive distillation.
Claim 3
Dependent Claim 38 words
The process of claim 1 wherein olefinic hydrocarbons are separated from at least two hydrocarbon mixtures containing paraffinic hydrocarbons and olefinic hydrocarbons and having different contents of the olefinic hydrocarbons which are easily soluble in the polar solvent.
Claim 4
Dependent Claim 11 words
The process of claim 2 wherein the polar solvent is dimethylformamide.
Claim 5
Dependent Claim 40 words
The process of claim 1 wherein diolefinic hydrocarbons are separated from at least two hydrocarbon mixtures containing paraffinic hydrocarbons, olefinic hydrocarbons and diolefinic hydrocarbons and having different contents of the diolefinic hydrocarbons which are easily soluble in the polar solvent.
Claim 6
Dependent Claim 11 words
The process of claim 4 wherein the polar solvent is dimethylformamide.

References Cited (Backward Citations)

US3050448A Cited
US3422163A Cited
US3436436A Cited
US3654094A Cited
US3798132A Cited
US4070408A Cited
US4158611A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-12-19 1987-06-20 1987-12-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-12-19 1991-06-20 1991-12-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-12-19 1995-06-20 1995-12-20 $7700.00 Window Closed / Lapsed

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