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Separation of toluene from non-aromatic hydrocarbons by extractive distillation

Assignee: Individual
•
Filing: 1981-11-20
•
Granted: 1982-12-14
•
Expires: 2001-11-20
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Abstract

Abstract Toluene is virtually impossible to separate from similar boiling non-aromatic hydrocarbons by conventional rectification or distillation. Toluene can be readily separated from similar boiling non-aromatic hydrocarbons by using extractive distillation in which the extractive agent is a mixture of phthalic anhydride and/or maleic anhydride plus a suitable solvent. A typical mixture comprises phthalic anhydride, maleic anhydride and glycerol triacetate.

Inventors

  • 👤 Lloyd Berg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 17:02
CPC Classifications
C; C07; C07C; C07C63/00; C07C63/14; C07C63/15; C07C63/16; C07C57/00; C07C57/02; C07C57/13; C07C57/145; C07C7/00; C07C7/04; C07C7/05; C07C7/08

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 90 words
A method for separating toluene from close boiling non-aromatic hydrocarbons which comprises distilling a mixture of toluene and close boiling non-aromatic hydrocarbons in a rectification column in the presence of an effective amount of an extractive agent sufficient to provide a relative volatility of 2.5 or greater comprising effective proportions of phthalic anhydride and/or maleic anhydride and a solvent from the group consisting of glycerol triacetate, dimethylformamide, ethyl acetoacetate, acetonyl acetone, acetophenone, 2,4-pentanedione, ethylene glycol phenyl ether, dichlorodiethyl ether, dimethylacetamide, benzophenone, ethylene glycol diacetate, furfural, nitrobenzene, 2-nitrotoluene, sulfolane, phenol, dimethylsulfoxide.
Claim 2
Independent Claim 90 words
A method for separating toluene from close boiling non-aromatic hydrocarbons which comprises distilling a mixture of toluene and close boiling non-aromatic hydrocarbons in a rectification column in the presence of an effective amount of an extractive agent sufficient to provide a relative volatility of 2.5 or greater comprising effective proportions of phthalic anhydride and/or maleic anhydride and a solvent from the group consisting of glycerol triacetate, dimethylformamide, ethyl acetoacetate, acetonyl acetone, acetophenone, 2,4-pentanedione, ethylene glycol phenyl ether, dichlorodiethyl ether, dimethylacetamide, benzophenone, ethylene glycol diacetate, furfural, nitrobenzene, 2-nitrotoluene, sulfolane, phenol, dimethylsulfoxide.
Claim 3
Dependent Claim 23 words
The method of claim 1 in which the extractive agent is phthalic anhydride and a solvent from the group listed in claim 1.
Claim 4
Dependent Claim 23 words
The method of claim 1 in which the extractive agent is maleic anhydride and a solvent from the group listed in claim 1.

References Cited (Backward Citations)

US2655467A Cited
US2431655A Cited
US3114783A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-12-13 1986-06-14 1986-12-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-12-13 1990-06-14 1990-12-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-12-13 1994-06-14 1994-12-14 $7700.00 Window Closed / Lapsed

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