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US3972692A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removing acid from hydrocarbons

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1975-04-03
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Granted: 1976-08-03
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Expires: 1995-04-03
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Abstract

Abstract Acidic gases, such as H2S, COS, CO2, and HCN are removed from a mixture of light hydrocarbons by first separating the mixture into a gas portion and a liquid portion. The gas portion is compressed, water washed and scrubbed with an absorbing solution prior to separating at least one hydrocarbon from other hydrocarbons in the mixture. The liquid portion is stripped of H2S. The stripped vapors containing the stripped H2S may be recycled to the gas compression step.

Inventors

  • 👤 Roberto L. Machado
  • 👤 Benjamin Eisenberg
  • 👤 George P. Baumann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 13:39
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/005; B; B01; B01D; B01D53/00; B01D53/14; B01D53/1456; C07C7/11

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 96 words
In a process for separating at least one hydrocarbon from other hydrocarbons in a mixture comprising light hydrocarbons and acidic gases, the improvement which comprises removing said acidic gases from said mixture prior to said hydrocarbon separation step by the steps which comprise: a. separating said mixture into a gaseous portion and a liquid portion; b. subjecting said gaseous portion to compression, water washing, and scrubbing with an aqueous absorbing solution; and c. subjecting the liquid portion to stripping to remove at least a portion of the hydrogen sulfide therefrom and produce a hydrogen sulfide-containing effluent.
Claim 2
Dependent Claim 96 words
In a process for separating at least one hydrocarbon from other hydrocarbons in a mixture comprising light hydrocarbons and acidic gases, the improvement which comprises removing said acidic gases from said mixture prior to said hydrocarbon separation step by the steps which comprise: a. separating said mixture into a gaseous portion and a liquid portion; b. subjecting said gaseous portion to compression, water washing, and scrubbing with an aqueous absorbing solution; and c. subjecting the liquid portion to stripping to remove at least a portion of the hydrogen sulfide therefrom and produce a hydrogen sulfide-containing effluent.
Claim 3
Dependent Claim 17 words
The process of claim 1, wherein the hydrogen sulfide-containing effluent is recycled to said gas compression step.
Claim 4
Dependent Claim 27 words
The process of claim 1, wherein said acidic gases are selected from the group consisting of H 2 S, CO 2 , COS, HCN and mixtures thereof.
Claim 5
Dependent Claim 22 words
The process of claim 1, wherein said mixture of light hydrocarbons comprises hydrocarbons boiling in the range between Cl and 400° F.
Claim 6
Dependent Claim 21 words
The process of claim 1, wherein said mixture of light hydrocarbons comprises the overhead vapor of a coking reaction products fractionator.
Claim 7
Dependent Claim 22 words
The process of claim 1, wherein said mixture of light hydrocarbons comprises the overhead vapor of a catalytic cracking reaction products fractionator.

References Cited (Backward Citations)

US3553936A Cited
US3664091A Cited
US3733779A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-03 1980-02-02 1980-08-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-03 1984-02-02 1984-08-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-03 1988-02-02 1988-08-03 $7700.00 Window Closed / Lapsed

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