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US3772158A Expired / Lapsed US ⏱️ 0.0 years remaining

Butadiene recovery process

Assignee: DYK PRESTRESSED TANKS Inc
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Filing: 1971-03-29
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Granted: 1973-11-13
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Expires: 1991-03-29
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Abstract

Abstract A process for separating butadiene from mixtures of butadiene and C4 unsaturates in an extractive distillation of the mixture in the presence of a polar solvent and recovering the butadiene from the fat solvent mixture is disclosed. The butadienecontaining hydrocarbon mixture is introduced to the intermediate portion of an extractive distillation zone wherein it is contacted with the polar solvent which flows downwardly in the zone. In this manner butadiene is recovered in the fat solvent from the bottom of the extractive distillation zone. This fat solvent is introduced to a flash zone, operated at a pressure lower than that of the extractive distillation zone wherein a major portion of the butadiene is vaporized. The remaining solvent, partially depleted in butadiene, is then transferred to a first stripping zone operated at a pressure lower than the extractive distillation zone where the remaining butadiene is stripped from the solvent. The butadiene rich vapor from this first stripping zone is then combined with the vapor obtained in the flash zone and the resulting mixture is compressed. A portion of the compressed vapor is returned to the bottom portion of the extractive distillation zone and butadiene is recovered from the remaining portion of the compressed vapor in a second stripping zone.

Inventors

  • 👤 D Sarno

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 05:08
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/04; C07C7/05; C07C7/08

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 6 words
compressing the resulting mixed vapor phase,
Claim 2
Dependent Claim 29 words
A process according to claim 1 wherein the polar solvent is selected from the group consisting of acetonitrile, acetone, furfural, dimethylformamide, dioxane, phenol and N-methylpyrrolidone and their aqueous admixtures.
Claim 3
Dependent Claim 20 words
A process according to claim 2 wherein the polar solvent is aqueous acetonitrile having at least 10 mol percent water.
Claim 4
Dependent Claim 14 words
returning a portion of the compressed mixed vapor phase to said extractive distillation zone,
Claim 5
Dependent Claim 37 words
passing the remainder of the compressed mixed vapor phase into a second stripping zone operating at a pressure of from 60 to 100 psia, which pressure is greater than the pressure of the low pressure stripping zone,
Claim 6
Dependent Claim 19 words
recovering butadiene from the remainder of the compressed mixed vapor phase as overhead product from said second stripping zone,
Claim 7
Dependent Claim 30 words
transferring the bottoms from said second stripping zone to the top of the low pressure stripping zone, and recovering lean solvent from the bottom of said low pressure stripping zone.

References Cited (Backward Citations)

US2376425A Cited
US2920113A Cited
US2993841A Cited
GB1158566A Cited
US3436436A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-11-12 1977-05-14 1977-11-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-11-12 1981-05-14 1981-11-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-11-12 1985-05-14 1985-11-13 $7700.00 Window Closed / Lapsed

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