US4248695A
Expired / Lapsed
US
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Desulfurizing a fuel with alkanol-alkali metal hydrosulfide solution
Assignee: Individual
•
Filing: 1979-10-01
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Granted: 1981-02-03
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Expires: 1999-10-01
Abstract
Abstract Petroleum crude and certain liquid distillate fractions derived therefrom, and other sulfur containing fuels or residues are reduced in sulfur content by intimately contacting the fuel or residues with alkanol solutions of alkali metal hydrosulfides, at temperatures and pressures from ambient up to the critical temperature of the alkanol for from 1 to 20 minutes. Thereafter, the fuel is caused to separate from the alkanol solution by the addition of water. A liquid-liquid separation separates desulfurized fuel from the alkanol solution. Hydrogen sulfide formed in the process is used to re-generate alkali metal hydrosulfide for use in desulfurizing additional petroleum fuel.
Inventors
- 👤 Rollan Swanson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:38
CPC Classifications
C; C10; C10G; C10G29/00; C10G29/06; C10G29/10
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
196 words
A process for desulfurizing a sulfur-containing fuel comprising contacting said fuel with a (lower) primary alkanol solution containing an alkali metal hydrosulfide at a temperature and pressure from ambient up to the critical temperature of the alkanol solvent, the water content of said solution being below that which will cause said hydrosulfide to decompose into K 2 S hydroxide, and separating said fuel from said alkanol solution now containing the corresponding higher sulfur content alkali metal polysulfide with the proviso that the volume ratio of said alkanol solution to said fuel is determined by the gram mols of sulfur present in the fuel divided by 11/2 gram mols of sulfur, when sodium is the alkali metal, times the molecular weight of sodium hydrosulfide divided by the number of grams of sodium hydrosulfide per milliliters of the alkanol solution and the volume ratio of said alkanol solution to said fuel is determined by the gram mols of sulfur present in the fuel divided by 2 gram mols of sulfur, when potassium is the alkali metal, times the molecular weight of potassium hydrosulfide divided by the number of grams of potassium hydrosulfide per milliliters of the alkanol solution.
Claim 2
Dependent Claim
196 words
A process for desulfurizing a sulfur-containing fuel comprising contacting said fuel with a (lower) primary alkanol solution containing an alkali metal hydrosulfide at a temperature and pressure from ambient up to the critical temperature of the alkanol solvent, the water content of said solution being below that which will cause said hydrosulfide to decompose into K 2 S hydroxide, and separating said fuel from said alkanol solution now containing the corresponding higher sulfur content alkali metal polysulfide with the proviso that the volume ratio of said alkanol solution to said fuel is determined by the gram mols of sulfur present in the fuel divided by 11/2 gram mols of sulfur, when sodium is the alkali metal, times the molecular weight of sodium hydrosulfide divided by the number of grams of sodium hydrosulfide per milliliters of the alkanol solution and the volume ratio of said alkanol solution to said fuel is determined by the gram mols of sulfur present in the fuel divided by 2 gram mols of sulfur, when potassium is the alkali metal, times the molecular weight of potassium hydrosulfide divided by the number of grams of potassium hydrosulfide per milliliters of the alkanol solution.
Claim 3
Dependent Claim
22 words
The process of claim 1, wherein said alkali metal is sodium or potassium and said polysulfides are sodium tetrasulfide or potassium pentasulfide.
Claim 4
Dependent Claim
37 words
The process of claim 2 in which the hydrogen sulfide formed in the process is passed through the water solution of the separated alkali metal polysulfide under pressure while being cooled to not less than 55° F.
Claim 5
Dependent Claim
17 words
The process of claim 1, wherein said contacting takes place for between one minute and twenty minutes.
Claim 6
Dependent Claim
27 words
The process of claim 1, wherein said hydrosulfide is potassium hydrosulfide and said contacting takes place for a period of 5 to 30 days at ambient temperature.
Claim 7
Dependent Claim
31 words
The process of claim 1, wherein the concentration of the alcohol solution, when ethanol is the alcohol, is of the order of 0.24 grams of potassium hydrosulfide per milliliter of solution.
Claim 8
Dependent Claim
20 words
The process of claim 1, wherein the alkali metal hydrosulfide concentration in said solution ranges from one percent to saturation.
Claim 9
Dependent Claim
35 words
The process of claim 1, further including the step of adding 10% water to said separated alkanol solution when the alcohol is below boiling temperatures to separate the alcohol and the polysulfide from the fuel.
Claim 10
Dependent Claim
43 words
The process of claim 1, in which water in an amount of not more than one half of the volume of the alkanol is added to dissolve the alkali metal polysulfide to form a concentrated solution in water which separates from the fuel.
Claim 11
Dependent Claim
19 words
The process of claim 1, wherein said alkanol solution contains also an alkali metal sulfide in a minor amount.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-02-03 | 1984-08-04 | 1985-02-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-02-03 | 1988-08-04 | 1989-02-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-02-03 | 1992-08-04 | 1993-02-03 | $7700.00 | Window Closed / Lapsed |