Methods for processing liquid organic hydrogen carriers
US-12540284-B2 · Feb 3, 2026 · US
US9453168B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9453168-B2 |
| Application number | US-201414558156-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 2, 2014 |
| Priority date | Jun 11, 2009 |
| Publication date | Sep 27, 2016 |
| Grant date | Sep 27, 2016 |
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A method and a product made by treating a sulfur-containing hydrocarbon heavy feed, e.g., heavy crude asphaltene reduction is disposed herein. The method comprises the steps of: mixing the sulfur-containing hydrocarbon heavy feed with a hydrogen donor solvent and an addled silica to form a mixture and oxidizing the sulfur in the mixture at a temperature between 50° C. and 210° C. wherein the oxidation lowers the amount sulfur in the sulfur-containing hydrocarbon heavy feed by at least 90%.
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What is claimed is: 1. A method of extracting sulfur from an oxidized hydrocarbon feed, said method comprising the steps of: mixing a solution comprising a sulfur containing oxidized hydrocarbon feed, an acidified silica, a hydrogen donor solvent, any unreacted materials and reaction by-products with one or more polar organic solvents; allowing the sulfur containing oxidized hydrocarbon feed to migrate to the polar organic solvent phase; and removing the one or more polar organic solvents by evaporation to recover the sulfur. 2. The method of claim 1 , wherein the oxidized hydrocarbon feed comprises asphaltenes, tar sands, bitumens, heavy petroleum or mixtures thereof. 3. The method of claim 1 , wherein the hydrogen donor solvent is selected from the group consisting of hydrogen, natural petroleum, bases, alcohols, decahydronaphthalene, and tetrahydronaphthalene. 4. The method of claim 1 , wherein acidified silica has a pH range from 0 to 2. 5. The method of claim 1 , wherein the acidified silica comprises an amorphous silica or a silica gel. 6. The method of claim 1 , wherein the polar organic solvent is selected from the group consisting of ethanol, methanol, n-propanol, isopropanol, n-butanol, formic acid, acetic acid, 1,4-dioxane, THF, dichloromethane, acetone, acetonitrile, DMF, DMSO, and any combinations thereof. 7. A sulfur extracted from a hydrocarbon feed by the method of claim 1 . 8. A treated crude oil with reduced asphaltene content made by the method of claim 1 . 9. A method for mid-distillate upgradatlon and sulfur removal in a fuel, said method comprising the steps of: mixing the fuel with a hydrogen donor solvent and an acidified silica to form a mixture; and oxidizing the sulfur in the mixture in air or a mixture of air and O 2 at a temperature between 50° C. and 210° C. 10. The method of claim 9 , wherein the fuel comprises diesel, heavy petroleum, asphaltene, tar sands, bitumens, or mixtures thereof. 11. The method of claim 9 , wherein the hydrogen donor solvent is selected from the group consisting of hydrogen, natural petroleum, bases, alcohols, decahydronaphthalene, and tetrahydronaphthalene. 12. The method of claim 9 , wherein acidified silica has a pH range from 0 to 2. 13. The method of claim 9 , wherein the acidified silica comprises an amorphous silica or a silica gel. 14. The method of claim 9 , wherein the temperature for oxidizing the mixture is 120° C. to 160° C. 15. The method of claim 9 , further comprising the step of adding a reduced noble metal catalyst or a mixture of a noble metal and one or more acidic catalysts, wherein the acidic catalysts comprise zeolites, silica, alumina or combinations thereof. 16. The method of claim 9 , further comprising adding reduced gold, platinum, silver, and palladium metal nanoparticles or mixtures thereof. 17. The method of claim 9 , wherein the silica comprises reduced gold, platinum, silver, and palladium particles or mixtures thereof. 18. The method of claim 9 , wherein the solvents comprise at least one of decalin, tetralin, toluene, heptane, and dodecane. 19. The method of claim 9 , wherein the method lowers the amount sulfur in the fuel by at least 90%. 20. The method of claim 9 , wherein the fuel has less than 1,000, 500, 250, 200, 100, 50 or 10 ppm sulfur after treatment. 21. A fuel made by the method of claim 9 .
Dibenzothiophenes · CPC title
Organic compounds; Autofining · CPC title
Mixing, stirring of fuel components · CPC title
characterised by the catalyst used · CPC title
in combination with oil conversion- or refining processes · CPC title
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