Composition and methods for improved fuel production
US-9222032-B2 · Dec 29, 2015 · US
US9790435B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9790435-B2 |
| Application number | US-201514744590-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 19, 2015 |
| Priority date | Jun 20, 2014 |
| Publication date | Oct 17, 2017 |
| Grant date | Oct 17, 2017 |
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Materials and methods for converting brown grease to useful diesel fuel are described. One material is a palladium catalyst on a silicon/carbon support. A method comprises flowing fresh hydrogen over a reaction of diluted brown grease on a palladium/carbon catalyst.
Opening claim text (preview).
What is claimed is: 1. A catalyst for decarboxylation of a fatty acid, the catalyst comprising: about 0.5% to about 10% palladium by weight; and a support comprising silicon atoms and carbon atoms, a ratio of carbon atoms to silicon atoms of the support being about 3:1 to about 40:1. 2. The catalyst according to claim 1 , wherein the ratio of carbon atoms to silicon atoms is about 4.3:1 to about 34.7:1. 3. The catalyst according to claim 2 wherein the ratio of carbon atoms to silicon atoms is about 4.3:1. 4. The catalyst according to claim 1 having a porous surface with an average pore diameter of about 3.6 nanometers to about 5.4 nanometers. 5. The catalyst according to claim 1 comprising about 5% palladium by weight. 6. The catalyst according to claim 1 wherein the palladium comprises a metal particle having a diameter of about 3 nanometers to about 8 nanometers. 7. The catalyst according to claim 1 wherein the catalyst has an acidity of about 0.10 to about 2.5 mmol/gcat. 8. The catalyst according to claim 1 wherein when exposed to oleic acid, the catalyst converts at least 10% of the oleic acid to n-heptadecane. 9. The catalyst according to claim 8 which converts at least 30% of the oleic acid to n-heptadecane. 10. A method of making a catalyst for decarboxylation of a fatty acid, the method comprising: combining activated carbon with tetraethyl orthosilicate to form a support, a ratio of carbon atoms to silicon atoms of the support being about 3:1 to about 40:1; mixing a palladium solution with the support to result in the catalyst finally comprising about 0.5% to about 10% palladium by weight; and drying the catalyst. 11. The method of claim 10 wherein the tetraethyl orthosilicate is provided in a mass ratio to the activated carbon of about 0.5:1 to about 4:1. 12. The method of claim 11 wherein the mass ratio of tetraethyl orthosilicate to activated carbon is about 4:1. 13. The method of claim 10 wherein palladium comprises about 5% of a weight of the catalyst. 14. The method of claim 10 wherein the palladium solution is a solution of about 1.1% palladium chloride by weight and a weight ratio of palladium chloride to support is about 0.088:1. 15. The method of claim 10 wherein when the catalyst is exposed to oleic acid, it converts at least 10% of the oleic acid to n-heptadecane. 16. A method of converting brown grease to green diesel, the method comprising: diluting the brown grease with a diluent; combining brown grease with a catalyst comprising about 0.5% to about 10% palladium by weight on a support comprising silicon atoms and carbon atoms in a reactor having a gas flow intake and a gas relief valve, a ratio of carbon atoms to silicon atoms of the support being about 3:1 to about 40:1; and providing a volume of gas comprising hydrogen gas through the gas flow intake and allowing gas to exhaust through the gas relief valve to maintain a pressure of about 1.5 megapascal. 17. The method of claim 16 further comprising pretreating the brown grease with a catalyst comprising palladium and carbon under a flow of hydrogen gas. 18. The method of claim 17 wherein pretreating comprises about two hours at about one hundred degrees Celsius at a pressure of 1.5 megapascal. 19. The method of claim 16 wherein the catalyst is soaked with dodecane and reduced under a flow of hydrogen gas prior to combining with brown grease.
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