Process and apparatus for producing hydrocarbons from feed-stocks comprising tall oil and terpene-compounds
US-9382483-B2 · Jul 5, 2016 · US
US9885000B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9885000-B2 |
| Application number | US-201414781989-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 24, 2014 |
| Priority date | Apr 2, 2013 |
| Publication date | Feb 6, 2018 |
| Grant date | Feb 6, 2018 |
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The present invention provides a composition comprising 8-30 mass % of C 4-12 linear alkanes, 5-50 mass % of C 4-12 branched alkanes, 25-60 mass % of C 5-12 cycloalkanes, 1-25 mass of C 6-12 aromatic hydrocarbons, no more than 1 mass % of alkenes, and no more than 0.5 mass % in total of oxygen-containing compounds; wherein the total amount of C 4-12 alkanes is 40-80 mass %, and the total amount of C 4-12 alkanes, C 5-12 cycloalkanes and C 6-12 aromatic hydrocarbons is at least 95 mass %; and wherein the amounts are based on the mass of the composition. Also provided is a method for producing the composition comprising the step of hydroprocessing a biological feedstock using a catalyst and the step of fractionating the product of the hydroprocessing step.
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The invention claimed is: 1. A composition comprising 8-30 mass % of C 4-12 linear alkanes, 20-50 mass % of C 4-12 branched alkanes, 25-60 mass % of C 5-12 cycloalkanes, 1-25 mass of C 6-12 aromatic hydrocarbons, no more than 1 mass % of alkenes, and no more than 0.5 mass % in total of oxygen-containing compounds; wherein the total amount of C 4-12 alkanes is 40-70 mass %, and the total amount of C 4-12 alkanes, C 5-12 cycloalkanes and C 6-12 aromatic hydrocarbons is at least 95 mass %; and wherein the amounts are based on the mass of the composition. 2. A composition according to claim 1 , wherein the amount of C 4-12 linear alkanes is 10-20 mass %. 3. A composition according to claim 1 , wherein the amount of C 4-12 branched alkanes is 20-40 mass %. 4. A composition according to claim 1 , wherein the amount of C 5-12 cycloalkanes is 30-50 mass %. 5. A composition according to claim 1 , wherein the amount of C 6-12 aromatic hydrocarbons is 2-15 mass %. 6. A composition according to claim 1 , wherein the linear alkanes are C 5-10 linear alkanes. 7. A composition according to claim 1 , wherein the branched alkanes are C 5-11 branched alkanes. 8. A composition according to claim 1 , wherein the cycloalkanes are C 6-10 cycloalkanes. 9. A composition according to claim 1 , wherein the aromatic hydrocarbons are C 6-10 aromatic hydrocarbons. 10. A fuel blend comprising a composition as defined in claim 1 . 11. A fuel blend according to claim 10 , wherein the amount of the composition is 2-85 vol. % based on the volume of the fuel blend. 12. A fuel blend according to claim 11 , wherein the amount of the composition is 5-25 vol. %. 13. A fuel blend according to claim 11 , which further comprises a petroleum-derived fuel. 14. A fuel blend according to claim 13 , wherein the petroleum-derived fuel is petroleum naphtha and/or petroleum gasoline. 15. A fuel blend according to claim 10 , which further comprises ethanol. 16. A fuel blend according to claim 15 , wherein the amount of ethanol is up to 85 vol. % based on the volume of the fuel blend. 17. A fuel blend according to claim 16 , wherein the amount of ethanol is 75-85 vol %. 18. A fuel blend according to claim 10 , which further comprises at least one of butane, isobutanol and ethyl tert-butyl ether. 19. A fuel blend according to claim 10 , which comprises 2-25 vol. % of the composition, 75-85 vol. % of ethanol, 1-5 vol. % of ether compounds containing five or more carbon atoms, and up to 2 vol. % of C 3-8 higher alcohols, the amount of butane contained in the fuel blend being 2-10 vol. %. 20. The composition according to claim 1 , wherein the density of the composition is 720-775 kg/m 3 as measured at 15° C. by EN ISO 12185 method. 21. The composition according to claim 1 , wherein the composition begins to distill at 30° C. and finishes distilling at 210° C. as measured using EN ISO 3405 method.
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