Pipeline arrangement for utilizing a gas comprising biomethane
US-9222048-B1 · Dec 29, 2015 · US
US9567541B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9567541-B2 |
| Application number | US-201314073208-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 6, 2013 |
| Priority date | Nov 12, 2012 |
| Publication date | Feb 14, 2017 |
| Grant date | Feb 14, 2017 |
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A jet-range hydrocarbon product includes a mixture of paraffins. The mixture exhibits a freeze point of less than or equal to about −70° C., a 95% distillation point of greater than or equal to about 275° C., and a smooth boiling point curve that is characterized as having no intervals of the boiling point curve having a slope that is steeper than 4° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 20% to about 80%. The steepness of the boiling point curve slope is calculated over any 10 mass % increments within the specified mass % ranges.
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What is claimed is: 1. A jet-range hydrocarbon product comprising: a mixture of paraffins, wherein the mixture exhibits a freeze point of less than or equal to about −70° C., a 95% distillation point of greater than or equal to about 275° C., and a smooth boiling point curve that is characterized as having no intervals of the boiling point curve having a slope that is steeper than 4° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 20% to about 80%, wherein the steepness of the boiling point curve slope is calculated over any 10 mass % increments within the specified mass % ranges; and wherein the jet-range hydrocarbon product is produced by oligomerization of C4 olefins using an MTT catalyst. 2. The jet-range hydrocarbon product of claim 1 , wherein the smooth boiling point curve is characterized as having no intervals of the boiling point curve steeper than 4° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 10% to about 90%. 3. The jet-range hydrocarbon product of claim 1 , wherein the smooth boiling point curve is further characterized as having no intervals shallower than 0.3° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 20% to about 80%. 4. The jet-range hydrocarbon product of claim 3 , wherein the smooth boiling point curve is further characterized as having no intervals shallower than 0.2° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 20% to about 80%. 5. The jet-range hydrocarbon product of claim 3 , wherein the smooth boiling point curve is characterized as having no intervals shallower than 0.3° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 10% to about 90%. 6. The jet-range hydrocarbon product of claim 5 , wherein the smooth boiling point curve is further characterized as having no intervals shallower than 0.2° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 20% to about 80%. 7. The jet-range hydrocarbon product of claim 1 , wherein the mixture exhibits a 95% distillation point of greater than or equal to about 285° C. 8. The jet range hydrocarbon product of claim 1 , wherein the mixture exhibits a freeze point of less than or equal to about −75° C. 9. The jet range hydrocarbon product of claim 1 , wherein the smooth boiling point curve is characterized as having no intervals of the boiling point curve steeper than 2.5° C./mass %. 10. The jet range hydrocarbon product of claim 1 , wherein the mixture of paraffins have a 14 C/ 12 C ratio indicative of atmospheric carbon. 11. A jet-range hydrocarbon product comprising: a mixture of paraffins, wherein the mixture exhibits a freeze point of less than or equal to about −70° C., a 95% distillation point of greater than or equal to about 275° C., and a smooth boiling point curve that is characterized as having no intervals of the boiling point curve having a slope that is steeper than 4° C./mass % and no intervals shallower than 0.3° C./mass % as defined by ASTM standard D2887 between mass recovered ranges of about 10% to about 90%, wherein the steepness of the boiling point curve slope is calculated over any 10 mass % increments within the specified mass % ranges; and wherein the jet-range hydrocarbon product is produced by oligomerization of C4 olefins using an MTT catalyst. 12. The jet range hydrocarbon product of claim 11 , wherein the mixture of paraffins have a 14 C/ 12 C ratio indicative of atmospheric carbon. 13. The jet range hydrocarbon product of claim 12 , wherein the mixture exhibits a freeze point of less than or equal to about −75° C. 14. The jet-range hydrocarbon product of claim 13 , wherein the mixture exhibits a 95% distillation point of greater than or equal to about 285° C.
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