Production of renewable biofuels
View Patent ↗A process and system for separating and upgrading bio-oil into renewable fuels is provided. The process comprises separating bio-oil into a light fraction and heavy fraction based on their boiling points. The heavy fraction is then subjected to hydrotreatment, while the light fraction is not subjected to hydrotreatment. At least a portion of the un-hydrotreated light fraction and at least a portion of the hydrotreated heavy fraction are blended with petroleum-derived gasoline to thereby provide a renewable gasoline, and at least a portion of the hydrotreated heavy fraction is blended with petroleum-derived diesel to thereby provide a renewable diesel.
1. A system for producing a bio-oil, said system comprising:
a biomass feedstock source for providing solid particulate biomass;
a conversion reactor for thermally converting said solid particulate biomass into a bio-oil;
a separator for separating said bio-oil into at least a bio-gasoline fraction and a bio-distillate fraction;
a hydrotreater for hydrotreating said bio-distillate fraction to thereby produce a hydrotreated product;
a fractionator for fractionating said hydrotreated product into at least a hydrotreated bio-gasoline and a hydrotreated bio-diesel;
a petroleum-derived gasoline source for providing a petroleum-derived gasoline,
a gasoline blending system for combining at least a portion of said bio-gasoline fraction and at least a portion of said hydrotreated bio-gasoline with said petroleum-derived gasoline, wherein said separator is in fluid communication with said gasoline blending system and said separator is configured to introduce at least a portion of said bio-gasoline fraction into gasoline blending system;
a petroleum-derived diesel source for providing a petroleum-derived diesel; and
a diesel blending system for combining at least a portion of said hydrotreated bio-diesel with said petroleum-derived diesel.
2. The system of claim 1 , wherein said conversion reactor is a riser reactor.
3. The system of claim 1 , wherein said separator is a heated distillation column.
4. The system of claim 3 , wherein said system does not include a hydrotreater for hydrotreating said bio-oil upstream of said separator.
5. The system of claim 1 , wherein said fractionator is operable to fractionate said hydrotreated product into said hydrotreated bio-gasoline, said hydrotreated bio-diesel, and a hydrotreated bio-fuel oil.
6. The system of claim 5 , further comprising a petroleum-derived fuel oil source for providing a petroleum-derived fuel oil, further comprising a fuel oil blending system for combining at least a portion of said hydrotreated bio-fuel oil with said petroleum-derived fuel oil.
7. A system for producing one or more renewable fuels, said system comprising:
a biomass feedstock source for providing solid particulate biomass;
a conversion reactor for thermally converting said solid particulate biomass into a bio-oil;
a separation system for separating said bio-oil into one or more bio-gasoline fractions and one or more bio-distillate fractions, wherein said separation system comprises a fluids separator for separating said bio-oil into said bio-gasoline fractions and said bio-distillate fractions;
a petroleum-derived gasoline source for providing a petroleum-derived gasoline;
a first blending system for combining at least one of said bio-gasoline fractions with said petroleum-derived gasoline, wherein said fluids separator is in fluid communication with said first blending system, wherein said fluids separator is configured to introduce at least a portion of said bio-gasoline fractions into said first blending system for combination with said petroleum-derived gasoline;
one or more petroleum-derived distillate sources for providing one or more petroleum-derived distillates;
a second blending system for combining at least one of said bio-distillate fractions with at least one of said petroleum-derived distillates; and
a hydrotreater for (i) hydrotreating at least one of said bio-gasoline fractions prior to combination with said petroleum-derived gasoline in said first blending system and/or (ii) hydrotreating least one of said bio-distillate fractions prior to combination with at least one of said petroleum-derived distillates in said second blending system.
8. The system of claim 7 , wherein said fluids separator comprises a heated distillation column.
9. The system of claim 7 , wherein said fluids separator is in fluid communication with said hydrotreater, wherein said fluids separator is configured to introduce at least a portion of said bio-distillate fractions into said hydrotreater.
10. The system of claim 9 , wherein said separation system further comprises a fractionator for fractionating at least a portion of said bio-distillate fractions.
11. The system of claim 10 , wherein said fractionator is located downstream of said hydrotreater.
12. The system of claim 11 , wherein said fractionator is operable to produce at least one of said bio-gasoline fractions and at least one of said bio-distillate fractions.
13. The system of claim 11 , wherein said fractionator is operable to produce at least two of said bio-distillate fractions.
14. The system of claim 13 , wherein said petroleum derived-distillate sources comprise a petroleum-derived diesel source for providing a petroleum-derived diesel and a petroleum-derived fuel oil source for providing a petroleum-derived fuel oil, wherein said bio-distillate fractions comprise a hydrotreated bio-diesel and a hydrotreated bio-fuel oil, wherein said second blending system comprises a diesel blending system for combining at least a portion of said petroleum-derived diesel with at least a portion of said hydrotreated bio-diesel and a fuel oil blending system for combining at least a portion of said petroleum-derived fuel oil with at least a portion of said hydrotreated bio-fuel oil.
15. The system of claim 10 , wherein said fractionator is in fluid communication with said first blending zone and is operable to produce at least one of said bio-gasoline fractions, wherein said fractionator is configured to introduce said bio-gasoline fraction produced by said fractionator into said first blending zone.