The present application generally relates to the introduction of a renewable fuel oil as a feedstock into refinery systems or field upgrading equipment. For example, the present application is directed to methods of introducing a liquid thermally produced from biomass into a petroleum conversion uni
The present application generally relates to the introduction of a renewable fuel oil as a feedstock into refinery systems or field upgrading equipment. For example, the present application is directed to methods of introducing a liquid thermally produced from biomass into a petroleum conversion unit; for example, a refinery fluid catalytic cracker (FCC), a coker, a field upgrader system, a hydrocracker, and/or hydrotreating unit; for co-processing with petroleum fractions, petroleum fraction reactants, and/or petroleum fraction feedstocks and the products, e.g., fuels, and uses and value of the products resulting therefrom.
대표청구항▼
1. A fuel, comprising: a product of a fluidized catalytic cracker co-processing a feed comprising a petroleum fraction and an unenriched renewable fuel oil feedstock, wherein the co-processing converts at least 70 wt. % of the oxygen in the unenriched renewable fuel oil feedstock, as measured on a m
1. A fuel, comprising: a product of a fluidized catalytic cracker co-processing a feed comprising a petroleum fraction and an unenriched renewable fuel oil feedstock, wherein the co-processing converts at least 70 wt. % of the oxygen in the unenriched renewable fuel oil feedstock, as measured on a moisture free basis, into water, the unenriched renewable fuel oil feedstock comprising: i) a product of non-catalytic rapid thermal conversion of a cellulosic biomass; andii) a carbon content of at least 40 wt. % on a moisture-free basis, and an oxygen content in the range of between 20-50 wt. % on a moisture-free basis. 2. The fuel of claim 1, wherein the feed comprises: i) 93-99.95 wt. % of the petroleum fraction; andii) 0.05-7 wt. % of the unenriched renewable fuel oil feedstock. 3. The fuel of claim 1, wherein the fuel is less than 0.25 wt. % oxygen. 4. The fuel of claim 3, wherein the unenriched renewable fuel oil feedstock has a solids content of less than 0.5 wt. % and a water content in the range of between 10-40 wt. %. 5. The fuel of claim 4, wherein the cellulosic biomass comprises wood or wood residues. 6. The fuel of claim 4, wherein the solids content is less than 0.1 wt. %. 7. The fuel of claim 4, wherein the unenriched renewable fuel oil feedstock has an ash content of less than 0.05 wt. %. 8. The fuel of claim 1, wherein the cellulosic biomass comprises wood or wood residues. 9. The fuel of claim 1, wherein the cellulosic biomass comprises bagasse, palm fronds, or empty fruit bunches. 10. The fuel of claim 1, wherein at least 60 wt. % of the cellulosic biomass is converted to the unenriched renewable fuel oil feedstock, and the feed further comprises: i) 93-99.95 wt. % of the petroleum fraction; andii) 0.05-7 wt. % of the unenriched renewable fuel oil feedstock, the unenriched renewable fuel oil feedstock further comprising a product of mechanical grinding of the cellulosic biomass. 11. The fuel of claim 10, wherein the unenriched renewable fuel oil feedstock comprises a carbon content in the range of between 50-75 wt. % on a moisture-free basis. 12. The fuel of claim 11, wherein: i) the cellulosic biomass comprises wood or wood residues; andii) the unenriched renewable fuel oil feedstock has a solids content of less than 0.5 wt. % and an ash content of less than 0.1 wt. %. 13. The fuel of claim 1, wherein the unenriched renewable fuel oil feedstock further comprises: i) a product of mechanical grinding of the cellulosic biomass; andii) a carbon content in the range of between 50-75 wt. % on a moisture-free basis. 14. The fuel of claim 13, wherein: i) the cellulosic biomass comprises bagasse, palm fronds, or empty fruit bunches; andii) the unenriched renewable fuel oil feedstock has a solids content of less than 0.5 wt. % and an ash content of less than 0.1 wt. %. 15. The fuel of claim 10, wherein: i) the cellulosic biomass comprises wood or wood residues;ii) the unenriched renewable fuel oil feedstock has a solids content of less than 0.5 wt. % and an ash content of less than 0.1 wt. %; andiii) the unenriched renewable fuel oil feedstock has an energy content level in the range of between 60-80% of the energy content contained in the cellulosic biomass. 16. The fuel of claim 10, wherein the unenriched renewable fuel oil feedstock has an energy content level of between 45-85% on a moisture-free basis, relative to the energy content of the petroleum fraction. 17. The fuel of claim 10, wherein: i) the cellulosic biomass comprises wood or wood residues;ii) the unenriched renewable fuel oil feedstock has a solids content of less than 0.5 wt. % and an ash content of less than 0.1 wt. %; andiii) the fluidized catalytic cracker is operated with a catalyst contact time in the range of between 3-5 seconds. 18. The fuel of claim 17, wherein the cellulosic biomass comprises wood or wood residues. 19. The fuel of claim 1, wherein: i) the petroleum fraction comprises a vacuum gas oil;ii) the unenriched renewable fuel oil feedstock has a solids content of less than 0.5 wt. % and an ash content of less than 0.1 wt. %; andiii) the fluidized catalytic cracker is operated with a catalyst contact time in the range of between 3-5 seconds. 20. The fuel of claim 1, wherein the petroleum fraction comprises a heavy gas oil or a heavy-middle distillate feedstock.
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