초록 ▼

Conversion of renewable hydrocarbons to transportation fuels is required to reduce carbon emission, limit the use of fossil fuels, and develop renewable energy sources. Sorbitol, xylitol and trehelose are polyalcohols generated from the liquefaction of various sugars and carbohydrates in biomass fro

Conversion of renewable hydrocarbons to transportation fuels is required to reduce carbon emission, limit the use of fossil fuels, and develop renewable energy sources. Sorbitol, xylitol and trehelose are polyalcohols generated from the liquefaction of various sugars and carbohydrates in biomass from algae, corn, sugarcane, switchgrasses, and biological wastes. Mixtures of aqueous polyols and fuel feedstocks are catalyzed over metal catalysts to produce hexanes, pentanes, and lighter hydrocarbons. By managing the catalyst, reaction conditions and sulfur content, the octane value of the product fuel is dramatically increased.

대표청구항 ▼

1. A hydrotreating process comprising: a) mixing a polyol feedstock with a fuel oil feedstock to form a reaction mixture,b) reacting the reaction mixture (a) in the presence of a hydrotreating catalyst, andc) obtaining one or more light gasses, gasolines, carbon monoxide, carbon dioxide, and mixture

1. A hydrotreating process comprising: a) mixing a polyol feedstock with a fuel oil feedstock to form a reaction mixture,b) reacting the reaction mixture (a) in the presence of a hydrotreating catalyst, andc) obtaining one or more light gasses, gasolines, carbon monoxide, carbon dioxide, and mixtures thereofwherein said reaction occurs between about 400 and 1000° F., about 150 and 3000 psig, in the presence of hydrogen and a hydrotreating catalyst; andfurther wherein said polyol feedstock comprises at least one of Arabitol, Ribitol, Xylitol, Allitol, Dulcitol, Galactitol, Iditol, Mannitol, Sorbitol, Isomalt, Lactitol, Maltitol, Trehalose, and combinations thereof. 2. The hydrotreating process of claim 1, wherein said fuel oil feedstock is selected from the group consisting of gasoline, jet fuel, kerosene, heating oil, fuel oils, diesel fuel, petro-diesel, biodiesel, synthetic diesel, blended diesel, and combinations thereof. 3. The hydrotreating process of claim 1, wherein said hydrotreating catalyst is selected from the group consisting of cobalt (Co), molybdenum (Mo), nickel (Ni), titanium (Ti), tungsten (W), zinc (Zn), antimony (Sb), bismuth (Bi), cerium (Ce), vanadium (V), niobium (Nb), tantalum (Ta), chromium (Cr), manganese (Mn), rhenium (Re), iron (Fe), platinum (Pt), iridium (Ir), palladium (Pd), osmium (Os), rhodium (Rh), ruthenium (Ru), and combinations thereof. 4. The hydrotreating process of claim 1, wherein said hydrotreating catalyst is a bimetallic catalyst selected from the group consisting of Co/Mo, Co/W, Ni/Mo, Ni/W, Ti/Mo, Ti/W and combinations thereof. 5. The hydrotreating process of claim 1, wherein said reaction occurs at an approximate temperature of 400° F., 425° F., 450° F., 475° F., 500° F., 525° F., 550° F., 575° F., 600° F., 625° F., 650° F., 675° F., 700° F., 725° F., 750° F., 775° F., 800° F., 825° F., 850° F., 875° F., or 900° F. 6. The hydrotreating process of claim 1, wherein said reaction occurs at an approximate pressure of 500, 550, 600, 650, 700, 750, 800, 850, 900, 950, 1000, 1050, 1100, 1150, 1200, 1250, 1500, 1750, 2000, 2250, 2500, 2750, and 3000 psig. 7. The hydrotreating process of claim 1, wherein said hydrotreating catalyst is an highly active catalyst selected from the group consisting of Co/Mo, Co/W, Ni/Mo, Ni/W, Ti/Mo, Ti/W, Co/Mo/W, Ni/Mo/W, Ti/Mo/W and combinations thereof. 8. A process for converting biomass to gasoline comprising: a) liquifying biomass to generate a polyol feedstock,b) mixing the polyol feedstock with a fuel oil feedstock to form a reaction mixture,c) reacting the reaction mixture (b) in the presence of a hydrotreating catalyst, andd) obtaining one or more light gasses, gasolines, carbon monoxide, carbon dioxide, and mixtures thereofwherein said reaction occurs between about 400 and 1000° F., about 150 and 3000 psig, in the presence of hydrogen and a hydrotreating catalyst; andfurther wherein said polyol feedstock comprises at least one of Arabitol, Ribitol, Xylitol, Allitol, Dulcitol, Galactitol, Iditol, Mannitol, Sorbitol, Isomalt, Lactitol, Maltitol, Trehalose, and combinations thereof. 9. The process for converting biomass to gasoline of claim 8, wherein said fuel oil feedstock is selected from the group consisting of gasoline, jet fuel, kerosene, heating oil, fuel oils, diesel fuel, petro-diesel, bio-diesel, synthetic diesel, blended diesel, and combinations thereof. 10. The process for converting biomass to gasoline of claim 8, wherein said hydrotreating catalyst is selected from the group consisting of cobalt (Co), molybdenum (Mo), nickel (Ni), titanium (Ti), tungsten (W), zinc (Zn), antimony (Sb), bismuth (Bi), cerium (Ce), vanadium (V), niobium (Nb), tantalum (Ta), chromium (Cr), manganese (Mn), rhenium (Re), iron (Fe), platinum (Pt), iridium (Ir), palladium (Pd), osmium (Os), rhodium (Rh), ruthenium (Ru), and combinations thereof. 11. The process for converting biomass to gasoline of claim 8, wherein said hydrotreating catalyst is a bimetallic catalyst selected from the group consisting of Co/Mo, Co/W, Ni/Mo, Ni/W, Ti/Mo, Ti/W and combinations thereof. 12. The process for converting biomass to gasoline of claim 8, wherein said reaction occurs at an approximate temperature of 400° F., 425° F., 450° F., 475° F., 500° F., 525° F., 550° F., 575° F., 600° F., 625° F., 650° F., 675° F., 700° F., 725° F., 750° F., 775° F., 800° F., 825° F., 850° F. 875° F., or 900° F. 13. The hydrotreating process of claim 8, wherein said reaction occurs at an approximate pressure of 500, 550, 600, 650, 700, 750, 800, 850, 900, 950, 1000, 1050, 1100, 1150, 1200, 1250, 1500, 1750, 2000, 2250, 2500, 2750, and 3000 psig. 14. The process for converting biomass to gasoline of claim 8, wherein said hydrotreating catalyst is an highly active catalyst selected from the group consisting of Co/Mo, Co/W, Ni/Mo, Ni/W, Ti/Mo, Ti/W, Co/Mo/W, Ni/Mo/W, Ti/Mo/W and combinations thereof. 15. A process for converting biomass to gasoline comprising: a) liquifying biomass to generate a polyol feedstock and biomass solidsb) mixing the polyol feedstock with a fuel oil feedstock to form a reaction mixture,c) hydrotreating the reaction mixture (b) in the presence of a hydrotreating catalyst, wherein said reaction occurs between about 400 and 1000° F., and between about 500 and 3000 psig, in the presence of hydrogen and a hydrotreating catalystd) obtaining one or more light gasses, gasolines, carbon monoxide, carbon dioxide, and mixtures thereof, ande) reforming biomass solids from (a) and light gasses (d) to generate H2 and COX, wherein said H2 generated by reforming (e) is part of the hydrogen consumed during hydrotreating (c); andfurther wherein said polyol feedstock comprises at least one of Arabitol, Ribitol, Xylitol, Allitol, Dulcitol, Galactitol, Iditol, Mannitol, Sorbitol, Isomalt, Lactitol, Maltitol, Trehalose, and combinations thereof. 16. The process for converting biomass to gasoline of claim 15, wherein said fuel oil feedstock is selected from the group consisting of gasoline, jet fuel, kerosene, heating oil, fuel oils, diesel fuel, petro-diesel, bio-diesel, synthetic diesel, blended diesel, and combinations thereof. 17. The process for converting biomass to gasoline of claim 15, wherein said hydrotreating catalyst is selected from the group consisting of cobalt (Co), molybdenum (Mo), nickel (Ni), titanium (Ti), tungsten (W), zinc (Zn), antimony (Sb), bismuth (Bi), cerium (Ce), vanadium (V), niobium (Nb), tantalum (Ta), chromium (Cr), manganese (Mn), rhenium (Re), iron (Fe), platinum (Pt), iridium (Ir), palladium (Pd), osmium (Os), rhodium (Rh), ruthenium (Ru), and combinations thereof. 18. The process for converting biomass to gasoline of claim 15, wherein said hydrotreating catalyst is a bimetallic catalyst selected from the group consisting of Co/Mo, Co/W, Ni/Mo, Ni/W, Ti/Mo, Ti/W and combinations thereof. 19. The process for converting biomass to gasoline of claim 15, wherein said reaction occurs at an approximate temperature of 400° F., 425° F., 450° F., 475° F., 500° F., 525° F., 550° F., 575° F., 600° F., 625° F., 650° F., 675° F., 700° F., 725° F., 750° F., 775° F., 800° F., 825° F., 850° F., 875° F., or 900° F. 20. The process for converting biomass to gasoline of claim 15, wherein said reaction occurs at an approximate pressure of 500, 550, 600, 650, 700, 750, 800, 850, 900, 950, 1000, 1050, 1100, 1150, 1200, 1250, 1500, 1750, 2000, 2250, 2500, 2750, and 3000 psig. 21. The process for converting biomass to gasoline of claim 15, wherein said hydrotreating catalyst is an highly active catalyst selected from the group consisting of Co/Mo, Co/W, Ni/Mo, Ni/W, Ti/Mo, Ti/W, Co/Mo/W, Ni/Mo/W, Ti/Mo/W and combinations thereof.