Method for co-production of aviation fuel and diesel
A process plant and a process for production of a hydrocarbon fraction suitable for use as jet fuel from a feedstock being a renewable feedstock or an oxygenate feedstock, including combining the feedstock with an amount of a hydrocracked intermediate product and optionally an additional liquid diluent, to form a combined feedstock, directing the combined feedstock to contact a material catalytically active in hydrodeoxygenation under hydrotreating conditions to provide a hydrodeoxygenated intermediate product, separating the hydrodeoxygenated intermediate product in at least two fractions; a vapor fraction and a liquid fraction, directing at least an amount of the liquid fraction to contact a material catalytically active in isomerization under isomerization conditions to provide an isomerized intermediate product, fractionating said isomerized intermediate product to provide at least a hydrocarbon suitable for use as jet fuel and a bottom fraction, hydrocracking the bottom fraction to provide the hydrocracked intermediate product.
1. A process for production of a hydrocarbon fraction suitable for use as jet fuel from an oxygenate feedstock, comprising the steps of
a. combining the feedstock with an amount of a hydrocracked intermediate product and optionally a liquid diluent to form a combined feedstock, directing said combined feedstock to contact a material catalytically active in hydrodeoxygenation under hydrotreating conditions to provide a hydrodeoxygenated intermediate product,
b. separating said hydrodeoxygenated intermediate product in at least two fractions including a vapor fraction and a liquid fraction,
c. optionally providing an amount of said liquid fraction as said liquid diluent, directing at least an amount of said liquid fraction to contact a material catalytically active in isomerization under isomerization conditions to provide an isomerized intermediate product,
d. fractionating said isomerized intermediate product to provide at least a hydrocarbon suitable for use as jet fuel and a bottom fraction,
directing at least an amount of said bottom fraction to contact a material catalytically active in hydrocracking under hydrocracking conditions to provide the hydrocracked intermediate product.
2. The process according to claim 1 , wherein said hydrocarbon fraction suitable for use as jet fuel has a final boiling point according to ASTM D86 being less than 300° C.
3. The process according to claim 1 , wherein the volume of hydrogen sulfide relative to the volume of molecular hydrogen in the gas phase of the combined feedstock directed to contact the material catalytically active in hydrodeoxygenation is at least 50 ppm v , optionally by adding a stream comprising one or more sulfur compounds.
4. The process according to claim 1 , wherein the volume of hydrogen sulfide relative to the volume of molecular hydrogen in the gas phase of the total stream directed to contact the material catalytically active in hydrocracking is at least 50 ppm v , optionally by adding a stream comprising one or more sulfur compounds.
5. The process according to claim 1 , wherein said feedstock comprises at least 50% wt triglycerides or fatty acids.
6. The process according to claim 1 , wherein hydrodeoxygenation conditions involve a temperature in the interval 250-400° C., a pressure in the interval 30-150 Bar, and a liquid hourly space velocity in the interval 0.1-2 and wherein the material catalytically active in hydrodeoxygenation comprises one or more sulfided metals taken from the group of nickel, cobalt, molybdenum or tungsten, supported on a carrier comprising one or more refractory oxides.
7. The process according to claim 1 , wherein hydrocracking conditions involve a temperature in the interval 250-425° C., a pressure in the interval 30-150 Bar, and a liquid hourly space velocity in the interval 0.5-4, optionally together with intermediate cooling by quenching with cold hydrogen, feed or product and wherein the material catalytically active in hydrocracking comprises (a) one or more active metals taken from the group platinum, palladium, nickel, cobalt, tungsten and molybdenum, (b) an acidic support taken from the group of a molecular sieve showing high cracking activity, and amorphous acidic oxides and (c) a refractory support.
8. The process according to claim 1 , wherein the amount of material boiling above 300° C. in said hydrocracked intermediate product is reduced by at least 20% wt compared to said bottom fraction.
9. The process according to claim 1 , wherein at least an amount of said isomerized intermediate product is directed to contact a material catalytically active in hydrodearomatization under hydrodearomatization conditions to provide a hydrodearomatized product comprising less than 1 wt/wt %, calculated by total mass of the aromatic molecules relative to all hydrocarbons in the stream.
10. The process according to claim 9 , wherein hydrodearomatization conditions involve a temperature in the interval 200-350° C., a pressure in the interval 30-150 Bar, and a liquid hourly space velocity in the interval 0.5-8 and wherein said material catalytically active in hydrodearomatization comprises an active metal taken from the group comprising platinum, palladium, nickel, cobalt, tungsten and molybdenum, and a refractory support.
11. The process according to claim 8 , wherein a hydrogen rich stream comprising at least 90% vol hydrogen is directed to contact the material catalytically active in hydrodearomatization.
12. The process according to claim 1 , wherein isomerization conditions involves a temperature in the interval 250-350° C., a pressure in the interval 30-150 Bar, and a liquid hourly space velocity in the interval 0.5-8 and wherein the material catalytically active in isomerization comprises an active metal taken from the group comprising platinum, palladium, nickel, cobalt, tungsten and molybdenum, an acidic support, and an amorphous refractory support comprising one or more oxides taken from the group comprising alumina, silica and titania or combinations thereof.
13. The process according to claim 1 , wherein
the material catalytically active in hydrodeoxygenation comprises one or more sulfided metals taken from the group of nickel, cobalt, molybdenum or tungsten, supported on a carrier comprising an amorphous refractory oxides,
the material catalytically active in isomerization comprises one or more elemental noble metals, a molecular sieve and an amorphous refractory support,
the material catalytically active in hydrocracking comprises one or more sulfided base metals such as nickel, cobalt, tungsten and/or molybdenum, an acidic support and a refractory support.