US2011056869A1PendingUtilityA1
Fuel production from feedstock containing lipidic material
Est. expirySep 8, 2029(~3.1 yrs left)· nominal 20-yr term from priority
C10G 3/45C10G 65/043C10L 1/026C10G 3/50C10G 2400/08C10G 2300/1018C10G 2300/1014C10G 3/48C10G 2400/04Y02P30/20C10G 65/12C10G 3/46C10G 2300/301C10G 45/58
40
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Claims
Abstract
This invention relates to the production of dewaxed and/or hydroisomerized fuel composition that includes a step of hydrotreating a feedstock containing the lipidic material. The fuel compositions are high quality fuel compositions in which the fuel can be ultimately tailored for a variety of end uses such as jet fuel or diesel fuel.
Claims
exact text as granted — not AI-modified1 . A method for producing a dewaxed fuel composition comprising:
providing a feedstock containing lipidic biomass; hydrotreating the feedstock to produce a hydrotreated material; and dewaxing at least a portion of the hydrotreated material to produce the dewaxed fuel composition.
2 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is recovered as jet fuel or diesel fuel.
3 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is recovered as jet fuel having a smoke point of at least 25.0 mm.
4 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is recovered as jet fuel having a freeze point of not higher than −35° C.
5 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is recovered as jet fuel having an ASTM D86 90% distillation point within the range of from 250° C. to 290° C.
6 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is recovered as jet fuel having an ASTM D86 90% distillation point within the range of from 200° C. to 240° C.
7 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is recovered as diesel fuel having an ASTM D86 90% distillation point within the range of from 260° C. to 350° C.
8 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is distilled and at least one jet fuel or at least one diesel fuel is recovered following distillation.
9 . The method of claim 1 , wherein at least a portion of the dewaxed fuel composition is hydroisomerized to produce a hydroisomerized composition and at least a portion of the hydroisomerized composition is recovered as jet fuel or diesel fuel.
10 . The method of claim 1 , wherein the feedstock further comprises mineral oil.
11 . A method for producing a hydroisomerized fuel composition comprising:
providing a feedstock containing lipidic biomass; hydrotreating the feedstock to produce a hydrotreated material; and hydroisomerizing at least a portion of the hydrotreated material to produce the hydroisomerized fuel composition.
12 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is recovered as jet fuel or diesel fuel.
13 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is recovered as jet fuel having a smoke point of at least 25.0 mm.
14 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is recovered as jet fuel having a freeze point of not higher than −35° C.
15 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is recovered as jet fuel having an ASTM D86 90% distillation point within the range of from 250° C. to 290° C.
16 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is recovered as jet fuel having an ASTM D86 90% distillation point within the range of from 200° C. to 240° C.
17 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is recovered as diesel fuel having an ASTM D86 90% distillation point within the range of from 260° C. to 350° C.
18 . The method of claim 11 , wherein at least a portion of the hydroisomerized fuel composition is distilled and at least one jet fuel or at least one diesel fuel is recovered following distillation.
19 . The method of claim 11 , wherein the feedstock further comprises mineral oil.
20 . A method for producing a hydroisomerized fuel composition comprising:
providing a feedstock containing lipidic biomass; hydrotreating the feedstock to produce a hydrotreated material; dewaxing at least a portion of the hydrotreated material to produce a dewaxed fuel composition; and hydroisomerizing at least a portion of the dewaxed fuel composition to produce the hydroisomerized fuel composition.Join the waitlist — get patent alerts
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