US2011056869A1PendingUtilityA1

Fuel production from feedstock containing lipidic material

Assignee: EXXONMOBIL RES & ENG COPriority: Sep 8, 2009Filed: Sep 3, 2010Published: Mar 10, 2011
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
PatentIndex Score
0
Cited by
0
References
0
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-modified
1 . 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

Track US2011056869A1 — get alerts on status changes and closely related new filings.

We store only your email — no account needed. See our privacy policy.