Process for converting fats, oils and greases into fuels

Patent metadata

Field	Value
Publication number	US-9701911-B2
Application number	US-201314441665-A
Country	US
Kind code	B2
Filing date	Nov 8, 2013
Priority date	Nov 9, 2012
Publication date	Jul 11, 2017
Grant date	Jul 11, 2017

Abstract

A method for producing a light oil fraction from plant-based and/or animal-based fats, oils or greases is disclosed. The method comprises introducing a feedstock including free fatty acids into a processing system. The system is heated at a controlled rate to a specified temperature, both of which are selected to produce a light oil fraction with a reduced fatty acid content. The system is permitted to reflux for a predetermined time, during which more of the light oil fraction is produced. The light oil fraction is separated from the remainder of the feedstock and contains less than 10% free fatty acids.

First claim

What is claimed is:

1. A method for producing a light oil fraction with low fatty acids from plant-based and/or animal-based fats, oils or greases, the method comprising:
introducing a feedstock comprising free fatty acids into a processing system;
heating the feedstock at a predetermined rate to a predetermined temperature, the predetermined rate selected to produce a light oil fraction with a reduced fatty acid content;
permitting the feedstock to reflux by reacting the feedstock under a cracking reaction and a decarboxylation reaction at the predetermined temperature for a predetermined time, wherein the predetermined time is selected to produce the light oil fraction with the reduced fatty acid content;
separating the light oil fraction from the remainder of the feedstock, wherein the separated light oil fraction contains less than 10% free fatty acids;
wherein the predetermined temperature is at least 300° C., and the predetermined rate is less than 70° C. per hour.

2. The method of claim 1 , further comprising drying the feedstock prior to the step of introducing, such that the feedstock has less than about 0.5 percent water.

3. The method of claim 1 , wherein the feedstock has less than about 0.1 percent water.

4. The method of claim 2 , wherein the step of drying comprises heating the feedstock while under a pressure of less than 1 atmosphere to remove water.

5. The method of claim 1 , wherein the light oil fraction contains less than 1% free fatty acids.

6. The method of claim 1 , wherein the feedstock comprises at least one of a virgin oil, an animal fat, a yellow grease, or a brown grease.

7. The method of claim 1 , wherein the feedstock comprises at least one oil selected from the group consisting of corn oil, oil from algae, oil from bacteria, oil from seaweeds and combinations thereof.

8. The method of claim 1 , wherein the step of separating the light oil fraction from the remainder of the feedstock comprises condensing the light oil fraction.

9. The method of claim 1 , wherein the feedstock has a feedstock mass and more than about 20% of the feedstock mass is converted to the light oil fraction within about 10 hours to about 24 hours of starting the step of permitting the feedstock to reflux.

10. The method of claim 1 , wherein the feedstock has a feedstock mass and more than about 40% of the feedstock mass is converted to the light oil fraction within about 10 hours to about 24 hours of starting the step of permitting the feedstock to reflux.

11. The method of claim 1 , wherein the feedstock has a feedstock mass and more than about 30% of the feedstock mass is converted to the light oil fraction within about 6 hours of starting the step of permitting the feedstock to reflux.

12. The method of claim 1 , wherein the feedstock has a feedstock mass and more than about 60% of the feedstock mass is converted to the light oil fraction within about 30 hours of starting the step of permitting the feedstock to reflux.

13. The method of claim 1 , wherein the predetermined temperature is between 300° C. and 400° C.

14. The method of claim 1 , wherein the light oil fraction is separated from the reacting mixture by use of a vapor/liquid separator that:
cools vapor rising from the reacting mixture to a temperature below 250° C.; returns condensed liquid to the processing system; and
allows uncondensed components of the vapor that was cooled to a temperature below 250° C. to pass through a cooling element of the vapor/liquid separator and the uncondensed components, after being exposed to condensation conditions, comprise the light oil fraction.

15. The method of claim 1 , wherein the processing system is catalyst-free.

16. The method of claim 1 , further comprising adding at least one catalyst to the processing system.

17. The method of claim 1 , wherein the predetermined rate is constant throughout the step of heating the feedstock.

18. The method of claim 1 , further comprising extracting the feedstock from a biological organism.

19. The method of claim 1 , wherein the feedstock consists essentially of fatty acids and triglycerides.

Assignees

• Univ City New York Res Found
• Univ Connecticut

Inventors

• Pratt Lawrence M
• Parnas Richard Steven

Classifications

• C10L1/02

  essentially based on components consisting of carbon, hydrogen, and oxygen only · CPC title

• C10L2200/0469

  Renewables or materials of biological origin · CPC title

• C10G3/40 Primary

  Thermal non-catalytic treatment · CPC title

• C10L2290/543

  Distillation, fractionation or rectification for separating fractions, components or impurities during preparation or upgrading of a fuel · CPC title

• Y02P30/20

  using bio-feedstock · CPC title