Production of biodiesel from scum

Patent metadata

Field	Value
Publication number	US-9745530-B2
Application number	US-201615019707-A
Country	US
Kind code	B2
Filing date	Feb 9, 2016
Priority date	Feb 9, 2015
Publication date	Aug 29, 2017
Grant date	Aug 29, 2017

Abstract

A method for production of a biodiesel is described herein. The method for production of a biodiesel comprises (a) separating solids from a waste oil composition to provide a clarified oil composition; (b) acidifying the clarified oil composition to produce an acidified oil composition including free fatty acids derived from the waste oil; (c) converting at least a portion of the free fatty acids in the acidified oil composition to glycerides to provide a glyceride composition; and (d) reacting at least a portion of the glycerides in the glyceride composition with methanol to form fatty acid methyl ester to provide a biodiesel composition.

First claim

What is claimed is:

1. A method for production of a biodiesel comprising:
(a) separating solids from a waste oil composition to provide a clarified waste oil composition;
(b) acidifying the clarified waste oil composition to produce an acidified oil composition comprising free fatty acids derived from the waste oil composition;
(c) converting at least a portion of the free fatty acids in the acidified oil composition to glycerides to provide a glyceride composition; and
(d) reacting at least a portion of the glycerides in the glyceride composition with methanol to form fatty acid methyl esters to provide a biodiesel composition.

2. The method of claim 1 , wherein acidifying the clarified oil composition comprises contacting the clarified oil composition with an aqueous acid to provide an organic fraction comprising the free fatty acids derived from the clarified oil composition and an aqueous fraction.

3. The method of claim 2 , wherein the organic fraction comprises at least about 50 wt. % free fatty acids.

4. The method of claim 2 , wherein the organic fraction comprises at least about 70 wt. % free fatty acids.

5. The method of claim 2 , wherein acidifying the clarified oil composition further includes heating the clarified oil composition and the aqueous acid.

6. The method of claim 2 , wherein acidifying the clarified oil composition comprises contacting the clarified oil composition with the aqueous acid and an organic solvent to provide the organic fraction comprising free fatty acids and the aqueous fraction.

7. The method of claim 6 , further comprising separating at least a portion of the organic solvent from the organic fraction following contacting the clarified oil composition with the aqueous acid and the organic solvent to provide the acidified oil composition comprising free fatty acids derived from the waste oil.

8. The method of claim 7 , wherein separating at least the portion of the organic solvent comprises heating the organic fraction to a temperature of at least 15° C., exposing the organic fraction to a pressure of about 1 atm or less, or both.

9. The method of claim 6 , wherein the organic solvent is chosen from at least one of hexane, heptane, diethyl ether, ethyl acetate, and dichloromethane.

10. The method of claim 6 , wherein separating at least the portion of the organic solvent further includes recycling the separated portion of the organic solvent to be used for contact with the clarified scum.

11. The method of claim 1 , wherein converting at least a portion of the free fatty acids in the acidified oil composition to glycerides comprises esterification of the free fatty acids, transesterification of the free fatty acids, or both.

12. The method of claim 1 , wherein converting at least a portion of the free fatty acids in the acidified oil composition to glycerides comprises contacting the free fatty acids in the acidified oil composition with glycerol.

13. The method of claim 12 , wherein contacting the free fatty acids in the acidified oil composition with the glycerol is conducted at a temperature from about 175° C. to about 260° C.

14. The method of claim 1 , wherein reacting at least the portion of the glycerides in the glyceride composition with the methanol to form the fatty acid methyl esters is a base-catalyzed transesterification comprising contacting at least the portion of the glycerides and the methanol in the presence of a methoxide catalyst.

15. The method of claim 14 , wherein the methoxide catalyst is chosen from sodium methoxide, potassium methoxide, lithium methoxide, zinc methoxide, calcium methoxide, tributyltin methoxide, magnesium methoxide, tantalum(V) methoxide, titanium(IV) methoxide, antimony(III)methoxide, germanium methoxide, copper(II) methoxide, and combinations thereof.

16. The method of claim 1 , further comprising separating glycerol and methanol from the biodiesel composition.

17. The method of claim 16 , wherein separating the glycerol and the methanol from the biodiesel composition comprises (i) contacting the biodiesel composition with an acid to provide a salt of a methoxide catalyst; and
(ii) separating the glycerol, methanol, and the salt of the methoxide catalyst from the biodiesel composition.

18. The method of claim 1 , further comprising purifying the biodiesel composition with respect to the tatty acid methyl esters to produce a purified biodiesel composition.

19. The method of claim 18 , wherein purifying the biodiesel composition comprises distilling the biodiesel composition.

20. The method of claim 18 , further comprising the step of water washing and drying the purified biodiesel composition at a pressure of 1 atm or less.

Assignees

• Ruan Rongsheng
• Addy Min Min
• Nie Yong
• Anderson Erik Andrew
• Bi Chonghao
• Li Dong
• Chen Ling
• Univ Minnesota
• Univ China Agricultural

Inventors

• Ruan Rongsheng
• Addy Min Min
• Nie Yong
• Anderson Erik Andrew
• Bi Chonghao
• Li Dong
• Chen Ling

Classifications

• C11B13/00 Primary

  Recovery of fats, fatty oils or fatty acids from waste materials · CPC title

• C10L2290/543

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

• C11B3/04

  with acids · CPC title

• C10L2270/026

  for diesel engines, e.g. automobiles, stationary, marine · CPC title

• C10L1/08 Primary

  for compression ignition · CPC title