Production of biodiesel and glycerin from high free fatty acid feedstocks

• US 7,806,945 B2
• Filed: 01/26/2004
• Issued: 10/05/2010
• Est. Priority Date: 01/27/2003
• Status: Active Grant

• Current Assignee: REG Seneca LLC (Chevron Corp.), Komatsu Ltd.
• Original Assignee: Seneca Landlord, LLC (Chevron Corp.)
• Inventors: Jackam, John P, Fahrenbruck, Frank S, Pierce, Joel M
• Primary Examiner(s): Hill, Jr.; Robert J
• Assistant Examiner(s): MCCAIG, BRIAN A
• Application Number:
  US10/766,740
• Publication Number:
  US 20070277429A1
• Time in Patent Office: 2,444 Days
• Field of Search: 554/156, 554/157, 554/167, 554/175, 443/07, 443/08, 443/88
• US Class Current: 44/308
• CPC Class Codes: C10G 2300/1011 Biomass
• CPC Class Codes: C10L 1/19 Esters ester radical containing compounds; ester ethers; carbonic acid esters C10L1/1802, C10L1/1805, C10L1/1808, C10L1/1811, C10L1/1814, C10L1/1817 take precedence
• CPC Class Codes: C11C 3/003 by esterification of fatty acids with alcohols C11C3/02 takes precedence
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02P 30/20 using bio-feedstock

Abstract

A system and method for converting a high free fatty acid grease feedstock to biodiesel. The process comprises a glycerolysis reaction to convert free fatty acids to glycerides and a base catalyzed transesterification reaction to produce fatty acid methyl esters and glycerin in the absence of solvents. In preferred embodiments, both glycerin and methanol are recycled. The process can process a feedstock containing up to 100 percent free fatty acid content to produce biodiesel and glycerin with minimal waste generation.

Claims

1. A process for the production of purified biodiesel from a feedstock containing at least one fatty acid, the process comprising:

(A) converting the at least one fatty acid in the feedstock to a glyceride;

(B) reacting the glyceride with at least one alcohol to produce a fatty acid alkyl ester wherein the reaction is conducted in a transesterification reactor and further wherein the at least one alcohol is added to the transesterification reactor at a rate that is greater than the stoichiometric amount of alcohol required for transesterification; and

(C) separating the product of step (B) into a fatty acid alkyl ester rich stream and a glycerin rich stream; and

(D) purifying the fatty acid alkyl ester rich stream by distillation or fractionation to produce purified biodiesel having an acid number less than or equal to 0.80 mg KOH/g and total glycerin less than or equal to 0.240% mass without subjecting the fatty acid alkyl ester rich steam to water washing.

2. The process of claim 1, wherein step (A) comprises mixing the feedstock with glycerin for a time sufficient to convert the at least one fatty acid in the feedstock to a glyceride.

3. The process of claim 2, wherein the feedstock and glycerin is mixed at an elevated temperature in the absence of a catalyst.

4. The process of claim 2, wherein the glycerin is purified.

5. The process of claim 2, wherein the at least one fatty acid in the feedstock is converted to a glyceride by adding glycerin to the feedstock while mixing and subjecting the admixture to reduced pressure.

6. The process of claim 2, wherein the at least one fatty acid in the feedstock is converted to a glyceride in a glycerolysis reactor and further wherein glycerin is continuously added at a rate greater than the stoichiometric amount of glycerin required for glycerolysis.

7. The process of claim 6, wherein in step (A) glycerin is continuously added to the glycerolysis reactor at a rate in the range of about 110 percent to about 400 percent of the stoichiometric amount of glycerin required for glycerolysis.

8. The process of claim 1, wherein step (B) comprises reacting the glyceride with the at least one alcohol in the presence of an alkali catalyst to produce glycerin and the fatty acid alkyl ester.

9. The process of claim 1, wherein prior to step (A) the feedstock is conditioned to remove solids.

10. The process of claim 1, wherein the feedstock comprises at least one fatty acid at a concentration in the range of about 3 to about 97 percent by weight.

11. The process of claim 1, wherein in step (B) the alcohol is added at a rate equal to about 200 percent of the stoichiometric amount of alcohol required for transesterification.

12. The process of claim 1, wherein the process is continuous.

13. The process of claim 1, further comprising adjusting the pH of the glycerin rich stream by adding an acid solution thereto.

14. A process for the production of purified biodiesel from a feedstock containing at least one fatty acid, the process comprising:

(A) converting the at least one fatty acid in the feedstock to a glyceride;

(B) reacting the glyceride with at least one alcohol to produce a fatty acid alkyl ester wherein the reaction is conducted in a transesterification reactor and further wherein the at least one alcohol is added to the transesterification reactor at a rate that is greater than the stoichiometric amount of alcohol required for transesterification; and

(C) separating the product of step (B) into a fatty acid alkyl ester rich stream and a glycerin rich stream; and

(D) purifying the fatty acid alkyl ester rich stream by distillation or fractionation to produce purified biodiesel having an acid number less than or equal to 0.80 mg KOH/g and total glycerin less than or equal to 0.240% mass without subjecting the fatty acid alkyl ester rich stream to water washing;

wherein step (A) comprises mixing the feedstock with glycerin for a time sufficient to convert the at least one fatty acid in the feedstock to a glyceride;

wherein the feedstock and glycerin are reacted in at least two continuous stirred tank reactors.

15. The process of claim 14, wherein the at least two reactors have a combined residence time of not more than about 500 minutes.

16. A process for the production of purified biodiesel from a feedstock containing at least one fatty acid, the process comprising:

(A) converting the at least one fatty acid in the feedstock to a glyceride;

(B) reacting the glyceride with at least one alcohol to produce a fatty acid alkyl ester wherein the reaction is conducted in a transesterification reactor and further wherein the at least one alcohol is added to the transesterification reactor at a rate that is greater than the stoichiometric amount of alcohol required for transesterification; and

(C) separating the product of step (B) into a fatty acid alkyl ester rich stream and a glycerin rich stream; and

(D) purifying the fatty acid alkyl ester rich stream by distillation or fractionation to produce purified biodiesel having an acid number less than or equal to 0.80 mg KOH/g and total glycerin less than or equal to 0.240% mass without subjecting the fatty acid alkyl ester rich stream to water washing;

wherein the purified biodiesel produced in step (D) meets ASTM specification D 6751.

17. A process for the production of purified biodiesel from a feedstock containing at least one fatty acid, the process comprising:

(A) converting the at least one fatty acid in the feedstock to a glyceride;

(B) reacting the glyceride with at least one alcohol to produce a fatty acid alkyl ester wherein the reaction is conducted in a transesterification reactor and further wherein the at least one alcohol is added to the transesterification reactor at a rate that is greater than the stoichiometric amount of alcohol required for transesterification; and

(C) separating the product of step (B) into a fatty acid alkyl ester rich stream and a glycerin rich stream; and

(D) purifying the fatty acid alkyl ester rich stream by distillation or fractionation to produce purified biodiesel without subjecting the fatty acid alkyl ester rich steam to water washing.

18. The product produced by the process of claim 17.