Biodiesel purification by a continuous regenerable adsorbent process
A quick, economical and environmentally friendly, “green”, process for the continuous purification of biodiesel (fatty acid alkyl esters (FAAE)) is described using a powdered, granulated or extruded adsorbent. The adsorbent is contained in a column system and is regenerated for reuse multiple times. The process employs an adsorbent such as, but not limited to, carbon, silica, clay, zeolite or a metal silicate contained in a column to remove the impurities from fatty acid alkyl esters (FAAE) or crude biodiesel in a continuous process. The process utilizes the adsorbent column system for the purification of biodiesel, rather than water or filtration, to remove soaps and other impurities entrained in a crude biodiesel. The crude biodiesel is contacted with an adsorbent packed into a column, or multiple columns in series, for a sufficient amount of time to remove impurities such as, but not limited to, soaps, metals, free glycerin, sterol glucosides and many of the other impurities that reduce the stability of biodiesel. The resulting finished biodiesel exiting the column(s) is ready for the methanol recovery process. Once the adsorbent no longer removes the desired amount of impurities, it is regenerated for reuse. The solvent used for the regeneration process is reclaimed and reused by recycling it back to the transesterification reaction.
1. A process for purification of fatty acid alkyl esters (FAAE) comprising:
(a) treating fatty acid alkyl esters (FAAE) utilizing one or more adsorbent columns containing an adsorbent material for removing one or more impurities from the fatty acid alkyl esters (FAAE) and said fatty acid alkyl esters (FAAE) continuously flow through said one or more columns;
(b) regenerating the adsorbent material with an acidic alcohol for removing adsorbed impurities from the adsorbent material, and
(c) re-using the regenerated adsorbent material in step (a);
wherein said impurities are selected from one or more of soap, metals, free glycerin, sterol glycosides, and free fatty acids (FFA).
2. The process of claim 1 wherein the adsorbent material is a powder or is granulated.
3. The process of claim 1 wherein the adsorbent material is selected from carbon, silica, zeolite, metal silicate, bleaching clay, and activated bleaching clay.
4. The process of claim 1 wherein the adsorbent material is synthetic magnesium silicate.
5. The process of claim 1 wherein the fatty acid alkyl esters (FAAE) is crude biodiesel.
6. The process of claim 1 wherein the alcohol is methanol.
7. The process of claim 1 wherein the acid is sulfuric acid, citric acid, or malic acid.
8. The process of claim 1 wherein the amount of acid added to the alcohol is about 0.005% to about 3.00% by weight.
9. The process of claim 1 wherein after the step of regenerating the adsorbent material, further comprising the step of directly esterfying the FFA in the solvent filtrate using an acid as a catalyst.
10. The process of claim 9 wherein the acid is sulfuric acid.
11. The process of claim 9 wherein the fatty acid alkyl esters (FAAE) produced by the esterification step are reclaimed.
12. The process of claim 10 wherein the reclamation comprises separating glycerin and/or impurities from the alcohol and the biodiesel and recycling the alcohol and the biodiesel to be used directly in a transesterification reaction.
13. The process of claim 11 wherein the separated glycerin and/or impurities from the reclamation are added to glycerin and/or impurities from the transesterification reaction.
14. The process of claim 1 further comprising the step of:
pre-treating the fatty acid alkyl esters (FAAE) in one or more columns containing an ion-exchange resin before entering a lead column of said one or more adsorbent columns.
15. The process of claim 14 wherein the ion-exchange resin is cationic.
16. The process of claim 14 further comprising the steps of regenerating said ion-exchange resin thereby providing reuse of the ion-exchange resin.
17. The process of claim 16 wherein the step of regenerating the ion-exchange resin is performed with a solvent.
18. The process of claim 17 wherein the solvent is an alcohol.
19. The process of claim 17 wherein the alcohol is methanol.
20. The process of claim 16 wherein after the step of regenerating the ion-exchange resin further comprises the step of separating glycerin from the alcohol and residual FAAE and recycling the alcohol and residual FAAE to be used directly in a transesterification reaction.
21. The process of claim 20 wherein the glycerin from the separation process is added to glycerin and/or impurities from the transesterification process.