Production of biodiesel fuels which are low in glycerin and sulfur
The present invention relates to a process and apparatus for the production of carboxylic acid esters and/or biodiesel fuel from feedstocks containing fatty acids, glycerated fatty acids, and glycerin by reactive distillation. Specifically, in one embodiment, the present invention relates to the production of biodiesel fuels having low glycerin, water, and sulfur content on an industrial scale.
1. An esterification process for preparing biodiesel from a fatty acid feedstream, the esterification process comprising:
a) continuously introducing an alcohol vapor feedstream to a reaction vessel;
b) continuously introducing the fatty acid feedstream to the reaction vessel;
c) catalytically esterifying the alcohol vapor and fatty acid in a reaction zone within the reaction vessel to produce a fatty acid alkyl ester product stream and water, said reaction zone containing a heterogeneous catalyst;
d) stripping said water from the reaction vessel with the alcohol vapor;
e) separating the water from the alcohol vapor and recycling said alcohol to the reaction vessel;
f) converting the fatty acid alkyl ester product stream into a biodiesel meeting or exceeding biodiesel standard ASTM D6751, wherein said converting comprises removing impurities from said fatty acid alkyl ester product stream by at least one purification process selected from the group consisting of distillation, reboiled stripping, inert gas stripping, physical adsorption, and gravity separation.
2. The process of claim 1 , wherein the fatty acid alkyl ester product stream comprises fatty acid methyl ester.
3. The process of claim 1 , wherein the biodiesel contains from 0 to about 0.25% by weight total glycerin.
4. The process of claim 1 , wherein the biodiesel contains from 0 to about 500 ppm sulfur.
5. The process of claim 1 , wherein the fatty acid feedstream is the product of introducing a triglyceride feedstock into a fat splitter to produce a fatty-acid rich feedstream.
6. The process of claim 1 , wherein the reaction zone includes an ion exchange resin catalyst with —SO 3 H or —CO 2 H functional groups.
7. The process of claim 1 , wherein the heterogeneous catalyst is present in structured packing.
8. The process of claim 1 , wherein the alcohol is methanol.
9. The process of claim 1 , further comprising pre-esterification of the fatty acid feedstream prior to introduction of the fatty acid feedstream into the reaction vessel.
10. The process of claim 1 , wherein the biodiesel comprises a water content of less than 0.050% by volume.
11. The process of claim 1 , wherein the biodiesel comprises a kinematic viscosity of between 1.9 and 6 mm 2 /s.
12. The process of claim 1 , wherein the biodiesel comprises a cetane number greater than 47.
13. The process of claim 1 , wherein the biodiesel comprises a total glycerin content of less than 0.20% by weight.
14. The process of claim 1 , wherein the heterogeneous catalyst is present in a plurality of trays mounted one above the other.
15. The process of claim 1 , wherein the biodiesel comprises a cloud point of less than −20° C.
16. The process of claim 1 , wherein the biodiesel comprises a cloud point of less than −40° C.
17. The process of claim 1 , wherein said fatty acid feedstock comprises one or more fatty acids selected from the group consisting of decanoic acid, dodecanoic acid, tetradecanoic acid, hexadecanoic acid, octadecanoic adic, octadecenoic acid, linoleic acid, eicosanoic acid, and isostearic acid.
18. The process of claim 1 , wherein the fatty acid feedstock comprises 99% or greater fatty acids.