Methods of refining natural oils and methods of producing fuel compositions
View Patent ↗A method of refining a natural oil includes: (a) providing a feedstock that includes a natural oil; (b) reacting the feedstock in the presence of a metathesis catalyst to form a metathesized product that includes olefins and esters; (c) passivating residual metathesis catalyst with an agent selected from the group consisting of phosphorous acid, phosphinic acid, and a combination thereof; (d) separating the olefins in the metathesized product from the esters in the metathesized product; and (e) transesterifying the esters in the presence of an alcohol to form a transesterified product and/or hydrogenating the olefins to form a fully or partially saturated hydrogenated product. Methods for suppressing isomerization of olefin metathesis products produced in a metathesis reaction, and methods of producing fuel compositions are described.
1. A method of refining a natural oil comprising:
providing a feedstock comprising a natural oil;
reacting the feedstock in the presence of a metathesis catalyst to form a metathesized product comprising olefins, esters and residual metathesis catalyst;
treating the residual metathesis catalyst in the metathesis product with an isomerization suppression agent selected from the group consisting of phosphorous acid, phosphinic acid, and a combination thereof, to passivate at least a portion of the residual metathesis catalyst;
separating the olefins in the metathesized product from the esters in the metathesized product; and
transesterifying the esters in the presence of an alcohol to form a transesterified product.
2. The method of claim 1 wherein the natural oil is selected from the group consisting of canola oil, rapeseed oil, coconut oil, corn oil, cottonseed oil, olive oil, palm oil, peanut oil, safflower oil, sesame oil, soybean oil, sunflower oil, linseed oil, palm kernel oil, tung oil, jatropha oil, mustard oil, camelina oil, pennycress oil, hemp oil, algal oil, castor oil, lard, tallow, poultry fat, yellow grease, fish oil, tall oils, and combinations thereof.
3. The method of claim 1 wherein the residual metathesis catalyst comprises ruthenium.
4. The method of claim 1 wherein treating comprises treating the residual metathesis catalyst in the metathesis product with phosphorous acid.
5. The method of claim 1 wherein treating comprises treating the residual metathesis catalyst in the metathesis product with phosphinic acid.
6. The method of claim 1 , further comprising: separating glycerin from the transesterified product through a liquid-liquid separation; washing the transesterified product with water after separating the glycerin to further remove the glycerin; and drying the transesterified product after the washing to separate the water from the transesterified product.
7. The method of claim 6 further comprising distilling the transesterified product to separate a specialty chemical selected from the group consisting of an ester of 9-decenoic acid, an ester of 9-undecenoic acid, an ester of 9-dodecenoic acid, and combinations thereof.
8. The method of claim 7 further comprising hydrolyzing the specialty chemical, thereby forming an acid selected from the group consisting of: 9-decenoic acid, 9-undecenoic acid, 9-dodecenonic acid, and combinations thereof.
9. The method of claim 1 further comprising reacting the transesterified product with itself to form a dimer.
10. The method of claim 1 wherein the reacting comprises self-metathesis of the natural oil.
11. The method of claim 1 wherein the feedstock further comprises a low-molecular-weight olefin.
12. The method of claim 11 wherein the reacting comprises cross-metathesis between the natural oil and the low-molecular-weight olefin.
13. The method of claim 12 wherein the low-molecular-weight olefin comprises a material selected from the group consisting of ethylene, propylene, 1-butene, and combinations thereof.
14. The method of claim 12 wherein the low-molecular-weight olefin comprises at least one branched olefin having a carbon number between 4 and 10.
15. A method of producing a fuel composition comprising:
providing a feedstock comprising a natural oil;
reacting the feedstock in the presence of a metathesis catalyst to form a metathesized product comprising olefins, esters and residual metathesis catalyst;
treating the residual metathesis catalyst in the metathesized product with an isomerization suppression agent selected from the group consisting of phosphorous acid, phosphinic acid, and a combination thereof, to passivate at least a portion of the residual metathesis catalyst;
separating the olefins in the metathesized product from the esters in the metathesized product; and
hydrogenating the olefins to form a fuel composition.
16. The method of claim 15 wherein the fuel composition is (a) a kerosene jet fuel having a carbon number distribution between 8 and 16, a flash point between about 38° C. and about 66° C., an auto ignition temperature of about 210° C., and a freeze point between about −47° C. and about −40° C.; (b) a naphtha jet fuel having a carbon number distribution between 5 and 15, a flash point between about −23° C. and about 0° C., an auto ignition temperature of about 250° C.; and a freeze point of about −65° C.; or (c) a diesel fuel having a carbon number distribution between 8 and 25, a specific gravity of between about 0.82 and about 1.08 at about 15.6° C., a cetane number of greater than about 40, and a distillation range between about 180° C. and about 340° C.
17. The method of claim 15 further comprising flash-separating a light end stream from the metathesized product prior to separating the olefins from the esters, wherein the light end stream comprises a majority of hydrocarbons with carbon numbers between 2 and 4.
18. The method of claim 15 further comprising separating a light end stream from the olefins prior to hydrogenating the olefins, wherein the light end stream comprises a majority of hydrocarbons with carbon numbers between 3 and 8.
19. The method of claim 15 further comprising separating a C 18+ heavy end stream from the olefins prior to hydrogenating the olefins, wherein the heavy end stream comprises a majority of hydrocarbons with carbon numbers of at least 18.
20. The method of claim 15 further comprising separating a C 18+ heavy end stream from the fuel composition, wherein the heavy end stream comprises a majority of hydrocarbons with carbon numbers of at least 18.
21. The method of claim 15 further comprising isomerizing the fuel composition, wherein a fraction of normal-paraffin compounds in the fuel composition are isomerized into iso-paraffin compounds.
22. The method of claim 15 wherein the reacting comprises self-metathesis of the natural oil.
23. The method of claim 15 wherein the feedstock further comprises a low-molecular-weight olefin and the reacting comprises cross-metathesis between the natural oil and the low-molecular-weight olefin.