Skeletal isomerization of alkyl esters and derivatives prepared therefrom
View Patent ↗The present invention relates to a process for the skeletal isomerization of unsaturated linear fatty acids to branched fatty acids which comprises contacting said unsaturated linear fatty acids with at least one large pore zeolite catalyst wherein said at least one zeolite catalyst comprises a material having a three dimensional channel structure having a pore diameter of at least 6.0 Å. In another embodiment, the invention relates to a process for the skeletal isomerization and hydrogenation of unsaturated linear fatty acids to saturated branched fatty acids which comprises contacting said unsaturated linear fatty acids in the presence of an acidic catalyst, wherein said acidic catalyst comprises a mesoporous crystalline phase having pore walls containing primary and secondary crystalline building unit structures.
1. A branched fatty acid or alkyl ester thereof prepared by isomerizing a feedstock which comprises unsaturated linear fatty acids, alkyl esters of unsaturated fatty acids or mixtures thereof, wherein said process comprises subjecting said feedstock to an isomerization reaction in the presence of an acidic catalyst having a three-dimensional channel pore structure wherein at least one channel structure has a pore size diameter of at least 6 Å, wherein said acidic catalyst is not loaded with metal ions.
2. The branched fatty acid or alkyl ester thereof of claim 1 wherein said acidic catalyst comprises a zeolite, acidic clay, molecular sieve, or mixtures thereof.
3. The branched fatty acid or alkyl ester thereof of claim 2 wherein said acidic catalyst comprises a zeolite.
4. The branched fatty acid or alkyl ester thereof of claim 3 wherein said zeolite comprises at least one of the following framework structures: CON, DFO, FAU, AFS, AFY, BEA, BPH, EMT, GME, or mixtures thereof.
5. The branched fatty acid or alkyl ester thereof of claim 4 wherein the SiO 2 /Al 2 O 3 ratio of the zeolite is at least 2.
6. The branched fatty acid or alkyl ester thereof of claim 5 wherein said zeolite contains at least one channel structure having a pore diameter of at least 6.5 Å.
7. The branched fatty acid or alkyl ester thereof of claim 6 wherein said zeolite contains at least one channel structure having a pore diameter of at least 7 Å.
8. The branched fatty acid or alkyl ester thereof according to claim 1 wherein the feedstock comprises of at least 50% by weight of unsaturated fatty acids, alkyl esters of unsaturated fatty acids or mixtures thereof.
9. The branched fatty acid or alkyl ester thereof claim 8 wherein at least part of the isomerization is performed at a temperature of between 100° C. and 350° C.
10. The branched fatty acid or alkyl ester thereof of claim 9 wherein the amount of catalyst used is between 0.5 and 20% by weight of the feedstock in the batch reactor.
11. The branched fatty acid or alkyl ester thereof of claim 4 wherein said zeolite having a three-dimensional pore structure comprises at least one pore structure containing 10-membered rings as catalysts.
12. A derivative prepared from the branched fatty acid or alkyl ester thereof of claim 1 wherein said derivative is selected from the group consisting essentially of amphoteric, non-ionic, anionic and cationic surfactants.
13. The derivative of claim 12 wherein said derivative is selected from the group consisting essentially of fatty acid glucamides, glycerol esters, polyhydric esters, sulfoesters, sucrose esters, alpha sulfonates, N-acyl sarcosinates, acylated protein hydrolysates, acyl isethionates, amido propyl amine and derivatives thereof, alkanolamide, ethoxylated alkanolamides, nitriles, N-aryl taurates, soaps, esteramines, esterquats, alkyl polyglycosides (APGs), alcohol sulfates, phosphate esters, polyalkoxycarbonates and mixtures thereof.
14. The branched fatty acid or alkyl ester thereof of claim 4 wherein the SiO 2 /Al 2 O 3 ratio of the zeolite is at least 10.