Methods of making 15-hydroxy fatty acid derivatives
The present disclosure provides methods of making 15-hydroxy fatty acid derivatives, such as 15-(S)-hydroxyeicosatrienoic acid (HETrE or 15-(S)-HETrE) or 15(S)-hydroxyeicosapentaenoic acid (HEPE or 15(S)-HEPE) from the corresponding fatty acid (e.g., dihomo-γ-linolenic acid (DGLA) or eicosapentaenoic acid (EPA), respectively). In some embodiments, the method comprises contacting the fatty acid with an oxidizing agent (e.g., a lipoxygenase and oxygen) in the presence of a reducing agent (e.g., cysteine) to form the 15-hydroxy fatty acid derivatives in a single reaction vessel.
1. A process for the production of a15-hydroxy derivative of a fatty acid comprising, oxidizing a fatty acid under an oxygen atmosphere of about 1.1 bar to about 4 bar to form a 15-hydroperoxy fatty acid intermediate and reducing at least a portion of the 15-hydroperoxy fatty acid intermediate using a reducing agent to form a 15-hydroxy derivative of the fatty acid.
2. The process according to claim 1 , wherein the step of oxidizing comprises contacting the fatty acid with less than 400 M units of enzyme per gram of the fatty acid.
3. The process according to claim 1 , producing yield of the 15-hydroxy derivative of the fatty acid of at least about 50%.
4. The process of claim 1 , wherein the 15-hydroxy derivative is 15(S)-HETrE.
5. The process of claim 1 , wherein the 15-hydroxy derivative is 15(S)-hydroxyeicosapentaenoic acid.
6. The process of claim 1 , wherein the reducing agent comprises cysteine.
7. The process of claim 1 , wherein the fatty acid comprises DGLA.
8. The process of claim 1 , wherein the fatty acid comprises a polyunsaturated fatty acid.
9. The process of claim 1 , wherein the 15-hydroxy derivative of the fatty acid has a purity not less than 95% wt/wt.
10. The process of claim 1 , wherein the batch size is not less than 100 kg.
11. The process of claim 1 , wherein the batch size is not less than 250 kg.
12. The process of claim 1 , wherein the batch size is not less than 500 kg.
13. The process of claim 1 , wherein the oxidizing comprises contacting the fatty acid with a soy flour extract.
14. The process of claim 13 further comprising:
contacting soy flour with a buffer solution at pH 4.5 to produce a crude soy flour extract; and
filtering the crude soy flour extract to produce the soy flour extract.
15. The process of claim 14 , wherein the soy flour extract has an activity comparable to about 2 mg/mL of purified, freeze-dried lipoxygenase enzyme.