High Fidelity Restriction Endonucleases
US-2024352437-A1 · Oct 24, 2024 · US
US10597645B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10597645-B2 |
| Application number | US-201616062519-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 16, 2016 |
| Priority date | Dec 22, 2015 |
| Publication date | Mar 24, 2020 |
| Grant date | Mar 24, 2020 |
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A process of recovering oil, comprising (a) converting a starch-containing material into dextrins with an alpha-amylase; (b) saccharifying the dextrins using a carbohydrate source generating enzyme to form a sugar; (c) fermenting the sugar in a fermentation medium into a fermentation product using a fermenting organism; (d) recovering the fermentation product to form a whole stillage; (e) separating the whole stillage into thin stillage and wet cake; (e′) optionally concentrating the thin stillage into syrup; (f) recovering oil from the thin stillage and/or optionally the syrup, wherein a protease and a phospholipase are present and/or added during steps (a) to (c). Use of a protease and a phospholipase for increasing oil recovery yields from thin stillage and/or syrup in a fermentation product production process.
Opening claim text (preview).
The invention claimed is: 1. A process of recovering oil, comprising (a) converting a starch-containing material into dextrins with an alpha-amylase; (b) saccharifying the dextrins using a carbohydrate source generating enzyme to form a sugar; (c) fermenting the sugar in a fermentation medium into a fermentation product using a fermenting organism; (d) recovering the fermentation product to form a whole stillage; (e) separating the whole stillage into thin stillage and wet cake; (e′) optionally concentrating the thin stillage into syrup; (f) recovering oil from the thin stillage and/or optionally the syrup, wherein a protease and a phospholipase are present and/or added during steps (a) to (c), wherein the protease present and/or added in steps (a) to (c) is: (i) a protease having the amino acid sequence set out in SEQ ID NO: 14 herein, or a protease which has at least 90% identity to SEQ ID NO: 14 having a protease activity; or (ii) a protease having the amino acid sequence set out in SEQ ID NO: 3 herein, or a protease which has at least 90% identity to SEQ ID NO: 3 having a protease activity. 2. The process of claim 1 , wherein the protease and the phospholipase are present and/or added during steps (b) and/or (c). 3. The process of claim 1 wherein the phospholipase present and/or added in steps (a) to (c) is a phospholipase C. 4. The process of claim 1 , wherein the phospholipase, present and/or added in steps (a) to (c) has the amino acid sequence of SEQ ID NO: 15 herein; SEQ ID NO: 16 herein; or SEQ ID NO: 17 herein, preferably where the phospholipase has the amino acid sequence of SEQ ID NO: 16 herein. 5. The process of claim 1 , wherein the phospholipase present and/or added in steps (a) to (c) (i) the phospholipase shown in SEQ ID NO: 15 herein or one having a sequence identity thereto of at least 90% having a phospholipase activity; or (ii) the phospholipase shown in SEC) ID NO: 16 herein or one having a sequence identity thereto of at least 90% having a phospholipase activity; or (iii) the phospholipase shown in SEC) ID NO: 17 herein or one having a sequence identity thereto of at least 90% having a phospholipase activity. 6. The process of claim 1 , wherein the protease and the phospholipase are added sequentially or simultaneously. 7. The process of claim 1 , wherein the step (a) is performed at a temperature above the initial gelatinization temperature. 8. The process of claim 1 , wherein the temperature in step (a) is above the initial gelatinization temperature. 9. The process of claim 7 wherein a protease is added in step (a) carried out above the initial gelatinization temperature. 10. The process of claim 7 , wherein the protease further comprises the one shown in SEQ ID NO: 4 herein, or wherein the protease has at least 90% identity SEQ ID NO: 4 having a protease activity. 11. The process of claim 7 , wherein the protease, added in step (a) carried out at a temperature above the initial gelatinization temperature, has: (i) a thermostability of more than 20%, more than 30%, more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, more than 105%, more than 110%, more than 115%, or more than 120% determined as Relative Activity at 80° C./70° C.; (ii) a thermostability between 50 and 115% determined as Relative Activity at 80° C./70° C.; or (iii) a thermostability of more than 12%, more than 14%, more than 16%, more than 18%, more than 20%, more than 25%, more than 30%, more than 40%, more than 50%, more than 60%, more than 70%, more than 80%, more than 90%, more than 100%, or more than 110% determined as Relative Activity at 85° C./70° C. 12. The process of claim 7 , wherein the bacterial alpha-amylase is from the genus Bacillus. 13. The process of claim 1 , wherein the step (a) is performed at a temperature below the initial gelatinization temperature. 14. The process of claim 13 , wherein: (i) saccharification step (b) and fermentation step (c) are carried out simultaneously or sequentially; or (ii) steps (a), (b) and (c) are carried out simultaneously or sequentially at a temperature below the initial gelatinization temperature. 15. The process of claim 12 , wherein the alpha-amylase is a Bacillus stearothermophilus alpha-amylase. 16. The process of claim 12 , wherein the alpha-amylase is a variant of the Bacillus stearothermophilus alpha-amylase shown in SEQ ID NO: 1 herein having at least 80%, at least 85%, at least 90%, at least 95%, at least 96%, at least 97%, at least 98%, or at least 99% sequence identity thereto. 17. The process of claim 12 , wherein the alpha-amylase is truncated. 18. The process of claim 17 , wherein the alpha-amylase is truncated to have from 485-495 amino acids. 19. The process of claim 17 , wherein the alpha-amylase is truncated to have around 491 amino acids.
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