US2005136517A1PendingUtilityA1
Process for production of exopolysaccharides
Priority: Sep 7, 1999Filed: Feb 4, 2005Published: Jun 23, 2005
Est. expirySep 7, 2019(expired)· nominal 20-yr term from priority
C12P 19/06
46
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Claims
Abstract
The invention concerns a method for producing exopolysaccharides by fermenting micro-organisms characterised in that it consists in carrying out the fermentation in a nutrient medium comprising at least a source of carbon available to the micro-organisms and at least a source of nitrogen, said source being derived from a fraction of carob seed.
Claims
exact text as granted — not AI-modified1 - 16 . (canceled)
17 . A process for producing exopolysaccharides comprising a fermentation of microorganisms step, wherein the fermentation is carried out in a nutrient medium containing at least one carbon source assimilable by the microorganisms and at least one organic nitrogen source deriving from a carob bean.
18 . The process according to claim 17 , wherein the protein has a high content of arginine, of glutamine or glutamic acid, and of lysine.
19 . The process according to claim 17 , wherein the fraction of the carob bean has a content of lipids of at least 4% by weight with respect to the dry matter.
20 . The process according to claim 19 , wherein the content of lipids is of between 7 and 15%.
21 . The process according to claim 17 , wherein the fraction is a germ of the carob bean.
22 . The process according to claim 17 , wherein the carob bean fraction is in the form of a flour.
23 . The process according to claim 22 , wherein the flour has a granulometry of between 10 and 150 microns.
24 . The process according to claim 17 , wherein the nutrient medium further contains at least one inorganic nitrogen source.
25 . The process according to claim 24 , wherein the inorganic nitrogen source is an ammonium or sodium nitrate, an ammonium phosphate or sulfate, a magnesium sulfate, a potassium or sodium sulfate, or a mixture thereof.
26 . The process of claim 17 , wherein the organic and optionally inorganic nitrogen source in the fermentation medium is in a concentration of between 1 and 80 g/l.
27 . The process according to claim 26 , wherein the concentration of organic and optionally inorganic nitrogen source is of between 5 and 30 g/l.
28 . The process according to claim 17 , wherein the assimilable carbon source is a glucose or a sucrose.
29 . The process according to claim 17 , wherein the assimilable carbon source is a concentration of between 1 and 100 g/l.
30 . The process according to claim 29 , wherein the concentration of assimilable carbon source is of between 15 and 80 g/.
31 . The process according to claim 17 , wherein the fermentation of the microorganisms is carried out without an enzyme.
32 . The process according to claim 17 , wherein fermentation is carried out a temperature of between 15 and 100° C.
33 . The process according to claim 32 , wherein the temperature is of between 25 and 35° C.
34 . The process according to claim 17 , wherein the microorganism is selected from the group consisting of bacterias of the genus Xanthomonas , bacterias of the genus Alcaligenes , bacterias of the genus Agrobacterium , bacterias of the genus Arthrobacter , bacterias of the genus Azotobacter , bacterias of the genus Pseudomonas , bacterias of the genus Corynebacterium , bacterias of fungi of the genus Sclerotium , bacterias of the genus Aspergillus , and yeasts of the genus Hansenula.Cited by (0)
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