Production of polyunsaturated fatty acids using cell treatment method
A method for isolating one compound or more than one compound from a biomass which contains microorganisms that have produced the compound or compounds, the method comprising the following steps: (a) preparing or obtaining wet cells having an average moisture content of between 30% and 80%; (b) subjecting the wet cells to primary drying to obtain primary dried cells having an average moisture content of between 5% and 50%; (c) subjecting the primary dried cells obtained in (b) to secondary drying to obtain secondary dried cells having an average moisture content of no greater than 10%; and (d) extracting or isolating, purifying and/or refining the compound or each of the compounds from the secondary dried cells obtained in (c).
1. A method for isolating one compound or more than one compound from a microbial biomass which contains microorganisms that have produced the compound or compounds, the method comprising the following steps:
(a) preparing or obtaining wet cells having an average moisture content of between 30% and 80%;
(b) subjecting the wet cells to primary drying to obtain primary dried cells having an average moisture content of between 5% and 50%, wherein the primary drying is accomplished with a conduction heating system of a thermal adhesion conveyor drier;
(c) subjecting the primary dried cells obtained in (b) to secondary drying to obtain secondary dried cells having an average moisture content of no greater than 10%, wherein the secondary drying is accomplished with a convection heating system; and
(d) extracting, isolating, purifying and/or refining the compound or each of the compounds from the secondary dried cells obtained in (c),
wherein said compound or each of the compounds is a triglyceride and/or phospholipid comprising a polyunsaturated fatty acid as a constituent fatty acid.
2. The method according to claim 1 , wherein said thermal adhesion conveyor drier is a double drum drier.
3. The method according to claim 1 , wherein said convection heating system is a vibrating fluidized bed drier, a horizontal continuous fluidized bed drier, a rotary drier, a box-type parallel flow drier, a box-type air flow drier, a vibrating drier/cooler, a fluidized bed drier, a band-type air flow drier, or a band drier.
4. The method according to claim 1 , wherein the wet cells in (a) are obtained by solid/liquid separation of a culturing solution.
5. The method according to claim 4 , wherein said solid/liquid separation is carried out simultaneously with mechanical dehydration.
6. The method according to claim 1 , wherein said biomass contains a fungus or is derived from a fungus.
7. The method according to claim 6 , wherein said fungus belongs to the order Mucorales.
8. The method according to claim 6 , wherein said fungus belongs to the genus Mortierella.
9. The method according to claim 6 , wherein said fungus is Mortierella alpina.
10. The method according to claim 1 , wherein said biomass contains an alga or is derived from an alga.
11. The method according to claim 10 , wherein said alga belongs to the genus Crypthecodinium, Thraustochytrium , Schizochytrium, Ulkenia, Japonochytrium or Haliphthoros.
12. The method according to claim 10 , wherein said alga is Crypthecodinium cohnii.
13. The method according to claim 1 , wherein said polyunsaturated fatty acid is a C18 or greater ω3, 107 6 and/or ω9 fatty acid having two or more double bonds.
14. The method according to claim 1 , wherein said polyunsaturated fatty acid is α-linolenic acid (9,12,15-octadecatrienoic acid), 6,9,12,15-octadecatetraenoic acid (18:4ω3), 8,11,14,17-eicosatetraenoic acid (20:4ω3), EPA (5,8,11,14,17-eicosapentaenoic acid), DPAω3 (7,10,13,16,19-docosapentaenoic acid), DHA (4,7,10,13,16,19-docosahexaenoic acid), γ-linolenic acid (6,9,12-octadecatrienoic acid), dihomo-γ-linolenic acid (8,11,14-eicosatrienoic acid), arachidonic acid (5,8,11,14-eicosatetraenoic acid), 7,10,13,16-docosatetraenoic acid (22:4 ω6), DPAω6 (4,7,10,13,16-docosapentaenoic acid), 6,9-octadecadienoic acid (18:2ω9), 8,11-eicosadienoic acid (20:2ω9) and/or Mead acid (5,8,11-eicosatrienoic acid).
15. The method according to claim 1 , characterized in that the secondary dried cells obtained in step (c) are supplied to step (d) after cooling treatment by one of the following methods:
(i) cooling to at least 60° C. by supplying air having a composition with an oxygen concentration of no greater than 21%; or
(ii) cooling to at least 60° C. by static cooling in an atmosphere of air having a composition with an oxygen concentration of no greater than 21%.
16. A method for obtaining one compound or more than one compound from dried cells containing a biomass of microorganisms that have produced the compound or compounds, the method comprising the following steps:
(a) preparing or obtaining wet cells having an average moisture content of between 30% and 80%;
(b) subjecting the wet cells to primary drying to obtain primary dried cells having an average moisture content of between 5% and 50%, wherein the primary drying is accomplished with a conduction heating system of a thermal adhesion conveyor drier; and
(c) subjecting the primary dried cells obtained in (b) to secondary drying to obtain secondary dried cells having an average moisture content of no greater than 10%, wherein the secondary drying is accomplished with a convection heating system,
wherein the compound or each of the compounds is a triglyceride and/or phospholipid comprising a polyunsaturated fatty acid as a constituent fatty acid.
17. A method for storing dried cells comprising a microbial biomass containing a microorganism which has produced one compound or more than one compound, wherein
(1) dried cells are obtained by the following steps:
(a) preparing or obtaining wet cells having an average moisture content of between 30% and 80%;
(b) subjecting the wet cells to primary drying to obtain primary dried cells having an average moisture content of between 5% and 50%, wherein the primary drying is accomplished with a conduction heating system of a thermal adhesion conveyor drier;
(c) subjecting the primary dried cells obtained in (b) to secondary drying to obtain secondary dried cells having an average moisture content of no greater than 10%, wherein the secondary drying is accomplished with a convection heating system; and then
(2) the obtained secondary dried cells are subjected to cooling treatment by one of the following methods:
(i) cooling to at least 60° C. by supplying air having a composition with an oxygen concentration of no greater than 21%; or
(ii) cooling to at least 60° C. by static cooling in an atmosphere of air having a composition with an oxygen concentration of no greater than 21%; and
(3) the cooled secondary dried cells are stored by one of the following methods:
(I) filling said cells into a sealable container together with nitrogen gas and storing them at 15° C. or below; or
(II) filling said cells into a sealable container together with air having an oxygen concentration of no greater than 20%, and storing them at 15° C. or below,
wherein said compound or each of the compounds is a triglyceride and/or phospholipid comprising a polyunsaturated fatty acid as a constituent fatty acid.