METHODS AND SYSTEMS OF PRODUCING NUTRITIONAL SUPPLEMENT FROM MICROBIAL CELLS
A method of producing a nutritional supplement from microbial cells. The method includes cultivating microbial cells to obtain a biomass; incubating the biomass with a heat treatment at temperature from 55° C. up to 80° C. for an incubation time from 10 minutes up to 60 minutes; concentrating the biomass by separating and removing a liquid phase from a solid phase to obtain a dry matter content from 2% up to 40% of total weight of the nutritional supplement. Disclosed also is a system of producing a nutritional supplement from microbial cells using the aforementioned method. The system includes a bioreactor; a heat-exchanger and a separator for carrying out the respective steps of the aforementioned method. Reference is made to the Identification of the Microorganism, with the identification reference given by the Depositor SoF1, having the Accession number given by the INTERNATIONAL DEPOSITORY AUTHORITY, VTT E-193585, received on Jun. 11, 2019
1 . A method of producing a nutritional supplement from microbial cells, the method comprising:
cultivating the microbial cells to obtain a biomass comprising gram-negative bacteria;
incubating the biomass for at least partially degrading walls of the microbial cells with a heat treatment at temperature from 55° C. up to 80° C. for an incubation time from 10 minutes up to 60 minutes;
concentrating the incubated biomass by separating and removing a liquid phase from a solid phase to obtain a dry matter content from 2% up to 40% of total weight of the nutritional supplement; and
homogenizing the nutritional supplement with high-pressure homogenization at least one run for at least partially degrading the walls of the microbial cells.
2 . A method according to claim 1 , wherein the dry matter content is
from 5% up to 30%, or
preferably from 8% up to 25%
of total weight of the nutritional supplement.
3 . A method according to claim 1 further comprising drying the nutritional supplement to obtain dry matter content from 94% up to 99% of the total weight of the microbial product.
4 . A method according to claim 1 , wherein the incubation temperature is
from 55° C. up to 70° C., or
preferably from 60° C. up to 68° C.; and
the incubation time is
from 15 minutes up to 40 minutes, or
preferably from 20 minutes up to 30 minutes.
5 . A method according to claim 3 further comprising extruding the nutritional supplement with high-moisture extrusion.
6 . A method according to claim 1 , wherein the homogenizing is carried out at pressure
from 800 bars up to 2000 bars, or
preferably from 900 bars up to 1000 bars.
7 . A method according to claim 1 , wherein the separating is carried out with a separation method selected from at least one of a centrifugation, a filtration.
8 . A method according to claim 3 , wherein the drying is selected as at least one of a drum drying or a spray drying and drying temperature is from 120° C. up to 180° C.
9 . A method according to claim 1 , wherein the microbial cells comprise isolated bacterial strain deposited as VTT-E-193585 or a derivative thereof.
10 . A system for producing a nutritional supplement from microbial cells, the system comprising:
a bioreactor for cultivating the microbial cells to obtain a biomass comprising gram-negative bacteria;
a heat-exchanger having incubation temperature from 55° C. up to 80° C. and incubation time from 10 minutes up to 60 minutes for partially degrading walls of the microbial cells;
a separator for separating a solid phase and a liquid phase to obtain a dry matter content from 2% up to 40% of total weight of the nutritional supplement; and
a high-pressure homogenizer for at least partially degrading the walls of the microbial cells of the nutritional supplement.
11 . A system according to claim 10 further comprising a dryer to obtain a dry matter content from 94% up to 99% of the total weight of the nutritional supplement.
12 . A system according to claim 11 further comprising an extruder for extruding the microbial product with high-moisture extrusion.
13 . A system according to claim 10 , wherein the heat-exchanger is selected to be at least one of a tank heat-exchanger, a tubular heat-exchanger, or a plate heat-exchanger.
14 . A system according to claim 10 , wherein the pressure in the high-pressure homogenizer is from 800 bars up to 2000 bars or preferably from 900 bars up to 1000 bars.
15 . A system according to claim 10 , wherein the separator is selected to be at least one of a centrifugal separator, a filter.
16 . A system according to claim 11 , wherein the dryer is selected to be at least one of a drum dryer or a spray dryer.
17 . A system according to claim 10 , wherein the microbial cells comprise isolated bacterial strain deposited as VTT-E-193585 or a derivative thereof.