Reactor with plate-shaped catalytic membrane for direct conversion of microalgae into biofuels
US-2024026387-A1 · Jan 25, 2024 · US
US2018223247A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018223247-A1 |
| Application number | US-201815945658-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 4, 2018 |
| Priority date | Jul 25, 2013 |
| Publication date | Aug 9, 2018 |
| Grant date | — |
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The present invention relates to a method for optimising the downstream processing of a protein-rich microalgae biomass of the Chlorella genus previously prepared by fermentation in heterotrophic conditions and in the absence of light, comprising: 1) providing biomass comprising more than 50% protein by dry weight of biomass; next, at low temperature, carrying out the following steps: 2) harvesting the biomass at the end of fermentation, 3) washing and concentrating the biomass, 4) optionally, lysing the biomass, next, without low temperature stress, 5) optionally, concentrating the biomass slurry, 6) applying heat treatment, 7) drying the biomass obtained in this way in order to obtain the product, a step of adjusting the pH to 7 being applied before or after the heat treatment step 6).
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1 .- 10 . (canceled) 11 . A method for optimizing the downstream processing of a protein-rich biomass of microalgae of the Chlorella genus which has been prepared beforehand by fermentation in heterotrophic conditions and in the absence of light, comprising: 1 providing a fermentation broth comprising biomass, said biomass comprising more than 55% protein by dry weight; 2 chilling the fermentation broth to lower than 8° C. and recovering the biomass; 3 washing and concentrating the biomass; 4 optionally lysing the biomass; 5 optionally concentrating the biomass suspension; 6 applying a heat treatment; and 7 drying the resulting biomass to obtain the product. 12 . The method as claimed in claim 11 , characterized in that the protein comprises more than 60% by dry weight of the biomass. 13 . The method as claimed in claim 11 , characterized in that the heat treatment is a high temperature/short time (HTST) heat treatment for 30 seconds to 5 minutes at a temperature lower than 100° C. 14 . The method as claimed in claim 11 , characterized in that the heat treatment is an ultra-high temperature (UHT) heat treatment at a temperature of between 100° C. and 150° C. for 5 to 30 seconds. 15 . The method as claimed in claim 11 , characterized in that the biomass washed with at most 6 volumes of water per 1 volume of biomass. 16 . The method as claimed in claim 11 , characterized in that the fermentation broth is neutralized to pH 7 by adding KOH or NaOH. 17 . The method as claimed in claim 11 , characterized in that the cells of the biomass are lysed by milling. 18 . The method as claimed in claim 11 , characterized in that the biomass is concentrated by centrifugation or evaporation. 19 . The method as claimed in claim 11 , characterized in that the effects of the steps of processing the microalgal biomass on the quality of the product are also determined by one or more of the following parameters: measuring the dry sell weight in the biomass; measuring the sugar content; determining the amount of proteins analyzing the volatile organic compounds; measuring the enzyme activities, in particular lipoxygenase activity; measuring the coloration of the pigment content; measuring the content of metals, in particular iron, copper or nickel; and/or determining the degree of oxidation. 20 . The method as claimed in claim 11 , characterized in that the microalgae of the Chlorella genus is selected from the group consisting of Chlorella vulgaris, Chlorella sorokiniana and Chlorella protothecoides. 21 . The method as claimed in claim 20 , characterized in that the microalgae of the Chlorella genus is Chlorella protothecoides.
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