Sequential hydrothermal liquifaction (SEQHTL) for extraction of superior bio-oil and other organic compounds from oleaginous biomass
Methods of producing bio-fuel and other high-value products from oleaginous biomass (e.g. algae biomass) are provided. The two-step methods use a first step of subcritical water extraction of the biomass at low temperatures to produce polysaccharides and other high value products of interest, followed by, ii) hydrothermal liquefaction of remaining solid biomass at high temperatures to produce bio-oil.
1. A process for obtaining polysaccharides from oleaginous biomass comprising
heating a mixture consisting of oleaginous biomass and an aqueous medium to a temperature in the range of from 155 to 165° C.;
maintaining said mixture at said temperature for a period of time of from 15 to 25 minutes; then
recovering polysaccharides released from said oleaginous biomass from said mixture.
2. The method of claim 1 , wherein said step of recovering includes the steps of
separating a liquid fraction of said mixture from a solid fraction of said mixture; and
extracting polysaccharides from said liquid fraction.
3. The method of claim 2 , wherein said step of extracting is carried out via precipitation with ethanol.
4. The method of claim 1 , wherein said temperature is 160° C.
5. The method of claim 1 , wherein said period of time is 20 minutes.
6. The method of claim 1 , further comprising a step of recovering from said mixture a co-product selected from the group consisting of proteins, polypeptides, peptides and sugars.
7. The method of claim 1 , wherein said oleaginous biomass is algae biomass.
8. A process for obtaining bio-oils from oleaginous biomass comprising
separating a liquid fraction of an aqueous mixture comprising oleaginous biomass from a solid fraction of said aqueous mixture;
heating an aqueous mixture comprising said solid fraction of said mixture to a temperature in the range of from 237 to 243° C.;
maintaining said mixture at said temperature for a period of time of from 15 to 25 minutes; and
recovering bio-oils produced during said step of maintaining.
9. The method of claim 8 , wherein said temperature is 240° C.
10. The method of claim 8 , wherein said period of time is 20 minutes.
11. The method of claim 8 , wherein said step of recovering is carried out via CH 2 Cl 2 extraction of said mixture.
12. The method of claim 8 , wherein said oleaginous biomass is algae biomass.
13. A method for obtaining polysaccharides and bio-oils from oleaginous biomass, comprising
i) heating an aqueous mixture comprising said oleaginous biomass to a first temperature in the range of from 155 to 165° C.;
ii) maintaining said aqueous mixture comprising said oleaginous biomass at said first temperature for a first period of time of from 15 to 25 minutes;
iii) separating a liquid fraction of said aqueous mixture comprising said oleaginous biomass from a solid fraction of said mixture;
iv) recovering polysaccharides released from said oleaginous biomass from said liquid fraction,
v) heating an aqueous mixture comprising said solid fraction to a second temperature in the range of from 237 to 243° C.;
vi) maintaining said aqueous mixture comprising said solid fraction at said second temperature for a second period of time of from 15 to 25 minutes; and
vii) recovering, from said aqueous mixture comprising said solid fraction, bio-oils produced during said steps of v) heating and vi) maintaining.
14. The method of claim 13 , wherein said step of iv) recovering polysaccharides is carried out by ethanol precipitation.
15. The method of claim 13 , wherein said first temperature is 160° C. and said second temperature is 240° C.
16. The method of claim 13 , wherein said first and second periods of time are 20 minutes.
17. The method of claim 13 , further comprising a step of recovering from said liquid fraction a co-product selected from the group consisting of proteins, polypeptides, peptides and sugars.
18. The method of claim 13 , wherein said oleaginous biomass is algae biomass.