Method for converting algal biomass into a gas or into biocrude by hydrothermal gasification or hydrothermal liquefaction, respectively
The invention relates to methods for converting algal biomass into a gas or into biocrude comprising (a) gasification or hydrothermal liquefaction of an algal biomass in at least one first reactor, (b) separation of the gas or biocrude produced thereby from the aqueous effluents and the CO 2 produced, at the outlet of the first reactor, (c) recovery of the aqueous effluents, and (d) oxidation of the aqueous effluents in at least one second reactor. Continuous processes for culture of algal biomass and conversion of the algal biomass cultivated into a gas or into a biocrude are also disclosed.
1. A method for converting algal biomass into a gas or biocrude with a view to producing a fuel, a motor fuel, or a liquid fuel, or some other synthetic product, comprising:
(a) gasification or hydrothermal liquefaction of an algal biomass in at least one first reactor;
(b) separation between respectively the gas or biocrude produced and the aqueous effluents and the CO 2 produced at the outlet of the first reactor;
(c) recovery of the aqueous effluents; and
(d) oxidation of the aqueous effluents in at least one second reactor;
wherein step (d) is oxidation by a wet process or a hydrothermal oxidation (HTO) in supercritical conditions.
2. The method of conversion according to claim 1 , wherein step (a) is a liquefaction process carried out at a temperature ranging from 150° C. to 374° C.
3. The method of conversion according to claim 1 , wherein step (a) is a liquefaction process carried out at a pressure ranging from 0.5 MPa to 35 MPa.
4. The method of conversion according to claim 1 , wherein step (a) is a gasification process carried out at a temperature ranging from 374° C. to 800° C.
5. The method of conversion according to claim 1 , wherein step (a) is a gasification process carried out at a pressure ranging from 22.1 MPa to 35 MPa.
6. The method of conversion according to claim 1 , wherein step (a) is carried out for a residence time ranging from 15 seconds to 1 hour.
7. The method of conversion according to claim 1 , wherein step (d) is a wet-process oxidation carried out at a temperature ranging from 150° C. to 374° C.
8. The method of conversion according to claim 1 , wherein step (d) is a wet-process oxidation carried out at a pressure ranging from 0.5 MPa to 35 MPa.
9. The method of conversion according to claim 1 , wherein step (d) is a hydrothermal oxidation carried out at a temperature ranging from 374° C. to 800° C.
10. The method of conversion according to claim 1 , wherein step (d) is a hydrothermal oxidation carried out at a pressure ranging from 22.1 MPa to 35 MPa.
11. The method of conversion according to claim 1 , wherein step (d) is carried out for a residence time in the second reactor ranging from 15 seconds to 1 hour.
12. The method of conversion according to claim 1 , wherein step (d) is a wet-process oxidation carried out with part of the biocrude produced injected into the second reactor.
13. The method of conversion according to claim 1 , wherein the CO 2 produced is further separated and injected, as solvent, in the biocrude product.
14. The method of conversion according to claim 1 , wherein the heat produced during step (d) of oxidation in the second reactor is supplied to the first reactor for carrying out step (a) of hydrothermal liquefaction or gasification.
15. The method of conversion according to claim 1 , wherein the heat produced during step (d) of oxidation in the second reactor is supplied for preheating an oxidizing gas.
16. The method of conversion according to claim 1 , wherein step (a) of hydrothermal liquefaction and step (d) of oxidation are carried out in a double-jacket reactor, said double-jacket reactor comprising an inner jacket delimiting the chamber of the first reactor internally, and an outer jacket surrounding the inner jacket, with the space between the inner jacket and the outer jacket defining the chamber of the second reactor.
17. The method of conversion according to claim 1 , wherein step (a) of hydrothermal liquefaction or gasification is carried out in several first reactors fluidically in parallel.
18. The method of conversion according to claim 1 , wherein step (d) of oxidation is carried out in several second reactors fluidically in parallel.
19. A continuous process for culture of algal biomass and conversion of the algal biomass cultivated into a gas or into a biocrude, comprising:
(a′) culturing the algal biomass in a zone containing a culture medium;
(a″) harvesting the cultivated algal biomass;
(a) gasification or hydrothermal liquefaction of an algal biomass in at least one first reactor;
(b) separation between respectively the gas or biocrude produced and the aqueous effluents and the CO 2 produced at the outlet of the first reactor;
(c) recovery of the aqueous effluents;
(d) oxidation of the aqueous effluents in at least one second reactor; and
(d′) injecting the water, nutrients, and any CO 2 obtained at the outlet of the second reactor, into the culture zone.
20. The continuous process according to claim 19 , further comprising (d″) recovery of any oxygen (O 2 ) produced by the algal biomass to inject it, as oxidant, upstream of the second reactor before the oxidation step (d).