Method for processing biomass by co-grinding with a fossil-based feedstock

Patent metadata

Field	Value
Publication number	US-11248185-B2
Application number	US-201816628891-A
Country	US
Kind code	B2
Filing date	Jul 3, 2018
Priority date	Jul 7, 2017
Publication date	Feb 15, 2022
Grant date	Feb 15, 2022

Abstract

Process for the treatment of a feedstock containing biomass, the process includinga) drying the feedstock at a temperature between 20 and 180° C. for a duration between 5 and 180 minutes,b) torrefaction of the feedstock originating from step a) in order to produce at least one torrefied biomass solid effluent,c) co-grinding the torrefied biomass solid effluent originating from step b), in the presence of at least one solid fossil feedstock in order to obtain a powder.

First claim

The invention claimed is:

1. A process for the treatment of a feedstock comprising biomass, said process comprising at least the following steps:
a) a step of drying said feedstock comprising biomass at a temperature of 20 to 180° C. for a duration of 5 to 180 minutes,
b) a step of torrefaction of the dried feedstock originating from step a) producing at least one torrefied biomass solid effluent, and
c) a step of co-grinding of the at least one torrefied biomass solid effluent originating from step b), in the presence of at least one solid fossil feedstock obtaining a powder,
in which
the quantity of residual water at the end of drying step a) is 0.0% to 5.0% by weight with respect to the total weight of the feedstock,
the dimensions of the solid fossil feedstock introduced in co-grinding step c) are 1 to 100 millimeters, and
the solid fossil feedstock input into co-grinding step c) has a moisture content of 3.1 to 30.0% by weight,

and
one or more of the following conditions 1), 2), 3) and/or 4):
1) the biomass is a lignocellosic biomass selected from the group consisting of grass biomass, residues from agricultural operations, waste straw, maize cobs, crushed sugar cane stalks, residues from forestry operations, residues from sawmills and wood chips,
2) the at least one solid fossil feedstock is selected from the group consisting of solid fossil hydrocarbons, coal, petcoke, oil tanker residues, bituminous sands, derivatives of bituminous sands, oil shales and derivatives of oil shales,
3) the at least one torrefied biomass solid effluent originating from step b) is introduced in co-grinding step c) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 40 to 99% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock, and/or
4) the step of co-grinding of the at least one torrefied biomass solid effluent originating from step b) is performed at a temperature of 0° C. to 150° C.,
and
one or more of the following additional conditions i), ii), iii) and/or iv);
i) torrefied biomass solid effluent originating from step b) is introduced in cogrinding step c) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 75% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock,
ii) torrefied biomass solid effluent originating from step b) is introduced in cogrinding step c) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 50 to 98% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock, and/or
iii) torrefied biomass solid effluent originating from step b) is introduced in cogrinding step c) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 40 to 95% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock, and/or
iv) all of conditions 1), 2), 3) and 4).

2. The process according to claim 1 , further comprising a step d) of final drying of the powder obtained at the end of step c) at a temperature of 100 to 300° C.

3. The process according to claim 2 , in which the final drying step d) is carried out simultaneously with the co-grinding step c).

4. The process according to claim 1 , in which the biomass is wood chips.

5. The process according to claim 1 , further comprising a step i) of pretreatment of the biomass.

6. The process according to claim 1 , in which the torrefaction step b) is carried out at a temperature of 200 to 350° C., for a duration of 5 to 180 minutes, at an absolute operating pressure of 0.1 and 15 bar.

7. The process according to claim 1 , further comprising a step ii) of combustion of torrefaction gases ( 11 ) originating from step b).

8. The process according to claim 7 , in which energy originating from step ii) of combustion of the torrefaction gases ( 11 ) provides thermal energy in a step of the process.

9. The process according to claim 1 , in which the solid fossil feedstock introduced in co-grinding step c) is coal.

10. The process according to claim 1 , in which the solid fossil feedstock undergoes a step iii) of preliminary drying.

11. The process according to claim 1 , in which torrefied biomass solid effluent originating from step b) is introduced in co-grinding step c) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 75% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock.

12. The process according to claim 1 , in which the solid fossil feedstock input into co-grinding step c) has a moisture content of 5.0 to 20.0% by weight.

13. The process according to claim 1 , further comprising one or more steps e) of storage of the effluent originating from any of the steps of the process.

14. The process according to claim 1 , further comprising a step f) of transport.

15. The process according to claim 1 , further comprising a step g) of gasification at a temperature of 800 to 1800° C., and at an absolute pressure of 2 to 12 MPa.

16. The process according to claim 1 , wherein the dimensions of the solid fossil feedstock introduced in co-grinding step c) are 2.0 to 80 millimeters.

17. The process according to claim 1 , wherein the solid fossil feedstock input into co-grinding step c) has a moisture content of 4.0 to 25.0% by weight.

18. The process according to claim 1 , in which torrefied biomass solid effluent originating from step b) is introduced in co-grinding step c) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 50 to 98% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock.

19. A process for the treatment of a feedstock comprising biomass, said process comprising at least the following steps:
d) a step of drying said feedstock comprising biomass at a temperature of 20 to 180° C. for a duration of 5 to 180 minutes,
e) step of torrefaction of the dried feedstock originating from step d) producing at least one torrefied biomass solid effluent, and
f) step of co-grinding of the at least one torrefied biomass solid effluent originating from step e), in the presence of at least one solid fossil feedstock containing a powder,
in which
the quantity of residual water at the end of drying step d) is 0.0% to 5.0% by weight with respect to the total weight of the feedstock,
the dimensions of the solid fossil feedstock introduced in co-grinding step to 100 millimeters, and
the solid fossil feedstock input into co-grinding step f) has a moisture content of 3.1 to 30.0% by weight, and
torrefied biomass solid effluent originating from step e) is introduced in co-grinding step f) in a percentage by weight between the torrefied biomass solid effluent in the total solid feedstock of 40 to 95% by weight, said total solid feedstock being the sum of the torrefied biomass solid effluent and the fossil feedstock, and
one or more of the following conditions:
the biomass is a lignocellosic biomass selected from the group consisting of grass biomass, residues from agricultural operations, waste straw, maize cobs, crushed sugar cane stalks, residues from forestry operations, residues om sawmills and wood chips, the at least one solid fossil f

Assignees

• Ifp Energies Now
• Axens
• Commissariat Energie Atomique
• Total Raffinage Chimie
• Thyssenkrupp Ind Solutions Ag
• Avril
• Bionext

Inventors

• Plennevaux Thomas
• Gazarian Jeremy
• Bournay Laurent
• Ullrich Norbert

Classifications

• C10L9/083

  Torrefaction · CPC title

• C10L5/442

  Wood or forestry waste · CPC title

• C10L5/363

  Pellets or granulates · CPC title

• C10L5/04 Primary

  Raw material {of mineral origin} to be used; Pretreatment thereof {(pretreatment of fuels of non-mineral origin C10L5/40)} · CPC title

• C10L5/44 Primary

  on vegetable substances · CPC title