Biomass conversion reactors and associated systems and methods

Patent metadata

Field	Value
Publication number	US-11339342-B2
Application number	US-201816613692-A
Country	US
Kind code	B2
Filing date	May 16, 2018
Priority date	May 16, 2017
Publication date	May 24, 2022
Grant date	May 24, 2022

Abstract

Systems and methods associated with biomass decomposition are generally described. Certain embodiments are related to adjusting a flow rate of a fluid comprising oxygen into a reactor in which biomass is decomposed. The adjustment may be made, at least in part, based upon a measurement of a characteristic of the reactor and/or a characteristic of the biomass. Certain embodiments are related to cooling at least partially decomposed biomass. The biomass may be cooled by flowing a gas over an outlet conduit in which the biomass is cooled, and then directing the gas to a reactor after it has flowed over the outlet conduit. Certain embodiments are related to systems comprising a reactor and an outlet conduit configured such that greater than or equal to 75% of its axially projected cross-sectional area is occupied by a conveyor. Certain embodiments are related to systems comprising a reactor comprising an elongated compartment having a longitudinal axis arranged substantially vertically and an outlet conduit comprising a conveyor.

First claim

What is claimed is:

1. A method of performing torrefaction of biomass within a reactor to form a primarily solid product, comprising:
measuring a characteristic of the biomass; and
adjusting, via a controller, a flow rate of a fluid comprising oxygen into the reactor in which the biomass is torrefied, wherein the adjustment is made, at least in part, based upon the measurement of the characteristic of the biomass.

2. The method of claim 1 , wherein the reactor comprises an inlet fluidically connected to a source of the fluid comprising the oxygen.

3. The method of claim 1 , wherein the characteristic of the biomass is a moisture content of the biomass.

4. The method of claim 1 , wherein the characteristic of the biomass is
a characteristic of one or more exhaust gases produced during torrefaction of the biomass.

5. The method of claim 1 , wherein the reactor is a moving bed reactor.

6. The method of claim 1 , wherein the reactor comprises an outlet conduit, and wherein the outlet conduit is configured such that greater than or equal to 75% of its axially projected cross-sectional area is occupied by a conveyor.

7. The method of claim 1 , wherein adjusting the flow rate of the fluid comprising the oxygen into the reactor in which the biomass is torrefied comprises increasing the flow rate of the fluid comprising the oxygen into the reactor in which the biomass is torrefied.

8. The method of claim 1 , further comprising adjusting a rate at which the biomass is introduced into the reactor.

9. The method of claim 1 , wherein the method is performed in a system comprising the reactor, the system further comprises a sensor, and wherein:
the sensor is configured to perform the measurement of the characteristic of the biomass; and
the sensor comprises a thermocouple, a mass flow sensor, a gas analyzer, an oxygen sensor, a pressure transducer, a load cell, a rotary encoder, and/or a level detector.

10. The method of claim 1 , further comprising adjusting a rate at which the biomass is output from the reactor.

11. The method of claim 1 , wherein the characteristic of the biomass is an energy density of the biomass prior to the torrefaction within the reactor.

12. The method of claim 1 , wherein the characteristic of the biomass is an energy density of the biomass after the torrefaction within the reactor.

13. The method of claim 1 , wherein the characteristic of the biomass is an index of torrefaction of the biomass after torrefaction within the reactor.

14. The method of claim 1 , wherein the characteristic of the biomass is a biomass type.

15. The method of claim 1 , wherein the characteristic of the biomass is a chemical composition of the biomass prior to and/or after torrefaction within the reactor.

16. The method of claim 1 , wherein the characteristic of the biomass is a ratio of a flow rate of torrefied biomass out of the reactor to a flow rate of the biomass into the reactor.

17. The method of claim 1 , wherein the characteristic of the biomass is a product of the flow rate of torrefied biomass out of the reactor and an index of torrefaction of the torrefied biomass.

18. The method of claim 1 , wherein the characteristic of the biomass is a combustion temperature of the biomass after torrefaction within the reactor.

19. The method of claim 1 , wherein adjusting the flow rate of the fluid comprising the oxygen into the reactor in which the biomass is torrefied comprises maintaining the flow rate of the fluid comprising the oxygen into the reactor in which the biomass is torrefied.

20. The method of claim 1 , further comprising introducing an ignition source into the reactor.

Assignees

• Massachusetts Inst Technology

Inventors

• Kung Kevin S
• Slocum Alexander H
• Shanbhogue Santosh Janardhan
• Ghoniem Ahmed Fouad
• Stoner Robert James

Classifications

• B01J2219/00121

  by direct heating or cooling · CPC title

• C10G1/00

  Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal (mechanical winning of oil from oil-shales, oil-sand, or the like B03B) · CPC title

• B01J2219/00186

  controlling the composition of the reactive mixture · CPC title

• C10L5/445

  Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues · CPC title

• B01J19/0006

  Controlling or regulating processes (controlling or regulating in general G05) · CPC title