Process for producing high-carbon biogenic reagents

Patent metadata

Field	Value
Publication number	US-10982161-B2
Application number	US-201816199653-A
Country	US
Kind code	B2
Filing date	Nov 26, 2018
Priority date	Apr 15, 2011
Publication date	Apr 20, 2021
Grant date	Apr 20, 2021

Abstract

This invention provides processes and systems for converting biomass into high carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu/lb, 13,000 Btu/lb, 14,000 Btu/lb, or 14,500 Btu/lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and/or strength that derive from the feedstock, heat rate, and additives.

First claim

What is claimed is:

1. A process for producing a high-carbon biogenic reagent, the process comprising:
(a) providing a carbon-containing feedstock comprising biomass;
(b) optionally drying the feedstock to remove at least a portion of moisture contained within the feedstock;
(c) optionally deaerating the feedstock to remove at least a portion of interstitial oxygen, if any, contained with the feedstock or the dried feedstock;
(d) in a pyrolysis zone, pyrolyzing the feedstock in the presence of a substantially inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases;
(e) separating at least a portion of the condensable vapors and at least a portion of the non-condensable gases from the hot pyrolyzed solids;
(f) in a cooling zone, cooling the hot pyrolyzed solids, in the presence of the substantially inert gas with a cooling zone temperature less than the pyrolysis temperature, to generate warm pyrolyzed solids;
(g) in an optional cooler that is separate from the cooling zone, cooling the warm pyrolyzed solids to generate cool pyrolyzed solids; and
(h) recovering a high-carbon biogenic reagent comprising at least a portion of the cool pyrolyzed solids.

2. The process of claim 1 , the process further comprising:
drying the feedstock to remove at least a portion of moisture contained within the feedstock, deaerating the feedstock to remove at least a portion of interstitial oxygen contained with the feedstock, and/or prior to step (d), preheating the dried feedstock in a preheating zone in the presence of the substantially inert gas for at least 5 minutes and with a preheating temperature selected from about 80° C. to about 500° C.

3. The process of claim 1 , wherein the pyrolysis step (d) is carried out for at least 10 minutes and with a pyrolysis temperature at least about 250° C. and/or the cooling step (f) is carried out for at least 5 minutes.

4. The process of claim 1 , wherein the cooling zone temperature is selected from about 150° C. to about 350° C.

5. The process of claim 1 , wherein each of the zones is located within a single reactor and/or in a separate reactor.

6. The process of claim 1 , wherein the substantially inert gas is selected from the group consisting of N 2 , Ar, CO, CO 2 , H 2 , CH 4 , and combinations thereof and/or at least some of the substantially inert gas includes one or more non-condensable gas species recycled from step (e).

7. The process of claim 1 , wherein the pyrolysis zone and the cooling zone each comprise a gas phase containing less than 5 wt % oxygen.

8. The process of claim 1 , wherein the process is continuous or semi-continuous and wherein the inert gas flows either countercurrent or concurrent relative to the direction of solids flow.

9. The process of claim 1 , the process further comprising monitoring and controlling the process with at least one reaction gas probe.

10. The process of claim 9 , wherein the monitoring and controlling the process improves process energy efficiency and/or improves product attributed associated with the high carbon biogenic reagent.

11. The process of claim 10 , wherein the product attribute is carbon content, energy content, and/or structural integrity strength.

12. The process of claim 1 , the process further comprising process gas heating of at least a portion of the condensable vapors with an oxygen-containing gas and/or drying the feedstock to remove at least a portion of moisture contained within the feedstock,
wherein heat produced from the process gas heating is utilized, at least in part, for the drying.

13. The process of claim 12 , wherein the process gas heating is assisted with combustion of natural gas and/or heat produced from the process gas heating is utilized, at least in part, to heat the substantially inert gas.

14. The process of claim 13 , wherein at least a portion of the substantially inert gas is heated and then introduced to the pyrolysis zone.

15. The process of claim 1 , the process further comprising combining: at least a portion of the condensable vapors, in at least partially condensed form, with the cooled pyrolyzed solids, to increase the carbon content of the high-carbon biogenic reagent and/or at least a portion of the condensable vapors with the warm pyrolyzed solids, to increase the carbon content of the high-carbon biogenic reagent.

16. The process of claim 1 , the process further comprising introducing at least one additive selected from acids, bases, or salts thereof.

17. The process of claim 16 , wherein the additive is selected from the group consisting of sodium hydroxide, potassium hydroxide, magnesium oxide, hydrogen bromide, hydrogen chloride, sodium silicate, potassium permanganate, and combinations thereof or from the group consisting of a metal, a metal oxide, a metal hydroxide, a metal halide, and combinations thereof.

18. The process of claim 16 , wherein the additive is selected to maintain the structural integrity or mechanical strength of the high-carbon biogenic reagent relative to the feedstock, the presence of the additive in the process increases the carbon content of the high-carbon biogenic reagent compared to an otherwise-identical process without introduction of the additive, and/or the presence of the additive in the process increases the energy content of the high-carbon biogenic reagent compared to an otherwise-identical process without introduction of the additive.

19. The process of claim 16 , wherein the additive is introduced: prior to or during step (b), prior to or during step (d), during step (f), during step (g), between steps (f) and (g), after step (g), and/or to the warm pyrolyzed solids in an aqueous solution, vapor, or aerosol to assist with cooling of the warm pyrolyzed solids in step (g).

20. The process of claim 16 , wherein the additive is introduced to the cool pyrolyzed solids to form the high-carbon biogenic reagent containing the additive.

21. The process of claim 1 , the process further comprising introducing at least a portion of the cool pyrolyzed solids to a separate unit for additional pyrolysis, in the presence of a second substantially inert gas for at least 30 minutes and with a pyrolysis temperature selected from about 200° C. to about 600° C., to generate a solid product having higher carbon content than the cool pyrolyzed solids.

22. The process of claim 21 , the process further comprising process gas heating of at least a portion of the condensable vapors with an oxygen-containing gas; wherein heat produced from the process gas heating is utilized, at least in part, to heat the second substantially inert gas prior to introduction to the separate unit for additional pyrolysis.

23. The process of claim 21 , wherein the second substantially inert gas is selected from the group consisting of N 2 , Ar, CO, CO 2 , H 2 , CH 4 , and combinations thereof and/or wherein at least some of the second substantially inert gas includes one or more non-condensable gas species recovered from step (e).

24. The process of claim 2 , the process further comprising operating the cooler to cool the warm pyrolyzed solids with steam, thereby generating the cool pyrolyzed solids and superheated steam; wherein the drying is carried out, at least in part, with the superheated steam derived from the cooler.

25. The process of claim 24 , wherein the cooler is operated to first cool the warm pyrolyzed solids with steam to reach a first cooler tem

Assignees

• Carbon Tech Holdings Llc

Inventors

• Mennell James A
• Despen Daniel J

Classifications

• C10B57/06

  containing additives · CPC title

• Y02E60/10

  Energy storage using batteries · CPC title

• Y02E50/30

  Fuel from waste, e.g. synthetic alcohol or diesel · CPC title

• Y02P20/145

  the feedstock being materials of biological origin · CPC title

• Y02P10/143

  of methane [CH4] · CPC title