Methods and apparatus for enhancing the energy content of carbonaceous materials from pyrolysis

Patent metadata

Field	Value
Publication number	US-10611977-B2
Application number	US-201715802716-A
Country	US
Kind code	B2
Filing date	Nov 3, 2017
Priority date	Apr 15, 2011
Publication date	Apr 7, 2020
Grant date	Apr 7, 2020

Abstract

Processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Pyrolysis in the presence of an inert gas is employed 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

The invention claimed is:

1. A process for producing a high-carbon biogenic reagent, the process comprising:
(a) providing a carbon-containing feedstock comprising biomass;
(b) in a pyrolysis zone, pyrolyzing the feedstock in the presence of a substantially inert gas for at least 10 minutes at a pyrolysis temperature from about 250° C. to about 700° C., thereby generating hot pyrolyzed solids, condensable vapors, and non-condensable gases;
(c) separating at least a portion of the condensable vapors and at least a portion of the non-condensable gases from the hot pyrolyzed solids;
(d) in a cooling zone, cooling the hot pyrolyzed solids, in the presence of the substantially inert gas for at least 5 minutes at a cooling temperature less than the pyrolysis temperature, thereby generating warm pyrolyzed solids;
(e) subsequently passing at least a portion of the condensable vapors and/or at least a portion of the non-condensable gases from step (c) across the warm pyrolyzed solids, thereby forming enhanced pyrolyzed solids with increased carbon content; and
(f) recovering a high-carbon biogenic reagent comprising at least a portion of the enhanced pyrolyzed solids.

2. The process of claim 1 , further comprising drying the feedstock to remove at least a portion of moisture contained within the feedstock to thereby produce dried feedstock, and/or deaerating the dried feedstock to remove at least a portion of interstitial oxygen contained within the feedstock to thereby produce deaerated feedstock.

3. The process of claim 1 , further comprising, in step (e), passing:
at least a portion of the condensable vapors from step (c), in vapor and/or condensed form, across the warm pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content;
at least a portion of the non-condensable gases from step (c) across the warm pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content; and/or
at least a portion of the condensable vapors from step (c), in vapor and/or condensed form, across the cool pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content.

4. The process of claim 1 , further comprising recovering energy from the condensable vapors and/or from the non-condensable gases for use in the process.

5. The process of claim 1 , further comprising introducing an intermediate feed stream comprising at least a portion of the condensable vapors and at least a portion of the non-condensable gases, obtained from step (c), to a separation unit configured to generate a first output stream and a second output stream.

6. The process of claim 1 , further comprising introducing into the process an additive.

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

8. The process of claim 1 , wherein the pyrolysis temperature is from about 350° C. to about 600° C.

9. The process of claim 1 , further comprising pyrolyzing the feedstock in the presence of a substantially inert gas from about 0.5 hours to about 4 hours.

10. The process of claim 1 , further comprising pyrolyzing the feedstock in the presence of a substantially inert gas for about 2 hours, and wherein the pyrolysis temperature is about 600° C.

11. A process for producing a high-carbon biogenic reagent, the process comprising:
(a) providing a carbon-containing feedstock comprising biomass;
(b) in a pyrolysis zone, pyrolyzing the feedstock in the presence of a substantially inert gas for at least 10 minutes at a pyrolysis temperature from about 250° C. to about 700° C., thereby generating hot pyrolyzed solids, condensable vapors, and non-condensable gases;
(c) separating at least a portion of the condensable vapors and at least a portion of the non-condensable gases from the hot pyrolyzed solids;
(d) in a cooling zone, cooling the hot pyrolyzed solids, in the presence of the substantially inert gas for at least 5 minutes at a cooling temperature less than the pyrolysis temperature, thereby generating warm pyrolyzed solids;
(e) in a cooler, cooling the warm pyrolyzed solids to generate cool pyrolyzed solids;
(f) subsequently passing at least a portion of the condensable vapors and/or at least a portion of the non-condensable gases from step (c) across the warm pyrolyzed solids and/or the cool pyrolyzed solids, thereby forming enhanced pyrolyzed solids with increased carbon content; and
(g) recovering a high-carbon biogenic reagent comprising at least a portion of the enhanced pyrolyzed solids.

12. The process of claim 11 , further comprising drying the feedstock to remove at least a portion of moisture contained within the feedstock to thereby produce dried feedstock, and/or deaerating the dried feedstock to remove at least a portion of interstitial oxygen contained within the feedstock to thereby produce deaerated feedstock.

13. The process of claim 11 , further comprising, in step (e), passing:
at least a portion of the condensable vapors from step (c), in vapor and/or condensed form, across the warm pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content;
at least a portion of the non-condensable gases from step (c) across the warm pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content;
at least a portion of the condensable vapors from step (c), in vapor and/or condensed form, across the cool pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content
at least a portion of the non-condensable gases from step (c) across the cool pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content;
substantially all of the condensable vapors from step (c), in vapor and/or condensed form, across the cool pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon and/or energy content;
substantially all of the non-condensable gases from step (c) across the cool pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon content.

14. The process of claim 11 , further comprising recovering energy from the condensable vapors and/or from the non-condensable gases for use in the process.

15. The process of claim 11 , further comprising introducing an intermediate feed stream comprising at least a portion of the condensable vapors and at least a portion of the non-condensable gases, obtained from step (c), to a separation unit configured to generate a first output stream and a second output stream.

16. The process of claim 11 , further comprising introducing into the process an additive.

17. The process of claim 11 , further comprising monitoring and controlling the process with at least one reaction gas probe or with at least two reaction gas probes.

18. The process of claim 11 , wherein the pyrolysis temperature is from about 350° C. to about 600° C.

19. The process of claim 11 , further comprising pyrolyzing the feedstock in the presence of a substantially inert gas from about 0.5 hours to about 4 hours.

20. The process of claim 11 , further comprising pyrolyzing the feedstock in the presence of a substantially inert gas for about 2 hours, and wherein the pyrolysis temperature is about 600° C.

Assignees

• Carbon Tech Holdings Llc

Inventors

• Mennell James A
• Despen Daniel J

Classifications

• C10L2290/50

  Screws or pistons for moving along solids · CPC title

• C10L2200/0469

  Renewables or materials of biological origin · CPC title

• Y02W10/30

  Wastewater or sewage treatment systems using renewable energies · CPC title

• C10L5/04

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

• C10B39/00

  Cooling or quenching coke · CPC title