Process for producing high-carbon biogenic reagents
US-10174267-B2 · Jan 8, 2019 · US
US11286440B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11286440-B2 |
| Application number | US-202016840813-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 6, 2020 |
| Priority date | Apr 15, 2011 |
| Publication date | Mar 29, 2022 |
| Grant date | Mar 29, 2022 |
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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.
Opening claim text (preview).
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) optionally drying the feedstock to remove at least a portion of moisture contained within the feedstock; (c) optionally deaerating the dried feedstock to remove at least a portion of interstitial oxygen, if any, contained with the feedstock; (d) pyrolyzing, in a pyrolysis zone, the feedstock in the presence of a substantially inert gas, thereby generating 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) cooling, in a cooling zone, the hot pyrolyzed solids in the presence of the substantially inert gas with a cooling temperature less than the pyrolysis temperature, thereby generating warm pyrolyzed solids; (g) optionally cooling, in a cooler, the warm pyrolyzed solids, thereby generating cool pyrolyzed solids; (h) subsequently passing at least a portion of the condensable vapors and/or at least a portion of the non-condensable gases from step (e) across the warm pyrolyzed solids and/or the cool pyrolyzed solids, thereby forming enhanced pyrolyzed solids with increased carbon content; and (i) recovering a high-carbon biogenic reagent comprising at least a portion of the enhanced pyrolyzed solids. 2. The process of claim 1 , wherein step (h) includes passing substantially all of the non-condensable gases from step (e) across the cool pyrolyzed solids, thereby producing enhanced pyrolyzed solids with increased carbon content. 3. 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 dried feedstock to remove at least a portion of interstitial oxygen, if any, contained with the feedstock; (d) pyrolyzing, in a pyrolysis zone, the feedstock in the presence of a substantially inert gas, thereby generating 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) cooling, in a cooling zone, the hot pyrolyzed solids in the presence of the substantially inert gas with a cooling temperature less than the pyrolysis temperature, thereby generating warm pyrolyzed solids; (g) optionally cooling, in a cooler, the warm pyrolyzed solids, thereby generating cool pyrolyzed solids; (h) subsequently passing at least a portion of the condensable vapors and/or at least a portion of the non-condensable gases from step (e) across the warm pyrolyzed solids and/or the cool pyrolyzed solids, thereby forming enhanced pyrolyzed solids with increased carbon content; and (i) recovering a high-carbon biogenic reagent comprising at least a portion of the enhanced pyrolyzed solids; wherein the condensable vapors include at least one carbon-containing compound selected from terpenes, alcohols, acids, aldehydes, or ketones or at least one carbon-containing molecule selected from the group consisting of carbon monoxide, carbon dioxide, and methane.
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