Biogenic Reagent Pyrolysis with Inert-Gas Cooling Zones

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Solution Overview

Problem

Existing pyrolysis processes for converting biomass into high-carbon reagents face challenges in optimizing yield and quality, particularly in scaling up for continuous commercial-scale production while managing energy balance and controlling emissions, with traditional charcoal-making technologies being energy-inefficient and highly polluting.

Innovation Solution

A multi-zone biomass processing unit (BPU) process involving pyrolysis, cooling, and optional additive introduction to produce high-carbon biogenic reagents, with controlled atmospheric and temperature conditions, and use of inert gases to enhance carbon content and structural integrity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-generated harmful factors

If traditional charcoal-making pyrolysis processes are used, then carbon-containing reagents can be produced, but energy efficiency is poor and emissions are high

Engineering Contradiction:
ImproveemissionsVSAvoidenergy efficiency
Core Design Contradiction:
Object-generated harmful factorsVSUse of energy by moving object

Solution Approach 1:

The pyrolysis process is divided into multiple temperature zones (first pyrolysis zone at 200-400°C, second pyrolysis zone at 400-700°C) within a single reactor. This segmentation allows different stages of carbonization to occur simultaneously at optimal temperatures, improving energy efficiency by preventing heat loss and reducing emissions through controlled atmospheric conditions in each zone.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent introduces an inert gas (nitrogen or carbon dioxide) into the pyrolysis reactor to create an oxygen-deficient atmosphere. This inert environment prevents combustion of the biomass and pyrolysis products, thereby reducing harmful emissions while maintaining efficient energy utilization for carbonization. The inert gas also facilitates controlled heating and cooling processes.

Inventive Principle:
Principle #39Inert atmosphere (Inert environment)

2Quantity of substance

If pyrolysis temperature is increased to improve carbon content, then high-carbon reagents are produced, but energy consumption increases

Engineering Contradiction:
Improvecarbon contentVSAvoidenergy consumption
Core Design Contradiction:
Quantity of substanceVSUse of energy by moving object

Solution Approach 1:

The reactor is divided into multiple temperature zones allowing progressive carbonization. The first zone performs low-temperature pyrolysis (200-400°C) to remove moisture and volatiles, while the second zone performs high-temperature pyrolysis (400-700°C) to maximize carbon content. This segmentation achieves high carbon content in the final product without requiring the entire reactor to consume high energy levels continuously.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The multi-zone pyrolysis process operates continuously with overlapping temperature zones. Heat generated in the high-temperature zone partially preheats the incoming biomass in lower zones, creating a continuous energy cascade that reduces overall energy consumption while maintaining high carbon content production.

Inventive Principle:
Principle #20Continuity of useful action

3Productivity

If continuous commercial-scale production is implemented, then productivity increases, but process control and emissions management become more difficult

Engineering Contradiction:
Improveproduction scaleVSAvoidprocess control
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The reactor is segmented into multiple temperature zones with independent control capabilities. Each zone can be optimized for specific pyrolysis stages, allowing continuous operation at commercial scale while maintaining precise control over carbonization conditions. This zoned approach simplifies emissions management by containing different reaction stages in separate controlled environments.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent incorporates temperature sensors and control systems in each pyrolysis zone to monitor and adjust heating rates and atmospheric conditions in real-time. This feedback mechanism enables continuous operation with automatic process control, maintaining optimal carbon content while managing emissions and energy consumption at commercial production scales.

Inventive Principle:
Principle #23Feedback

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The process achieves high-carbon biogenic reagents with carbon content up to 70% and energy content of at least 11,000 Btu/lb, improving efficiency and reducing emissions, suitable for various industrial applications.

Implementation Method 1

Pyrolysis is a process for thermal conversion of solid materials in the complete absence of oxidizing agent (air or oxygen), or with such limited supply that oxidation does not occur to any appreciable extent.

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 2

in a cooling zone, cooling the hot pyrolyzed solids, in the presence of the substantially inert gas for at least about 5 minutes and with a cooling-zone temperature less than the pyrolysis temperature

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentUS12404472B2High-carbon biogenic reagents and uses thereof
Publication Date: 2025.09.02 CARBON TECHNOLOGY HOLDINGS LLC
  • US12404472B2 patent drawing
  • US12404472B2 patent drawing
  • US12404472B2 patent drawing

AI summary

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.