S2: Continuous Carbonization & Char-Gas Co-generation Solution

Our continuous carbonization system converts biomass and organic waste into high-quality biochar while simultaneously generating combustible syngas for power co-generation. The char-gas co-generation process achieves complete thermal energy circulation — the heat released during carbonization is captured and reused, dramatically improving overall energy efficiency.

Carbon accounting boundary: Potential storage and avoided-emission effects depend on feedstock traceability, biochar properties, end use, energibalance, the selected methodology and independent verification. No carbon-credit eligibility or emissions result is stated before project-specific review.

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ESG & Carbon Asset Management

Carbon-credit eligibility and any quantified climate benefit require a dated methodology, feedstock and operating evidence, product testing, eligible end use, independent validation and local project confirmation. They must not be treated as automatic project revenue.

Char-Gas Co-generation — Thermal Circulation Logic

The char-gas co-generation system operates on a closed-loop thermal circulation model:

1. Primary Carbonization: Biomass feedstock enters the continuous carbonization reactor, where controlled pyrolysis at 450-650°C produces biochar and releases volatile syngas.
2. Syngas Combustion: The hot syngas is directly fed into a gas combustion chamber, generating high-temperature flue gas (800-1000°C) for power generation via a steam turbine or ORC unit.
3. Waste Heat Recovery: Exhaust heat from power generation is captured through economizers and heat exchangers, preheating incoming feedstock and drying biomass — reducing moisture content below 15% before entering the reactor.
4. Thermal Recirculation: A portion of the hot flue gas is redirected to the carbonization reactor jacket, maintaining optimal pyrolysis temperature without external fuel input after startup.
5. Energy integration basis: Available gas and heat depend on feedstock moisture and composition, driftsstabilitet, gas cleaning, auxiliary loads and the selected generator or steam system. Self-sufficiency and export require a verified project energy balance and grid or receiving-load review.

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YUSHUNXIN BIOMASS CARBONIZATION

Connect biochar production with usable heat, steam or power.

A continuous carbonization project can be evaluated as a carbon-product system and an energy system. The correct route depends on biomass consistency, target carbon specification, heat demand, operating scale and the customer's ability to use energy continuously.

01 / MATERIAL TO VALUE

Separate three commercial routes before selecting equipment

Metallurgical biochar, carbon-project biochar and hard-carbon precursor projects have different customers, testing methods and acceptance cycles.

Metallurgical biochar

Prioritize fixed carbon, ash, sulfur, phosphorus, strength, sizing and delivered cost for the downstream furnace.

Carbon-project biochar

Prioritize feedstock traceability, stable carbon, emissions data, operating records and the applicable carbon methodology.

Activated-carbon feedstock

Prioritize precursor uniformity, volatile matter, ash and the subsequent activation route.

Hard-carbon precursor

Treat the project as a development program: precursor purification, controlled pre-carbonization and sample validation come before an industrial-line promise.

02 / ENERGY ROUTES

Use the recovered energy where it creates the clearest operating value

Direct steam supply can be more practical when a stable industrial steam user is nearby; power generation becomes a separate engineering package with stricter gas-cleaning and load-matching requirements.

1. 01Dry and size the biomass
2. 02Continuous oxygen-limited carbonization
3. 03Separate dust and condensable fractions
4. 04Clean and condition process gas
5. 05Return heat to the carbonizer first
6. 06Evaluate steam, power or combined heat-and-power use

03 / FEASIBILITY GATE

What must be verified before an energy claim is used

Do not calculate an energy return from nameplate throughput alone.

Feedstock test

Fugtighed, ash, bulk density, particle size and seasonal variation determine drying and feeding requirements.

Carbon target

The carbon specification defines residence time, thermal profile, cooling and product handling.

Gas characterization

Gas quantity, heating value, tar, dust and moisture determine whether an engine, boiler or thermal oxidizer route is practical.

Demand match

Confirm the user's hourly steam or electrical load, pressure or voltage conditions, annual schedule and backup-energy requirement.

PROJEKT VISUAL

Se grænsen for det tilsluttede udstyr.

Visuelle referencer understøtter diskussion af tidlig layout. Slutudstyr, arrangement og grænseflader bekræftes fra projektmaterialet og sitet.

Se hele projektets visualisering

REFERENCE KONFIGURATION

Oversæt projektfakta til en udstyrsliste.

Denne referencematrix viser beslutningslogikken. Endelige mængder, modeller og grænseflader hører hjemme i det godkendte projektforslag.

System blok	Typisk omfang	Konfigurationsgrundlag
Biomass preparation	Drying, size control, storage and metered feeding	Fugtighed, density and seasonal consistency
Karbonisering	Continuous reactor, atmosphere control and thermal profile	Target carbon specification
Product handling	Sealed cooling, sizing, storage and sample points	Oxidation, dust and product quality
Gas and condensables	Dust separation, condensation and gas conditioning	Tar, moisture and intended heat route
Energiintegration	Internal heat return, optional boiler, generator or user interface	Verified energy balance and demand match

Stage-GATED BESLUTNINGSVEJ

Fremfør kun projektet, når den nødvendige dokumentation er tilgængelig.

Hver gate forvandler kundeinformation til et defineret teknisk eller kommercielt output til den næste beslutning.

01

Biomass and product

Confirm biomass consistency and the actual carbon buyer specification.

ProduktionQualified material-to-product basis

02

Termisk rute

Define drying, sizing, carbonization, cooling and quality sampling.

ProduktionConnected carbon-production flow

03

Energy demand

Match process heat with a verified nearby steam, heat or power demand.

ProduktionPreliminary energy-use boundary

04

Evidence and acceptance

Agree operating records, tests, emissions and any methodology review.

ProduktionProject acceptance and evidence plan

PROJEKT FAQ

Spørgsmål, der skal løses før konfiguration.

Svar definerer den tekniske grænse; de erstatter ikke repræsentativ materialetestning eller lokal overensstemmelsesgennemgang.

What changes the continuous carbonization configuration?

Biomass type, fugtighed, particle size, ash, target carbon specification, driftstimer, heat-use route and environmental requirements change the equipment boundary.

Should steam or power generation be selected first?

The receiving energy load should be studied first. A stable nearby steam demand can favor direct steam use, while power generation requires a separate gas-cleaning, generator and electrical-integration package.

Can carbon-credit revenue be treated as guaranteed project income?

Ingen. Eligibility depends on feedstock traceability, operating evidence, metode, verification and local project conditions.

How is a hard-carbon precursor project different?

It requires precursor purification, controlled thermal development, powder processing and independent material or electrochemical validation beyond ordinary biochar production.

PROJEKT INGENIØR GENNEMGANG

Definer materialet, før du vælger udstyret.

Del en repræsentativ materialebeskrivelse, tilgængelig volumen, webstedsstatus og måloutput. YUSHUNXIN vil bruge disse fakta til at forberede den relevante procesgrænse og konfigurationsdiskussion.

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