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, энергетычны баланс, 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, стабільнасць працы, 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, сера, 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

Вільгаць, 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.

ВІЗУАЛЬНЫЯ МАТЕРЫАЛЫ ПРАЕКТА

Глядзіце мяжу падключанага абсталявання.

Даведачныя візуальныя матэрыялы падтрымліваюць ранняе абмеркаванне макета. Фінальнае абсталяванне, размяшчэнне і інтэрфейсы пацверджаны з матэрыялаў праекта і сайта.

Глядзіце поўную карцінку праекта

ЭТАЛЕННАЯ КАНФІГУРАЦЫЯ

Перавядзіце факты праекта ў спіс абсталявання.

Гэтая эталонная матрыца паказвае логіку рашэння. Канчатковыя колькасці, мадэлі і інтэрфейсы належаць да зацверджанай праектнай прапановы.

Сістэмны блок	Тыпавая сфера прымянення	Аснова канфігурацыі
Biomass preparation	Сушка, size control, storage and metered feeding	Вільгаць, density and seasonal consistency
Карбанізацыя	Continuous reactor, atmosphere control and thermal profile	Target carbon specification
Product handling	Герметычнае астуджэнне, 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
Энергетычная інтэграцыя	Internal heat return, optional boiler, generator or user interface	Verified energy balance and demand match

СТАДЫЙНЫ ШЛЯХ РАШЭННЯ

Прасоўвайце праект толькі пры наяўнасці неабходных доказаў.

Кожная брама ператварае інфармацыю аб кліенце ў пэўны тэхнічны або камерцыйны вынік для наступнага рашэння.

01

Biomass and product

Confirm biomass consistency and the actual carbon buyer specification.

ВыхадQualified material-to-product basis

02

Thermal route

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

ВыхадConnected carbon-production flow

03

Energy demand

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

ВыхадPreliminary energy-use boundary

04

Evidence and acceptance

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

ВыхадProject acceptance and evidence plan

ПРАЕКТ FAQ

Пытанні, якія трэба вырашыць перад канфігурацыяй.

Адказы вызначаюць інжынерную мяжу; яны не замяняюць рэпрэзентатыўнае тэсціраванне матэрыялу або мясцовы агляд адпаведнасці.

What changes the continuous carbonization configuration?

Biomass type, вільгаць, particle size, ash, target carbon specification, operating hours, 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?

няма. Eligibility depends on feedstock traceability, operating evidence, methodology, 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.

ТЭХНІЧНЫ АГЛЯД ПРАЕКТА

Перад выбарам абсталявання вызначыцеся з матэрыялам.

Падзяліцеся рэпрэзентатыўным апісаннем матэрыялу, даступны аб'ём, статус сайта і мэтавыя вынікі. YUSHUNXIN будзе выкарыстоўваць гэтыя факты для падрыхтоўкі адпаведнага абмеркавання межаў працэсу і канфігурацыі.

Пачаць агляд праекта