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, энергия балансы, 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, эш тотрыклылыгы, 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.

Reference layout for a continuous thermal processing system
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, күкерт, 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

Дым, 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.

Белешмә конфигурациясе

Проект фактларын җиһазлар исемлегенә тәрҗемә итегез.

Бу белешмә матрица карар логикасын күрсәтә. Соңгы күләмнәр, модельләр һәм интерфейслар расланган проект тәкъдимендә.

Система блокыТипик масштабКонфигурация нигезе
Biomass preparationDrying, size control, storage and metered feedingДым, density and seasonal consistency
КарбонизацияContinuous reactor, atmosphere control and thermal profileTarget carbon specification
Product handlingМөһерләнгән суыту, sizing, storage and sample pointsOxidation, dust and product quality
Gas and condensablesDust separation, condensation and gas conditioningTar, moisture and intended heat route
Энергия интеграциясеInternal heat return, optional boiler, generator or user interfaceVerified energy balance and demand match
Этап-карар кабул итү юлы

Проектны кирәкле дәлилләр булганда гына алга җибәрегез.

Eachәр капка клиент турында мәгълүматны киләсе карар өчен билгеләнгән техник яки коммерция нәтиҗәләренә әйләндерә.

01

Biomass and product

Confirm biomass consistency and the actual carbon buyer specification.

ЧыгышQualified material-to-product basis
02

Thermal route

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

ЧыгышConnected carbon-production flow
03

Energy demand

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

ЧыгышPreliminary energy-use boundary
04

Evidence and acceptance

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

ЧыгышProject acceptance and evidence plan
Проект сораулары

Конфигурация алдыннан чишү сораулары.

Ansаваплар инженерлык чикләрен билгели; алар материаль тестны яки җирле туры килүне тикшерүне алыштырмыйлар.

What changes the continuous carbonization configuration?

Biomass type, дым, 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?

.К. 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.

Проект инженериясе

Equipmentиһазны сайлаганчы материалны билгеләгез.

Вәкиллек материал тасвирламасы белән уртаклашыгыз, булган күләм, сайт статусы һәм максатлы нәтиҗәләр. USШУНХИН бу фактларны тиешле процесс чикләрен һәм конфигурация дискуссиясен әзерләү өчен кулланачак.

Проектны карау
КАТАЛОГ-АЛИГНИЯ ЭНЖЕНЕРИНГ БАСЫ

Continuous carbonization and energy integration

Select the carbonization class from prepared volumetric feed, bulk density, дым, target carbon and energy-use boundary.

01

Килүче материал

Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.

02

Көтелгән нәтиҗәләр

Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.

03

Проект интерфейслары

Drying/preparation, мөһерләнгән туклану, carbonization, gas treatment/combustion, cooling, саклау, fire control and optional heat recovery.

Модель һәм скоп теркәүчесе

Сайланган процесс чикләренә туры килгән рәтне кулланыгыз.

Каталог сылтамасыПотенциалКөчФизик конвертКерелгән чик
SXTD820Даими карбонизация1–2 м³ / с95 кВт600 m² каталог җир сылтамасыБиомассаның өзлексез карбонизация линиясе
SXTD1200Даими карбонизация3–5 м³ / с110 кВт650 m² каталог җир сылтамасыБиомассаның өзлексез карбонизация линиясе
SXTD1500Даими карбонизация5–8 м³ / с153 кВт800 m² каталог җир сылтамасыБиомассаның өзлексез карбонизация линиясе
SXTD1800Даими карбонизация8–10 м³ / с178 кВт800 m² каталог җир сылтамасыБиомассаның өзлексез карбонизация линиясе
SXTD2000 - 10–14 классДаими карбонизация10–14 м³ / с190 кВт850 m² каталог җир сылтамасыКаталог бу класс өчен SXTD2000 бастыра
SXTD2000 - 14–17 классДаими карбонизация14–17 м³ / с220 кВт850 m² каталог җир сылтамасыКаталог SXTD2000 кабатлый; соңгы модель коды язма раслауны таләп итә

Конфигурация кагыйдәсе: каталог сыйдырышлыгы - планлаштыру белешмәсе. Тотрыклы үткәрү, урнаштырылган / эш көче, эз, торгызу, чисталык, чыгару һәм файдалы сорау расланган җиһазлар исемлеген таләп итә, вәкиллекле материал һәм язма кабул итү шартлары.

Конфигурация һәм цитаталар алдыннан кирәкле мәгълүмат

  1. Вәкил материал фотолары, спецификацияләр һәм булган үрнәк.
  2. Кирәкле сыйдырышлык һәм сменага сәгатьләр, көнгә смена һәм эш көннәре.
  3. Максатлы нәтиҗәләр, сайлау ысулы һәм түбән агымдагы кабул итүче таләпләре.
  4. Сайт иле, булган көч, ягулык, су, кысылган һава һәм төзелеш чикләре.
  5. Localирле әйләнә-тирә мохит, ут, саклау һәм хезмәт-куркынычсызлык таләпләре.
  6. Тапшыру чикләре: җиһаз, макет, урнаштыру, тапшыру һәм укыту.