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.
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:
- Primary Carbonization: Biomass feedstock enters the continuous carbonization reactor, where controlled pyrolysis at 450-650°C produces biochar and releases volatile syngas.
- 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.
- 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.
- 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.
- 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.
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.

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.
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.
- 01Dry and size the biomass
- 02Continuous oxygen-limited carbonization
- 03Separate dust and condensable fractions
- 04Clean and condition process gas
- 05Return heat to the carbonizer first
- 06Evaluate steam, power or combined heat-and-power use
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.
Бәйләнгән җиһаз чикләрен карагыз.
Белешмә визуаллар иртә урнашу турында сөйләшүне хуплый. Соңгы җиһаз, аранжировка һәм интерфейслар проект материалыннан һәм сайттан расланган.
Проект фактларын җиһазлар исемлегенә тәрҗемә итегез.
Бу белешмә матрица карар логикасын күрсәтә. Соңгы күләмнәр, модельләр һәм интерфейслар расланган проект тәкъдимендә.
| Система блокы | Типик масштаб | Конфигурация нигезе |
|---|---|---|
| Biomass preparation | Drying, size control, storage and metered feeding | Дым, density and seasonal consistency |
| Карбонизация | Continuous reactor, atmosphere control and thermal profile | Target carbon specification |
| Product handling | Мөһерләнгән суыту, 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 |
| Энергия интеграциясе | Internal heat return, optional boiler, generator or user interface | Verified energy balance and demand match |
Проектны кирәкле дәлилләр булганда гына алга җибәрегез.
Eachәр капка клиент турында мәгълүматны киләсе карар өчен билгеләнгән техник яки коммерция нәтиҗәләренә әйләндерә.
Biomass and product
Confirm biomass consistency and the actual carbon buyer specification.
ЧыгышQualified material-to-product basisThermal route
Define drying, sizing, carbonization, cooling and quality sampling.
ЧыгышConnected carbon-production flowEnergy demand
Match process heat with a verified nearby steam, heat or power demand.
ЧыгышPreliminary energy-use boundaryEvidence and acceptance
Agree operating records, tests, emissions and any methodology review.
ЧыгышProject acceptance and evidence planКонфигурация 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.
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.
Continuous carbonization and energy integration
Select the carbonization class from prepared volumetric feed, bulk density, дым, target carbon and energy-use boundary.
Килүче материал
Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.
Көтелгән нәтиҗәләр
Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.
Проект интерфейслары
Drying/preparation, мөһерләнгән туклану, carbonization, gas treatment/combustion, cooling, саклау, fire control and optional heat recovery.
Сайланган процесс чикләренә туры килгән рәтне кулланыгыз.
| Каталог сылтамасы | Потенциал | Көч | Физик конверт | Керелгән чик |
|---|---|---|---|---|
| SXTD820Даими карбонизация | 1–2 м³ / с | 95 кВт | 600 m² каталог җир сылтамасы | Биомассаның өзлексез карбонизация линиясе |
| SXTD1200Даими карбонизация | 3–5 м³ / с | 110 кВт | 650 m² каталог җир сылтамасы | Биомассаның өзлексез карбонизация линиясе |
| SXTD1500Даими карбонизация | 5–8 м³ / с | 153 кВт | 800 m² каталог җир сылтамасы | Биомассаның өзлексез карбонизация линиясе |
| SXTD1800Даими карбонизация | 8–10 м³ / с | 178 кВт | 800 m² каталог җир сылтамасы | Биомассаның өзлексез карбонизация линиясе |
| SXTD2000 - 10–14 классДаими карбонизация | 10–14 м³ / с | 190 кВт | 850 m² каталог җир сылтамасы | Каталог бу класс өчен SXTD2000 бастыра |
| SXTD2000 - 14–17 классДаими карбонизация | 14–17 м³ / с | 220 кВт | 850 m² каталог җир сылтамасы | Каталог 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
- Вәкил материал фотолары, спецификацияләр һәм булган үрнәк.
- Кирәкле сыйдырышлык һәм сменага сәгатьләр, көнгә смена һәм эш көннәре.
- Максатлы нәтиҗәләр, сайлау ысулы һәм түбән агымдагы кабул итүче таләпләре.
- Сайт иле, булган көч, ягулык, су, кысылган һава һәм төзелеш чикләре.
- Localирле әйләнә-тирә мохит, ут, саклау һәм хезмәт-куркынычсызлык таләпләре.
- Тапшыру чикләре: җиһаз, макет, урнаштыру, тапшыру һәм укыту.