С2: 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, energy balance, 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, operating stability, 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, сумпор, фосфор, 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
Влага, 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.
See the connected equipment boundary.
Reference visuals support early layout discussion. Final equipment, arrangement and interfaces are confirmed from the project material and site.
Преведите чињенице о пројекту у листу опреме.
Ова референтна матрица показује логику одлучивања. Коначне количине, модели и интерфејси припадају одобреном предлогу пројекта.
| Системски блок | Типичан обим | Основа конфигурације |
|---|---|---|
| Biomass preparation | Сушење, size control, storage and metered feeding | Влага, density and seasonal consistency |
| Карбонизација | 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 |
| Energy integration | Internal heat return, optional boiler, generator or user interface | Verified energy balance and demand match |
Унапредите пројекат само када су потребни докази доступни.
Свака капија претвара информације о клијентима у дефинисани технички или комерцијални резултат за следећу одлуку.
Biomass and product
Confirm biomass consistency and the actual carbon buyer specification.
ИзлазQualified material-to-product basisThermal route
Define drying, sizing, carbonization, cooling and quality sampling.
ИзлазConnected carbon-production flowEnergy demand
Match process heat with a verified nearby steam, heat or power demand.
ИзлазPreliminary energy-use boundaryEvidence and acceptance
Agree operating records, tests, emissions and any methodology review.
ИзлазProject acceptance and evidence planПитања која треба решити пре конфигурисања.
Одговори дефинишу инжењерску границу; они не замењују репрезентативно тестирање материјала или локални преглед усклађености.
What changes the continuous carbonization configuration?
Biomass type, влаге, 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?
бр. 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.
Дефинишите материјал пре избора опреме.
Поделите репрезентативни опис материјала, расположива запремина, статус локације и циљне резултате. ИУСХУНКСИН ће користити те чињенице да припреми релевантну дискусију о границама процеса и конфигурацији.
Continuous carbonization and energy integration
Select the carbonization class from prepared volumetric feed, bulk density, влаге, target carbon and energy-use boundary.
Долазни материјал
Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.
Очекивани резултати
Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.
Интерфејси пројекта
Drying/preparation, sealed feeding, carbonization, gas treatment/combustion, cooling, складиштење, fire control and optional heat recovery.
Користите само ред који одговара изабраној граници процеса.
| Референца каталога | Капацитет | Повер | Физички омотач | Укључена граница |
|---|---|---|---|---|
| СКСТД820Континуирана карбонизација | 1–2 м³/х | 95 кВ | 600 м² каталог земљишта референца | Припремљена линија за континуирану карбонизацију биомасе |
| СКСТД1200Континуирана карбонизација | 3–5 м³/х | 110 кВ | 650 м² каталог земљишта референца | Припремљена линија за континуирану карбонизацију биомасе |
| СКСТД1500Континуирана карбонизација | 5–8 м³/х | 153 кВ | 800 м² каталог земљишта референца | Припремљена линија за континуирану карбонизацију биомасе |
| СКСТД1800Континуирана карбонизација | 8–10 м³/х | 178 кВ | 800 м² каталог земљишта референца | Припремљена линија за континуирану карбонизацију биомасе |
| СКСТД2000 - 10–14 разредКонтинуирана карбонизација | 10–14 м³/х | 190 кВ | 850 м² каталог земљишта референца | Каталог штампа СКСТД2000 за ову класу |
| СКСТД2000 - 14–17 разредКонтинуирана карбонизација | 14–17 м³/х | 220 кВ | 850 м² каталог земљишта референца | Каталог понавља СКСТД2000; коначан код модела захтева писмену потврду |
Правило конфигурације: каталошки капацитет је референца за планирање. Стабилан проток, инсталирана/радна снага, отисак стопала, опоравак, чистота, емисије и потражња за комуналије захтевају одобрену листу опреме, репрезентативни материјал и писани услови прихватања.
Потребне информације пре конфигурације и понуде
- Фотографије репрезентативног материјала, спецификације и расположиви узорак.
- Потребан капацитет плус сати по смени, смене по дану и радни дани.
- Циљни резултати, метода узорковања и захтеви пријемника у низводном току.
- Држава сајта, расположива снага, гориво, воде, компримовани ваздух и границе зграде.
- Локално окружење, ватра, захтеви за складиштење и безбедност на раду.
- Тражена граница испоруке: опреме, распоред, инсталација, пуштање у рад и обуку.