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, 에너지 균형, 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, 작동 안정성, 가스 청소, 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, 황, 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
수분, 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.
연결된 장비 경계 보기.
참조 시각적 자료는 초기 레이아웃 논의를 지원합니다.. 최종 장비, 배치 및 인터페이스는 프로젝트 자료 및 현장에서 확인됩니다..
프로젝트 정보를 장비 목록으로 변환.
이 참조 매트릭스는 결정 논리를 보여줍니다.. 최종 수량, 모델과 인터페이스는 승인된 프로젝트 제안에 속합니다..
| 시스템 블록 | 일반적인 범위 | 구성기준 |
|---|---|---|
| Biomass preparation | 건조, size control, storage and metered feeding | 수분, density and seasonal consistency |
| 탄화 | 연속반응기, atmosphere control and thermal profile | Target carbon specification |
| Product handling | 밀봉된 냉각, 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 |
| 에너지 통합 | Internal heat return, optional boiler, generator or user interface | Verified energy balance and demand match |
필요한 증거가 있는 경우에만 프로젝트를 진행하세요..
각 게이트는 고객 정보를 다음 결정을 위해 정의된 기술 또는 상업적 출력으로 전환합니다..
Biomass and product
Confirm biomass consistency and the actual carbon buyer specification.
산출Qualified material-to-product basisThermal route
Define drying, sizing, carbonization, cooling and quality sampling.
산출Connected carbon-production flowEnergy demand
Match process heat with a verified nearby steam, heat or power demand.
산출Preliminary energy-use boundaryEvidence and acceptance
Agree operating records, tests, emissions and any methodology review.
산출Project acceptance and evidence plan구성 전에 해결해야 할 질문.
답변은 엔지니어링 경계를 정의합니다; 이는 대표적인 재료 테스트 또는 현지 규정 준수 검토를 대체하지 않습니다..
What changes the continuous carbonization configuration?
Biomass type, 수분, 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?
아니요. 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.
장비를 선택하기 전에 재료를 정의하십시오..
대표적인 자료 설명 공유, 사용 가능한 볼륨, 사이트 상태 및 대상 출력. YUSHUNXIN은 이러한 사실을 사용하여 관련 프로세스 경계 및 구성 논의를 준비합니다..
Continuous carbonization and energy integration
Select the carbonization class from prepared volumetric feed, bulk density, 수분, target carbon and energy-use boundary.
들어오는 재료
Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.
예상 출력
Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.
프로젝트 인터페이스
Drying/preparation, 봉인된 먹이, carbonization, gas treatment/combustion, 냉각, storage, fire control and optional heat recovery.
선택한 프로세스 경계와 일치하는 행만 사용.
| 카탈로그 참조 | 용량 | 힘 | 물리적 봉투 | 포함된 경계 |
|---|---|---|---|---|
| SXTD820Continuous carbonization | 1–2 m³/h | 95 kW | 600 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1200Continuous carbonization | 3–5 m³/h | 110 kW | 650 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1500Continuous carbonization | 5–8 m³/h | 153 kW | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1800Continuous carbonization | 8–10 m³/h | 178 kW | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD2000 - 10–14 classContinuous carbonization | 10–14 m³/h | 190 kW | 850 m² catalogue land reference | Catalogue prints SXTD2000 for this class |
| SXTD2000 - 14–17 classContinuous carbonization | 14–17 m³/h | 220 kW | 850 m² catalogue land reference | Catalogue repeats SXTD2000; final model code requires written confirmation |
구성 규칙: 카탈로그 용량은 계획 참조입니다.. 안정적인 처리량, 설치/작동 전원, 발자국, 회복, 청정, 배출 및 유틸리티 수요에는 승인된 장비 목록이 필요합니다., 대표 자료 및 서면 승인 조건.
구성 및 견적 전에 필요한 정보
- 대표자료사진, 사양 및 사용 가능한 샘플.
- 필요 용량 + 교대당 시간, 하루 교대근무수 및 근무일수.
- 목표 출력, 샘플링 방법 및 다운스트림 수신기 요구 사항.
- 사이트 국가, 사용 가능한 전력, 연료, 물, 압축 공기 및 건물 한계.
- 지역 환경, 불, 보관 및 산업 안전 요구 사항.
- 요청된 배송 범위: 장비, 공들여 나열한 것, 설치, 시운전 및 교육.