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.

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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, 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.

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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, 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.

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

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.

참조 구성

프로젝트 정보를 장비 목록으로 변환.

이 참조 매트릭스는 결정 논리를 보여줍니다.. 최종 수량, 모델과 인터페이스는 승인된 프로젝트 제안에 속합니다..

시스템 블록일반적인 범위구성기준
Biomass preparation건조, size control, storage and metered feeding수분, density and seasonal consistency
탄화연속반응기, atmosphere control and thermal profileTarget carbon specification
Product handling밀봉된 냉각, sizing, storage and sample pointsOxidation, dust and product quality
Gas and condensablesDust separation, condensation and gas conditioningTar, moisture and intended heat route
에너지 통합Internal heat return, optional boiler, generator or user interfaceVerified energy balance and demand match
단계별 결정 경로

필요한 증거가 있는 경우에만 프로젝트를 진행하세요..

각 게이트는 고객 정보를 다음 결정을 위해 정의된 기술 또는 상업적 출력으로 전환합니다..

01

Biomass and product

Confirm biomass consistency and the actual carbon buyer specification.

산출Qualified material-to-product basis
02

Thermal route

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

산출Connected carbon-production flow
03

Energy demand

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

산출Preliminary energy-use boundary
04

Evidence and acceptance

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

산출Project acceptance and evidence plan
프로젝트 FAQ

구성 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.

프로젝트 엔지니어링 검토

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..

프로젝트 검토 시작
카탈로그에 맞춰진 엔지니어링 기반

Continuous carbonization and energy integration

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

01

들어오는 재료

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

02

예상 출력

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

03

프로젝트 인터페이스

Drying/preparation, 봉인된 먹이, carbonization, gas treatment/combustion, 냉각, storage, fire control and optional heat recovery.

모델 및 범위 등록

선택한 프로세스 경계와 일치하는 행만 사용.

카탈로그 참조용량힘물리적 봉투포함된 경계
SXTD820Continuous carbonization1–2 m³/h95 kW600 m² catalogue land referencePrepared biomass continuous carbonization line
SXTD1200Continuous carbonization3–5 m³/h110 kW650 m² catalogue land referencePrepared biomass continuous carbonization line
SXTD1500Continuous carbonization5–8 m³/h153 kW800 m² catalogue land referencePrepared biomass continuous carbonization line
SXTD1800Continuous carbonization8–10 m³/h178 kW800 m² catalogue land referencePrepared biomass continuous carbonization line
SXTD2000 - 10–14 classContinuous carbonization10–14 m³/h190 kW850 m² catalogue land referenceCatalogue prints SXTD2000 for this class
SXTD2000 - 14–17 classContinuous carbonization14–17 m³/h220 kW850 m² catalogue land referenceCatalogue 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

  1. 대표자료사진, 사양 및 사용 가능한 샘플.
  2. 필요 용량 + 교대당 시간, 하루 교대근무수 및 근무일수.
  3. 목표 출력, 샘플링 방법 및 다운스트림 수신기 요구 사항.
  4. 사이트 국가, 사용 가능한 전력, 연료, 물, 압축 공기 및 건물 한계.
  5. 지역 환경, 불, 보관 및 산업 안전 요구 사항.
  6. 요청된 배송 범위: 장비, 공들여 나열한 것, 설치, 시운전 및 교육.