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, тавозуни энергетикӣ, 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, устувории амалиёт, тоза кардани газ, 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, sulfur, 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
Рутубат, 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.
Сарҳади таҷҳизоти пайвастшударо бубинед.
Визуалиҳои истинод муҳокимаи тарҳбандии барвақтро дастгирӣ мекунанд. Таҷҳизоти ниҳоӣ, Тартиб ва интерфейсҳо аз мавод ва сайти лоиҳа тасдиқ карда мешаванд.
Далелҳои лоиҳаро ба рӯйхати таҷҳизот тарҷума кунед.
Ин матритсаи истинод мантиқи қарорро нишон медиҳад. Миқдори ниҳоӣ, моделҳо ва интерфейсҳо ба пешниҳоди лоиҳаи тасдиқшуда тааллуқ доранд.
| Блоки системавӣ | Доираи маъмулӣ | Асоси конфигуратсия |
|---|---|---|
| Biomass preparation | Drying, size control, storage and metered feeding | Рутубат, density and seasonal consistency |
| Карбонизатсия | 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 |
| Интегратсияи энергетикӣ | Internal heat return, optional boiler, generator or user interface | Verified energy balance and demand match |
Лоиҳаро танҳо дар сурати мавҷуд будани далелҳои зарурӣ пешбарӣ кунед.
Ҳар як дарвоза маълумоти муштариро ба натиҷаи муайяншудаи техникӣ ё тиҷоратӣ барои қарори навбатӣ табдил медиҳад.
Biomass and product
Confirm biomass consistency and the actual carbon buyer specification.
НатиҷаQualified material-to-product basisРоҳи гармидиҳӣ
Define drying, sizing, carbonization, cooling and quality sampling.
НатиҷаConnected carbon-production flowEnergy demand
Match process heat with a verified nearby steam, heat or power demand.
НатиҷаPreliminary energy-use boundaryEvidence and acceptance
Agree operating records, tests, emissions and any methodology review.
НатиҷаProject acceptance and evidence planСаволҳое, ки бояд пеш аз конфигуратсия ҳал карда шаванд.
Ҷавобҳо сарҳади муҳандисиро муайян мекунанд; онҳо санҷиши маводи намояндагӣ ё баррасии мувофиқати маҳаллиро иваз намекунанд.
What changes the continuous carbonization configuration?
Biomass type, намнокй, 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?
Не. Eligibility depends on feedstock traceability, operating evidence, методология, 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.
Пеш аз интихоби таҷҳизот, маводро муайян кунед.
Тавсифи маводро мубодила кунед, ҳаҷми дастрас, ҳолати сайт ва натиҷаҳои ҳадаф. ЮШУНСИН ин далелҳоро барои омода кардани сарҳади раванд ва муҳокимаи конфигуратсияи дахлдор истифода хоҳад кард.
Continuous carbonization and energy integration
Select the carbonization class from prepared volumetric feed, bulk density, намнокй, target carbon and energy-use boundary.
Маводи воридотӣ
Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.
Натиҷаҳои пешбинишуда
Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.
Интерфейси лоиҳа
Drying/preparation, sealed feeding, carbonization, gas treatment/combustion, хунуккунӣ, нигоҳдорӣ, fire control and optional heat recovery.
Танҳо сатри мувофиқи сарҳади раванди интихобшударо истифода баред.
| Маълумотнома каталог | Иқтидор | Қувва | Лифофаи ҷисмонӣ | Сарҳади дохилшуда |
|---|---|---|---|---|
| SXTD820Continuous carbonization | 1–2 m³/h | 95 кВт | 600 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1200Continuous carbonization | 3–5 m³/h | 110 кВт | 650 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1500Continuous carbonization | 5–8 m³/h | 153 кВт | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1800Continuous carbonization | 8–10 m³/h | 178 кВт | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD2000 - 10–14 classContinuous carbonization | 10–14 m³/h | 190 кВт | 850 m² catalogue land reference | Catalogue prints SXTD2000 for this class |
| SXTD2000 - 14–17 classContinuous carbonization | 14–17 m³/h | 220 кВт | 850 m² catalogue land reference | Catalogue repeats SXTD2000; final model code requires written confirmation |
Қоидаи конфигуратсия: иқтидори каталоги истинод ба нақша аст,. Ҳаҷми мӯътадил, қудрати насбшуда/амалкунанда, изи по, барқароршавӣ, покӣ, партовҳо ва талаботи коммуналӣ рӯйхати таҷҳизоти тасдиқшударо талаб мекунанд, шартҳои қабули маводи намояндагӣ ва хаттӣ.
Маълумоте, ки пеш аз конфигуратсия ва иқтибос лозим аст
- Суратҳои маводҳои намояндагӣ, мушаххасот ва намунаи дастрас.
- Иқтидори зарурӣ плюс соат дар як смена, смена дар як рӯз ва рӯзҳои корӣ.
- Натиҷаҳои мақсаднок, усули интихоб ва талаботи қабулкунандаи поёноб.
- Кишвари сайт, қувваи дастрас, сӯзишворӣ, об, ҳаво фишурда ва ҳудуди бино.
- Муҳити зисти маҳаллӣ, оташ, талаботҳои нигоҳдорӣ ва бехатарии меҳнат.
- Сарҳади интиқоли дархостшуда: тачхизот, тарҳрезӣ, насб, ба истифода додан ва тайёр кардан.
