S2: Trochrinnende karbonisaasje & Char-Gas Co-generation Solution
Us trochgeande karbonisaasjesysteem konvertearret biomassa en organysk ôffal yn biochar fan hege kwaliteit, wylst tagelyk brânber syngas genereart foar ko-generaasje fan enerzjy. It ko-generaasjeproses fan char-gas berikt folsleine sirkulaasje fan termyske enerzjy - de waarmte dy't frijkomt by karbonisaasje wurdt fêstlein en opnij brûkt, drastysk ferbetterjen fan totale enerzjy-effisjinsje.
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-generaasje - Thermal Circulation Logic
It char-gas ko-generaasjesysteem wurket op in sletten-loop termyske sirkulaasjemodel:
- Primêre karbonisaasje: Biomassa feedstock komt de trochgeande karbonisaasjereaktor yn, wêrby't kontroleare pyrolyse by 450-650 ° C biochar produseart en flechtich syngas frijlit.
- Syngas ferbaarning: It waarme syngas wurdt direkt yn in gasferbaarningskeamer brocht, it opwekken fan hege temperatuer flue gas (800-1000°C) foar enerzjygeneraasje fia in stoomturbine of ORC-ienheid.
- Waste Heat Recovery: Exhaust waarmte fan macht generaasje wurdt fêstlein troch economizers en waarmte Exchangers, preheating ynkommende feedstock en drogen biomassa - ferminderjen focht ynhâld hjirûnder 15% foardat jo de reaktor yngeane.
- Termyske recirkulaasje: In part fan it hite flue gas wurdt omlaat nei de carbonization reaktor jas, behâld fan optimale pyrolysis temperatuer sûnder eksterne brânstof input nei opstarten.
- 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, 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
Moisture, 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.
Translate project facts into an equipment list.
This reference matrix shows the decision logic. Final quantities, models and interfaces belong in the approved project proposal.
| System block | Typical scope | Configuration basis |
|---|---|---|
| Biomass preparation | Drying, size control, storage and metered feeding | Moisture, density and seasonal consistency |
| Karbonisaasje | 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 |
Foarút it projekt allinich as it fereaske bewiis beskikber is.
Elke poarte feroaret klantynformaasje yn in definieare technyske of kommersjele útfier foar it folgjende beslút.
Biomass and product
Confirm biomass consistency and the actual carbon buyer specification.
UtfierQualified material-to-product basisThermal route
Define drying, sizing, carbonization, cooling and quality sampling.
UtfierConnected carbon-production flowEnergy demand
Match process heat with a verified nearby steam, heat or power demand.
UtfierPreliminary energy-use boundaryEvidence and acceptance
Agree operating records, tests, emissions and any methodology review.
UtfierProject acceptance and evidence planFragen om op te lossen foar konfiguraasje.
Antwurden definiearje de engineering grins; se net ferfange represintative materiaal testen of lokale neilibjen review.
What changes the continuous carbonization configuration?
Biomass type, focht, 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?
Nee. 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.
Definiearje it materiaal foardat jo de apparatuer selektearje.
Diel in represintative materiaal beskriuwing, beskikber folume, sitestatus en doelútgongen. YUSHUNXIN sil dizze feiten brûke om de oanbelangjende prosesgrins en konfiguraasjediskusje te meitsjen.
Continuous carbonization and energy integration
Select the carbonization class from prepared volumetric feed, bulk density, focht, target carbon and energy-use boundary.
Ynkommende materiaal
Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.
Ferwachte útgongen
Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.
Projekt ynterfaces
Drying/preparation, sealed feeding, carbonization, gas treatment/combustion, cooling, storage, fire control and optional heat recovery.
Brûk allinich de rige dy't oerienkomt mei de selektearre prosesgrins.
| Katalogusferwizing | Kapasiteit | Krêft | Fysike envelope | Ynbegrepen grins |
|---|---|---|---|---|
| SCTD820Trochrinnende karbonisaasje | 1-2 m³/h | 95 kW | 600 m² katalogus lânferwizing | Tariede biomassa trochgeande carbonization line |
| SCTD1200Trochrinnende karbonisaasje | 3-5 m³/h | 110 kW | 650 m² katalogus lânferwizing | Tariede biomassa trochgeande carbonization line |
| SCTD1500Trochrinnende karbonisaasje | 5-8 m³/h | 153 kW | 800 m² katalogus lânferwizing | Tariede biomassa trochgeande carbonization line |
| SCTD1800Trochrinnende karbonisaasje | 8-10 m³/h | 178 kW | 800 m² katalogus lânferwizing | Tariede biomassa trochgeande carbonization line |
| SCTD2000 - 10-14 klasseTrochrinnende karbonisaasje | 10-14 m³/h | 190 kW | 850 m² katalogus lânferwizing | Katalogus printsjes SXTD2000 foar dizze klasse |
| SCTD2000 - 14-17 klasseTrochrinnende karbonisaasje | 14-17 m³/h | 220 kW | 850 m² katalogus lânferwizing | Katalogus werhellet SXTD2000; finale model koade fereasket skriftlike befêstiging |
Konfiguraasje regel: katalogus kapasiteit is in planning referinsje. Stabiele trochstreaming, ynstallearre / bestjoeringssysteem macht, fuotprint, herstel, suverens, útstjit en nut fraach fereaskje de goedkard apparatuer list, represintatyf materiaal en skriftlike akseptaasjebetingsten.
Ynformaasje nedich foar konfiguraasje en offerte
- Representative materiaal foto's, spesifikaasjes en beskikber sample.
- Required kapasiteit plus oeren per shift, ferskowings per dei en wurkdagen.
- Doelútgongen, sampling metoade en streamôfwerts ûntfanger easken.
- Site lân, beskikber macht, brânstof, wetter, komprimearre loft en gebou grinzen.
- Lokale miljeu, fjoer, easken foar opslach en beropsfeiligens.
- Oanfrege leveringsgrins: apparatuer, opmaak, ynstallaasje, oplieding en oplieding.