S2: Carboneiddio Parhaus & Ateb Cydgynhyrchu Nwy Char
Mae ein system garboneiddio barhaus yn trosi biomas a gwastraff organig yn fio-olosg o ansawdd uchel tra'n cynhyrchu syngas hylosg ar yr un pryd ar gyfer cydgynhyrchu pŵer.. Mae'r broses gyd-gynhyrchu nwy golosg yn cyflawni cylchrediad ynni thermol cyflawn - mae'r gwres a ryddheir yn ystod carboni yn cael ei ddal a'i ailddefnyddio, gwella effeithlonrwydd ynni cyffredinol yn ddramatig.
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 & Rheoli Asedau Carbon
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.
Cydgynhyrchu Nwy Char - Rhesymeg Cylchrediad Thermol
Mae'r system cydgynhyrchu golosg-nwy yn gweithredu ar fodel cylchrediad thermol dolen gaeedig:
- Carboneiddio Cynradd: Mae porthiant biomas yn mynd i mewn i'r adweithydd carbonoli parhaus, lle mae pyrolysis rheoledig ar 450-650°C yn cynhyrchu bio-olosg ac yn rhyddhau syngas anweddol.
- Hylosgiad Syngas: Mae'r syngas poeth yn cael ei fwydo'n uniongyrchol i siambr hylosgi nwy, cynhyrchu nwy ffliw tymheredd uchel (800-1000°C) ar gyfer cynhyrchu pŵer trwy dyrbin stêm neu uned ORC.
- Adfer Gwres Gwastraff: Mae gwres gwacáu o gynhyrchu pŵer yn cael ei ddal trwy economizers a chyfnewidwyr gwres, cynhesu porthiant sy'n dod i mewn ymlaen llaw a sychu biomas — lleihau'r cynnwys lleithder islaw 15% cyn mynd i mewn i'r adweithydd.
- Ailgylchrediad Thermol: Mae cyfran o'r nwy ffliw poeth yn cael ei ailgyfeirio i siaced yr adweithydd carbonization, cynnal y tymheredd pyrolysis gorau posibl heb fewnbwn tanwydd allanol ar ôl cychwyn.
- 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, sylffwr, 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
Lleithder, 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.
Gweler ffin yr offer cysylltiedig.
Mae delweddau cyfeiriol yn cefnogi trafodaeth gynnar ar y cynllun. Offer terfynol, trefniant a rhyngwynebau yn cael eu cadarnhau o ddeunydd y prosiect a safle.
Trosi ffeithiau prosiect yn rhestr offer.
Mae'r matrics cyfeirio hwn yn dangos y rhesymeg penderfyniad. Meintiau terfynol, mae modelau a rhyngwynebau yn perthyn i'r cynnig prosiect cymeradwy.
| Bloc system | Cwmpas nodweddiadol | Sail cyfluniad |
|---|---|---|
| Biomass preparation | Drying, size control, storage and metered feeding | Lleithder, density and seasonal consistency |
| Carboneiddio | 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 |
Symudwch y prosiect ymlaen dim ond pan fydd y dystiolaeth ofynnol ar gael.
Mae pob giât yn troi gwybodaeth cwsmeriaid yn allbwn technegol neu fasnachol diffiniedig ar gyfer y penderfyniad nesaf.
Biomass and product
Confirm biomass consistency and the actual carbon buyer specification.
AllbwnQualified material-to-product basisLlwybr thermol
Define drying, sizing, carbonization, cooling and quality sampling.
AllbwnConnected carbon-production flowEnergy demand
Match process heat with a verified nearby steam, heat or power demand.
AllbwnPreliminary energy-use boundaryEvidence and acceptance
Agree operating records, tests, emissions and any methodology review.
AllbwnProject acceptance and evidence planCwestiynau i'w datrys cyn ffurfweddu.
Mae'r atebion yn diffinio'r ffin peirianneg; nid ydynt yn disodli profion deunydd cynrychioliadol nac adolygiad cydymffurfio lleol.
What changes the continuous carbonization configuration?
Biomass type, lleithder, 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?
Nac ydw. 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.
Diffiniwch y deunydd cyn dewis yr offer.
Rhannu disgrifiad deunydd cynrychioliadol, cyfaint sydd ar gael, statws safle ac allbynnau targed. Bydd YUSHUNXIN yn defnyddio'r ffeithiau hynny i baratoi'r drafodaeth ffin broses a chyfluniad perthnasol.
Continuous carbonization and energy integration
Select the carbonization class from prepared volumetric feed, bulk density, lleithder, target carbon and energy-use boundary.
Deunydd sy'n dod i mewn
Sawdust, rice husk, straw, shell or other biomass; particle size, full/air-dry moisture, ash and bulk density.
Allbynnau disgwyliedig
Biochar and project-specific gas/heat streams; carbon properties require representative laboratory and stable-run data.
Rhyngwynebau prosiect
Drying/preparation, sealed feeding, carbonization, gas treatment/combustion, cooling, storfa, fire control and optional heat recovery.
Defnyddiwch y rhes sy'n cyfateb i ffin y broses a ddewiswyd yn unig.
| Cyfeirnod catalog | Gallu | Grym | Amlen gorfforol | Ffin wedi'i chynnwys |
|---|---|---|---|---|
| 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 |
Rheol cyfluniad: mae capasiti catalog yn gyfeirnod cynllunio. Trwybwn sefydlog, pŵer gosod / gweithredu, ôl troed, adferiad, purdeb, mae angen y rhestr offer cymeradwy ar allyriadau a galw am gyfleustodau, deunydd cynrychioliadol ac amodau derbyn ysgrifenedig.
Gwybodaeth sydd ei hangen cyn ffurfweddu a dyfynbris
- Lluniau deunydd cynrychioliadol, manylebau a sampl sydd ar gael.
- Capasiti gofynnol ynghyd ag oriau fesul sifft, shifftiau y dydd a diwrnodau gweithredu.
- Allbynnau targed, dull samplu a gofynion derbynnydd i lawr yr afon.
- Gwlad y safle, pŵer sydd ar gael, tanwydd, dwr, aer cywasgedig a therfynau adeiladu.
- Amgylchedd lleol, tân, gofynion storio a diogelwch galwedigaethol.
- Ffin dosbarthu y gofynnwyd amdani: offer, gosodiad, gosod, comisiynu a hyfforddi.