S2: Khabone e tsoelang pele & Tharollo ea Kopano ea Char-Gas

Sistimi ea rona e tsoelang pele ea carbonization e fetola biomass le litšila tsa manyolo hore e be biochar ea boleng bo holimo ha ka nako e ts'oanang e hlahisa li-syngas tse tukang bakeng sa ho kopanya motlakase.. Ts'ebetso ea co-generation ea char-gas e fihlella phepelo e felletseng ea matla a mocheso - mocheso o lokollotsoeng nakong ea carbonization oa tšoaroa ebe o sebelisoa hape., ka tsela e makatsang ho ntlafatsa ts'ebeliso ea matla ka kakaretso.

Carbon accounting boundary: Potential storage and avoided-emission effects depend on feedstock traceability, biochar properties, end use, tekanyo ea matla, the selected methodology and independent verification. No carbon-credit eligibility or emissions result is stated before project-specific review.

Kopa Tlhahlobo ea ROI

ESG & Taolo ea Letlotlo la Khabone

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

Sistimi ea co-generation ea char-gas e sebetsa ka mokhoa o koetsoeng oa ho potoloha ha mocheso:

  1. Carbonization ea mantlha: Biomass feedstock e kena ka har'a mochine o tsoelang pele oa carbonization, moo pyrolysis e laoloang ho 450-650 ° C e hlahisang biochar le ho ntša li-syngas tse feto-fetohang..
  2. Syngas Combustion: Li-syngas tse chesang li kenngoa ka ho toba ka kamoreng e tukang ea khase, ho hlahisa mocheso o phahameng wa mocheso wa mohatsela (800-1000°C) bakeng sa ho fehla motlakase ka mochini oa mouoane kapa yuniti ea ORC.
  3. Pheliso ea Mocheso oa litšila: Mocheso oa ho felloa ke matla o tsoang ho phepelo ea motlakase o ts'oaroa ka li-economizers le li-heaters tsa mocheso, preheating feedstock e kenang le ho omisa biomass - ho fokotsa mongobo ka tlase 15% pele o kena ka sekontiri.
  4. Recirculation ea mocheso: Karolo e 'ngoe ea khase e chesang e fetisetsoa ho baki ea carbonization reactor, ho boloka mocheso o nepahetseng oa pyrolysis ntle le ho kenya mafura ka ntle ka mor'a ho qala.
  5. Energy integration basis: Available gas and heat depend on feedstock moisture and composition, botsitso ba ho sebetsa, 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.

Kopa Tlhahlobo ea Mokoloto oa Carbon

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, sebabole, 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

Mongobo, 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.

TS'ELISO TIISETSO

Fetolela lintlha tsa morero lenaneng la lisebelisoa.

Matrix ena ea litšupiso e bonts'a mohopolo oa qeto. Lipalo tsa ho qetela, limotlelara le likhokahano li teng molemong oa projeke e amohetsoeng.

Thibelo ea tsamaisoSebaka se tloaelehilengMotheo oa tlhophiso
Biomass preparationDrying, size control, storage and metered feedingMongobo, density and seasonal consistency
CarbonizationContinuous reactor, atmosphere control and thermal profileTarget carbon specification
Product handlingPholiso e tiisitsoeng, sizing, storage and sample pointsOxidation, dust and product quality
Gas and condensablesDust separation, condensation and gas conditioningTar, moisture and intended heat route
Ho kopanya matlaInternal heat return, optional boiler, generator or user interfaceVerified energy balance and demand match
TSELA EA QETO E KHOTSOANG MOHATO

Tsoela pele ka morero feela ha bopaki bo hlokahalang bo le teng.

Monyako o mong le o mong o fetola tlhahisoleseding ea bareki hore e be tlhahiso e hlalositsoeng ea theknoloji kapa ea khoebo bakeng sa qeto e latelang.

01

Biomass and product

Confirm biomass consistency and the actual carbon buyer specification.

SephethoQualified material-to-product basis
02

Thermal route

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

SephethoConnected carbon-production flow
03

Energy demand

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

SephethoPreliminary energy-use boundary
04

Evidence and acceptance

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

SephethoProject acceptance and evidence plan
MORERO FAQ

Lipotso tse lokelang ho rarolloa pele ho tlhophiso.

Likarabo li hlalosa moeli oa boenjiniere; ha li nkele sebaka sa tlhahlobo ea lisebelisoa tse emelang kapa tlhahlobo ea boikamahanyo ea lehae.

What changes the continuous carbonization configuration?

Biomass type, mongobo, particle size, ash, target carbon specification, lihora tsa ts'ebetso, 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?

Che. 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.

TLHOKOMELISO EA MORORO

Hlalosa thepa pele u khetha thepa.

Arolelana tlhaloso ea lisebelisoa tsa moemeli, molumo o fumanehang, boemo ba sebaka le liphetho tse reriloeng. YSHUNXIN e tla sebelisa lintlha tseo ho lokisa moeli oa ts'ebetso le puisano ea tlhophiso.

Qala Tlhahlobo ea Morero
CATALOGUE-ALIGNED ENGINEERING BASIS

Continuous carbonization and energy integration

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

01

Incoming material

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

02

Expected outputs

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

03

Project interfaces

Drying/preparation, phepelo e tiisitsoeng, carbonization, gas treatment/combustion, cooling, storage, fire control and optional heat recovery.

MODEL AND SCOPE REGISTER

Use only the row matching the selected process boundary.

Catalogue referenceCapacityMatlaPhysical envelopeIncluded boundary
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

Configuration rule: catalogue capacity is a planning reference. Stable throughput, installed/operating power, footprint, ho hlaphoheloa, purity, emissions and utility demand require the approved equipment list, representative material and written acceptance conditions.

Information required before configuration and quotation

  1. Representative material photos, specifications and available sample.
  2. Required capacity plus hours per shift, shifts per day and operating days.
  3. Liphetho tse reriloeng, sampling method and downstream receiver requirements.
  4. Site country, available power, fuel, metsi, compressed air and building limits.
  5. Local environmental, fire, storage and occupational-safety requirements.
  6. Requested delivery boundary: thepa, sebopeho, ho kenya, commissioning and training.