Configure carbon production, process-gas treatment, boiler duty and the customer steam load as a connected system.
Turn stable carbonization heat into useful industrial steam.
A steam project should be designed around the receiving process load. Carbonization gas, supplementary fuel, boiler duty, water treatment and backup capacity must work as one operating system.
Keep carbon quality and steam reliability under separate control
The carbonizer creates the primary product; the energy train converts suitable process gas and heat into a controlled utility.
- 01Biomass drying and feeding
- 02Continuous carbonization
- 03Dust and condensable separation
- 04Gas cleaning and controlled combustion
- 05Steam generation and water treatment
- 06Distribution, metering and backup supply
Define the user before defining the boiler
Food and chemical plants require a clear hourly steam profile, pressure, quality and continuity basis.
Steam demand
Provide minimum, normal and peak demand, operating hours, pressure, temperature and seasonal production schedule.
Water system
Define raw-water quality, treatment, deaeration, blowdown, condensate return and make-up-water capacity.
Fuel stability
Gas cleaning, buffer volume, burner turndown and supplementary fuel determine pressure stability during feed or quality changes.
Interface boundary
Agree the battery limit for boiler house, steam header, metering, condensate return, civil works and operating responsibility.
Verify both carbon output and usable steam
Acceptance should be based on documented feedstock, operating conditions and measurement methods.
Carbon product
Record yield and product properties only against the tested biomass and agreed thermal program.
Steam output
Meter flow, pressure and temperature during a defined stable operating window instead of using theoretical heat alone.
Emissions boundary
Identify combustion, particulate and condensable controls and the local monitoring or permit requirements.
Continuity plan
Define startup, shutdown, maintenance, low-gas operation and backup-steam behavior for the receiving plant.
Se grensen for tilkoblet utstyr.
Visuelle referanser støtter tidlig layoutdiskusjon. Endelig utstyr, arrangement og grensesnitt bekreftes fra prosjektmaterialet og nettstedet.
Oversett prosjektfakta til en utstyrsliste.
Denne referansematrisen viser beslutningslogikken. Endelige mengder, modeller og grensesnitt hører hjemme i det godkjente prosjektforslaget.
| Systemblokk | Typisk omfang | Konfigurasjonsgrunnlag |
|---|---|---|
| Gas preparation | Støv, condensable and moisture control with safe buffering | Carbonization-gas variability and burner limits |
| Combustion system | Controlled burner, combustion chamber and safety interlocks | Steam duty, turndown and supplementary-fuel plan |
| Boiler island | Boiler, economizer, blowdown, instruments and protection | Pressure, temperature and operating code basis |
| Water and condensate | Treatment, deaeration, make-up water and condensate return | Source-water quality and user return conditions |
| Steam delivery | Header, metering, pressure control and backup interface | Minimum, normal and peak customer demand |
Fremme prosjektet bare når nødvendig bevis er tilgjengelig.
Hver gate gjør kundeinformasjon til en definert teknisk eller kommersiell produksjon for neste beslutning.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
ProduksjonMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
ProduksjonVerified preliminary heat balanceUtility design
Define boiler, vann, condensate, header and emissions interfaces.
ProduksjonConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
ProduksjonMeasurable project acceptance sheetSpørsmål å løse før konfigurasjon.
Svar definerer den tekniske grensen; de erstatter ikke representativ materialtesting eller lokal samsvarsgjennomgang.
What information is needed from the steam user?
Provide minimum, normal and peak steam demand, pressure, temperature, driftsplan, condensate return, water quality and continuity requirement.
Can process gas alone guarantee continuous steam supply?
Not without verification. Buffering, burner turndown, supplementary fuel and backup capacity may be needed when feedstock or gas production varies.
What belongs in the steam-system boundary?
The scope may include gas treatment, combustion, boiler, water treatment, deaeration, blowdown, steam header, metering, condensate return and backup interfaces.
How should steam acceptance be measured?
Use metered flow, pressure and temperature during a defined stable operating window with the agreed biomass, carbonization conditions and auxiliary loads.
Definer materialet før du velger utstyr.
Del en representativ materialbeskrivelse, tilgjengelig volum, nettstedstatus og målutganger. YUSHUNXIN vil bruke disse faktaene til å forberede den relevante prosessgrensen og konfigurasjonsdiskusjonen.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
Innkommende materiale
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Forventede utganger
Biochar and a qualified waste-heat stream for an agreed steam duty.
Prosjektgrensesnitt
Feed drying, carbonization gas, combustion, waste-heat boiler, water treatment, steam pressure/load and operating control.
Bruk kun raden som samsvarer med den valgte prosessgrensen.
| Katalogreferanse | Kapasitet | Makt | Fysisk konvolutt | Inkludert grense |
|---|---|---|---|---|
| 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 |
Konfigurasjonsregel: katalogkapasitet er en planleggingsreferanse. Stabil gjennomstrømning, installert/driftskraft, fotspor, bedring, renhet, utslipp og bruksbehov krever godkjent utstyrsliste, representativt materiale og skriftlige akseptbetingelser.
Informasjon nødvendig før konfigurasjon og tilbud
- Representative materialbilder, spesifikasjoner og tilgjengelig prøve.
- Nødvendig kapasitet pluss timer per skift, skift per dag og driftsdager.
- Mål utganger, prøvetakingsmetode og nedstrøms mottakerkrav.
- Nettstedets land, tilgjengelig kraft, brensel, vann, trykkluft og bygningsgrenser.
- Lokalt miljø, ild, krav til oppbevaring og yrkessikkerhet.
- Forespurt leveringsgrense: utstyr, layout, installasjon, igangkjøring og opplæring.
