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, driftstimer, pressure, temperature and seasonal production schedule.
Water system
Define raw-water quality, behandling, 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, opretholdelse, low-gas operation and backup-steam behavior for the receiving plant.
Se grænsen for det tilsluttede udstyr.
Visuelle referencer understøtter diskussion af tidlig layout. Slutudstyr, arrangement og grænseflader bekræftes fra projektmaterialet og sitet.
Oversæt projektfakta til en udstyrsliste.
Denne referencematrix viser beslutningslogikken. Endelige mængder, modeller og grænseflader hører hjemme i det godkendte projektforslag.
| System blok | Typisk omfang | Konfigurationsgrundlag |
|---|---|---|
| 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 |
Fremfør kun projektet, når den nødvendige dokumentation er tilgængelig.
Hver gate forvandler kundeinformation til et defineret teknisk eller kommercielt output til den næste beslutning.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
ProduktionMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
ProduktionVerified preliminary heat balanceUtility design
Define boiler, vand, condensate, header and emissions interfaces.
ProduktionConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
ProduktionMeasurable project acceptance sheetSpørgsmål, der skal løses før konfiguration.
Svar definerer den tekniske grænse; de erstatter ikke repræsentativ materialetestning eller lokal overensstemmelsesgennemgang.
What information is needed from the steam user?
Provide minimum, normal and peak steam demand, pressure, temperature, operating schedule, 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 vælger udstyret.
Del en repræsentativ materialebeskrivelse, tilgængelig volumen, webstedsstatus og måloutput. YUSHUNXIN vil bruge disse fakta til at forberede den relevante procesgrænse og konfigurationsdiskussion.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
Indgående materiale
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Forventede output
Biochar and a qualified waste-heat stream for an agreed steam duty.
Projektgrænseflader
Feed drying, carbonization gas, combustion, waste-heat boiler, water treatment, steam pressure/load and operating control.
Brug kun den række, der matcher den valgte procesgrænse.
| Katalog reference | Kapacitet | Magt | Fysisk konvolut | Inkluderet grænse |
|---|---|---|---|---|
| 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 |
Konfigurationsregel: Katalogkapacitet er en planlægningsreference. Stabil gennemstrømning, installeret/driftseffekt, fodspor, bedring, renhed, emissioner og forsyningsbehov kræver den godkendte udstyrsliste, repræsentativt materiale og skriftlige acceptbetingelser.
Oplysninger påkrævet før konfiguration og tilbud
- Repræsentative materialebilleder, specifikationer og tilgængelig prøve.
- Påkrævet kapacitet plus timer pr, vagter pr dag og arbejdsdage.
- Mål output, prøveudtagningsmetode og krav til downstream-modtagere.
- Site land, tilgængelig strøm, brændstof, vand, trykluft og bygningsgrænser.
- Lokalt miljø, brand, krav til opbevaring og arbejdssikkerhed.
- Anmodet leveringsgrænse: udstyr, layout, installation, idriftsættelse og træning.
