Konfigurearje koalstofproduksje, proses-gas behanneling, boiler plicht en de klant stoom load as in ferbûn systeem.
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
- 02Trochrinnende karbonisaasje
- 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, druk, quality and continuity basis.
Steam demand
Provide minimum, normal and peak demand, operating hours, druk, 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.
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 |
|---|---|---|
| Gas preparation | Stof, 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 |
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.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
UtfierMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
UtfierVerified preliminary heat balanceUtility design
Define boiler, wetter, condensate, header and emissions interfaces.
UtfierConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
UtfierMeasurable project acceptance sheetFragen om op te lossen foar konfiguraasje.
Antwurden definiearje de engineering grins; se net ferfange represintative materiaal testen of lokale neilibjen review.
What information is needed from the steam user?
Provide minimum, normal and peak steam demand, druk, 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, ferbaarning, boiler, wetter behanneling, 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.
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.
Carbonization mei ôffal-waarmte stoom oanbod
Konfigurearje de carbonization line en ûntfange stoom load út ien mjitten waarmte en massa lykwicht.
Ynkommende materiaal
Tariede biomassa plus oere / deistich feed profyl en doel carbon spesifikaasje.
Ferwachte útgongen
Biochar en in kwalifisearre ôffalwaarmtestream foar in ôfpraat stoomplicht.
Projekt ynterfaces
Feed droech, carbonization gas, ferbaarning, ôffal-waarmte boiler, wetter behanneling, steam druk / lading en bestjoeringssysteem kontrôle.
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.
