Konfigurēt oglekļa ražošanu, process-gāzes apstrāde, katla pienākums un klienta tvaika slodze kā savienota sistēma.
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
- 02Nepārtraukta karbonizācija
- 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.
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 | Putekļi, 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 |
Advance the project only when the required evidence is available.
Each gate turns customer information into a defined technical or commercial output for the next decision.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
IzvadeMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
IzvadeVerified preliminary heat balanceUtility design
Define boiler, ūdens, condensate, header and emissions interfaces.
IzvadeConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
IzvadeMeasurable project acceptance sheetQuestions to resolve before configuration.
Answers define the engineering boundary; they do not replace representative material testing or local compliance review.
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, degšana, boiler, ūdens apstrāde, 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.
Define the material before selecting the equipment.
Share a representative material description, available volume, site status and target outputs. YUSHUNXIN will use those facts to prepare the relevant process boundary and configuration discussion.
Karbonizācija ar siltuma tvaika padevi
Konfigurējiet karbonizācijas līniju un tvaika slodzes saņemšanu no viena izmērītā siltuma un masas bilances.
Ienākošais materiāls
Sagatavots biomasas plus stundas/dienas barības profils un mērķa oglekļa specifikācija.
Paredzamie rezultāti
Bioogle un kvalificēta atkrituma siltuma plūsma par saskaņotu tvaika nodevu.
Projektu saskarnes
Barības žāvēšana, karbonizācijas gāze, degšana, siltuma katls, ūdens apstrāde, tvaika spiediens/slodze un darbības kontrole.
Izmantojiet tikai rindu, kas atbilst atlasītajai procesa robežai.
| Kataloga atsauce | Jauda | Jauda | Fiziskā aploksne | Iekļautā robeža |
|---|---|---|---|---|
| SXTD820Nepārtraukta karbonizācija | 1-2 m³/h | 95 kW | 600 m² kataloga zemes atsauce | Sagatavota biomasas nepārtrauktās karbonizācijas līnija |
| SXTD1200Nepārtraukta karbonizācija | 3-5 m³/h | 110 kW | 650 m² kataloga zemes atsauce | Sagatavota biomasas nepārtrauktās karbonizācijas līnija |
| SXTD1500Nepārtraukta karbonizācija | 5-8 m³/h | 153 kW | 800 m² kataloga zemes atsauce | Sagatavota biomasas nepārtrauktās karbonizācijas līnija |
| SXTD1800Nepārtraukta karbonizācija | 8-10 m³/h | 178 kW | 800 m² kataloga zemes atsauce | Sagatavota biomasas nepārtrauktās karbonizācijas līnija |
| SXTD2000 - 10-14 klaseNepārtraukta karbonizācija | 10-14 m³/h | 190 kW | 850 m² kataloga zemes atsauce | Katalogs izdrukā SXTD2000 šai klasei |
| SXTD2000 - 14-17 klaseNepārtraukta karbonizācija | 14-17 m³/h | 220 kW | 850 m² kataloga zemes atsauce | Katalogs atkārto SXTD2000; gala modeļa kodam nepieciešams rakstisks apstiprinājums |
Konfigurācijas noteikums: kataloga ietilpība ir plānošanas atsauce. Stabila caurlaidspēja, uzstādītā/darba jauda, pēdas nospiedums, atveseļošanās, tīrība, emisijām un komunālo pakalpojumu pieprasījumam ir nepieciešams apstiprināto iekārtu saraksts, reprezentatīvie materiālie un rakstiskie pieņemšanas nosacījumi.
Nepieciešamā informācija pirms konfigurēšanas un piedāvājuma
- Reprezentatīvās materiālu fotogrāfijas, specifikācijas un pieejamais paraugs.
- Nepieciešamā kapacitāte plus stundas maiņā, maiņas dienā un darba dienās.
- Mērķa izvadi, paraugu ņemšanas metode un pakārtotā uztvērēja prasības.
- Vietnes valsts, pieejamā jauda, degviela, ūdens, saspiestais gaiss un ēkas ierobežojumi.
- Vietējā vide, uguns, uzglabāšanas un darba drošības prasības.
- Pieprasītā piegādes robeža: iekārtas, izkārtojumu, uzstādīšana, nodošana ekspluatācijā un apmācība.
