I-configure ang paggawa ng carbon, proseso-gas na paggamot, tungkulin ng boiler at ang steam load ng customer bilang konektadong sistema.
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
- 02Patuloy na 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, pagpapanatili, 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 | Alikabok, 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.
OutputMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
OutputVerified preliminary heat balanceUtility design
Define boiler, tubig, condensate, header and emissions interfaces.
OutputConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
OutputMeasurable 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, pagkasunog, boiler, paggamot ng tubig, 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.
Carbonization na may waste-heat steam supply
I-configure ang linya ng carbonization at pagtanggap ng steam load mula sa isang sinusukat na balanse ng init at masa.
Papasok na materyal
Inihanda ang biomass kasama ang oras-oras/araw-araw na profile ng feed at target na detalye ng carbon.
Mga inaasahang output
Biochar at isang kwalipikadong waste-heat stream para sa isang napagkasunduang steam duty.
Mga interface ng proyekto
Pagpatuyo ng feed, carbonization gas, pagkasunog, waste-heat boiler, paggamot ng tubig, steam pressure/load at operating control.
Gamitin lamang ang row na tumutugma sa napiling hangganan ng proseso.
| Sanggunian ng katalogo | Kapasidad | kapangyarihan | Pisikal na sobre | Kasamang hangganan |
|---|---|---|---|---|
| SXTD820Patuloy na carbonization | 1–2 m³/h | 95 kW | 600 m² catalog land reference | Inihanda ang tuloy-tuloy na linya ng carbonization ng biomass |
| SXTD1200Patuloy na carbonization | 3–5 m³/h | 110 kW | 650 m² catalog land reference | Inihanda ang tuloy-tuloy na linya ng carbonization ng biomass |
| SXTD1500Patuloy na carbonization | 5–8 m³/h | 153 kW | 800 m² catalog land reference | Inihanda ang tuloy-tuloy na linya ng carbonization ng biomass |
| SXTD1800Patuloy na carbonization | 8–10 m³/h | 178 kW | 800 m² catalog land reference | Inihanda ang tuloy-tuloy na linya ng carbonization ng biomass |
| SXTD2000 - 10-14 na klasePatuloy na carbonization | 10–14 m³/h | 190 kW | 850 m² catalog land reference | Catalog prints SXTD2000 para sa klase na ito |
| SXTD2000 - 14–17 klasePatuloy na carbonization | 14–17 m³/h | 220 kW | 850 m² catalog land reference | Inuulit ng Catalog ang SXTD2000; Ang panghuling code ng modelo ay nangangailangan ng nakasulat na kumpirmasyon |
Panuntunan sa pagsasaayos: Ang kapasidad ng katalogo ay isang sanggunian sa pagpaplano. Matatag na throughput, naka-install/operating power, bakas ng paa, pagbawi, kadalisayan, ang mga emisyon at pangangailangan ng utility ay nangangailangan ng inaprubahang listahan ng kagamitan, kinatawan ng materyal at nakasulat na mga kondisyon sa pagtanggap.
Kinakailangan ang impormasyon bago ang pagsasaayos at pagsipi
- Mga larawan ng kinatawan ng materyal, mga pagtutukoy at magagamit na sample.
- Kinakailangang kapasidad at oras sa bawat shift, mga shift bawat araw at araw ng pagpapatakbo.
- Mga target na output, paraan ng sampling at mga kinakailangan sa downstream na receiver.
- Bansa ng site, magagamit na kapangyarihan, panggatong, tubig, compressed air at mga limitasyon ng gusali.
- Lokal na kapaligiran, apoy, imbakan at mga kinakailangan sa kaligtasan sa trabaho.
- Hiniling na hangganan ng paghahatid: kagamitan, layout, pag-install, komisyon at pagsasanay.
