Konfigirasyon pwodiksyon kabòn, pwosesis-tretman gaz, devwa chofaj ak chaj la vapè kliyan kòm yon sistèm konekte.
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
- 02Karbonizasyon kontinyèl
- 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 | Pousyè, 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, dlo, 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, combustion, boiler, tretman dlo, 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.
Karbonizasyon ak rezèv vapè fatra-chalè
Konfigure liy karbonizasyon an ak resevwa chaj vapè nan yon sèl mezire chalè ak balans mas.
Materyèl k ap rantre
Byomass prepare plis pwofil manje èdtan / chak jou ak spesifikasyon kabòn sib.
Pwodiksyon espere
Biochar ak yon kouran dechè-chalè kalifye pou yon devwa vapè dakò.
Entèfas pwojè
Manje siye, gaz karbonizasyon, combustion, chodyè fatra-chalè, tretman dlo, presyon vapè / chaj ak kontwòl opere.
Sèvi ak sèlman ranje ki matche ak fwontyè pwosesis chwazi a.
| Referans katalòg | Kapasite | Pouvwa | Anvlòp fizik | Enkli fwontyè |
|---|---|---|---|---|
| SXTD820Karbonizasyon kontinyèl | 1-2 m³/h | 95 kW | 600 m² katalòg tè referans | Prepare byomass liy karbonizasyon kontinyèl |
| SXTD1200Karbonizasyon kontinyèl | 3-5 m³/h | 110 kW | 650 m² katalòg tè referans | Prepare byomass liy karbonizasyon kontinyèl |
| SXTD1500Karbonizasyon kontinyèl | 5-8 m³/h | 153 kW | 800 m² katalòg tè referans | Prepare byomass liy karbonizasyon kontinyèl |
| SXTD1800Karbonizasyon kontinyèl | 8-10 m³/h | 178 kW | 800 m² katalòg tè referans | Prepare byomass liy karbonizasyon kontinyèl |
| SXTD2000 - 10–14 klasKarbonizasyon kontinyèl | 10-14 m³/h | 190 kW | 850 m² katalòg tè referans | Katalòg enprime SXTD2000 pou klas sa a |
| SXTD2000 - 14–17 klasKarbonizasyon kontinyèl | 14-17 m³/h | 220 kW | 850 m² katalòg tè referans | Katalòg repete SXTD2000; kòd modèl final la mande pou yon konfimasyon alekri |
Règ konfigirasyon: kapasite katalòg se yon referans planifikasyon. Debi ki estab, pouvwa enstale / opere, anprint, rekiperasyon, pite, emisyon ak demann sèvis piblik mande pou lis ekipman apwouve a, materyèl reprezantan ak kondisyon akseptasyon ekri.
Enfòmasyon ki nesesè anvan konfigirasyon ak sitasyon
- Foto materyèl reprezantan, espesifikasyon ak echantiyon ki disponib.
- Kapasite obligatwa plis èdtan pou chak chanjman, orè pou chak jou ak jou fonksyònman.
- Sib rezilta yo, metòd echantiyon ak kondisyon reseptè en.
- Peyi sit la, pouvwa ki disponib, gaz, dlo, lè konprese ak limit bilding yo.
- Anviwònman lokal yo, dife, depo ak kondisyon sekirite nan travay.
- Limit livrezon yo mande: ekipman, layout, enstalasyon, komisyonin ak fòmasyon.
