Configurar u producción carbono, Ts'a'akal u gas tuukula', meyaj ti' le caldera yéetel le kuuch vapor ti' le cliente bey juntúul t.u.m conectado.
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
- 02Carbonización continua
- 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, horas meyaj, pressure, temperature and seasonal production schedule.
Water system
Define raw-water quality, tráatamiento, 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 | Polbóo, 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 |
Avanzar le proyecto chéen ken yaan le pruebas k'a'abeto'ob.
Amal joolnajo' ku sutk'esik a'almaj t'aan ti' le cliente ti' jump'éel salida técnica wa comercial definida uti'al u láak' k'alt'aan.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
SalidaMetered or documented steam-demand basisEnergy balance
Match process-gas availability, internal heat demand and backup fuel.
SalidaVerified preliminary heat balanceUtility design
Define boiler, ja', condensate, header and emissions interfaces.
SalidaConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
SalidaMeasurable project acceptance sheetK'áat chi'oba' uti'al u yutskíinta'al táanil ti' u configuración.
Le núukik ku jets'ik u xuul le ingenieríao'; ma' tu k'exik le prueba material representativo wa le revisión local ti' le cumplimiento.
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, tóoka'al, boiler, ts'aak ja', 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.
Definir le xooko'obo' bey ma' seleccionar le nu'ukulil.
Ts'aiko'on jump'éel tsoolil le xooko'obo' representativo, volumen yaan, noj le ts'ono'oto' yéetel salidas destino. YUSHUNXIN yaan u utilizar le hechos utia'al u preparar le límite tuukula' pertinente yéetel discusión configuración.
Carbonización yéetel suministro vapor u ooxoj residual
Configurar le internet ichil carbonización yéetel k'amik kuuch vapor ti' jump'éel equilibrio ooxoj yéetel juuch' medido.
Xooko'ob ku yokol
Biomasa preparada asab perfil alimentación horaria leti' diaria yéetel especificación carbono objetivo.
Ba'ax ku páa'ta'al
Biochar yéetel jump'éel flujo u ooxoj residual calificado uti'al jump'éel deber vapor acordado.
Interfaces ti' le proyecto
U tikintal le janalo', gas u carbonización, tóoka'al, caldera u ooxoj residual, ts'aak ja', presión leti' kuuch vapor yéetel kaambalil yo'osal funcionamiento.
Meyaj chéen le fila ku nupikubáa yéetel u xuul le tuukula' yéeya'ano'.
| Referencia ti' le catálogo | Páajtalil | Muuk | Sobre físico | Límite incluido |
|---|---|---|---|---|
| SXTD820Carbonización continua | 1–2 m3/h | 95 kW | 600 m2 u k'a'ana'anil u lu'umil catálogo | Internet ichil carbonización continua ti' biomasa preparada |
| SXTD1200Carbonización continua | 3–5 m3/h | 110 kW | 650 m2 u k'a'ana'anil u lu'umil catálogo | Internet ichil carbonización continua ti' biomasa preparada |
| SXTD1500Carbonización continua | 5–8 m3/h | 153 kW | 800 m2 u k'a'ana'anil u lu'umil catálogo | Internet ichil carbonización continua ti' biomasa preparada |
| SXTD1800Carbonización continua | 8–10 m3/h | 178 kW | 800 m2 u k'a'ana'anil u lu'umil catálogo | Internet ichil carbonización continua ti' biomasa preparada |
| SXTD2000 - 10–14 xookCarbonización continua | 10–14 m3/h | 190 kW | 850 m2 u k'a'ana'anil u lu'umil catálogo | Le catálogo ku imprimir SXTD2000 uti'al le xooka' |
| SXTD2000 - 14–17 xookCarbonización continua | 14–17 m3/h | 220 kW | 850 m2 u k'a'ana'anil u lu'umil catálogo | Le catálogo ku ka'a beetik SXTD2000; u ts'ook código modelo k'a'abet u ts'íibta'al confirmación |
Regla u configuración: le Buka'aj u ba'al u catálogo jach jump'éel k'a'ana'an u planificación. Rendimiento estable, instalado/funcionamiento u páajtalil, u yooko'ob, ch'a' óol, pureza, emisiones yéetel demanda utilidad k'a'abet le tsoolol nu'ukulil aprobado, xooko'ob representativos yéetel condiciones u k'a'amal ts'íib.
A'almaj t'aan k'a'abéet bey ma' u configuración yéetel cita
- Fotos u material representativo, especificaciones yéetel muestra disponible.
- Buka'aj u ba'al k'a'abéet asab horas tumen turno, k'eexpajal tumen k'iin yéetel k'iino'ob meyaj.
- Salidas objetivo, método u muestreo yéetel requisitos receptor abajo de le corriente.
- Lu'umil le ts'ono'oto', páajtalil yaan, kóombustible, ja', iik' comprimido yéetel límites edificio.
- Ka'a jeets'el tu'ux, k'áak', almacenamiento yéetel requisitos ti' seguridad ocupacional.
- Límite u k'u'ubul k'áata'an: nu'ukulil, díisposision, instalación, puesta tu marcha yéetel formación.
