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Las bobinas de los supercalentadores de la caldera
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Pared de membrana de la caldera
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Ahorrador de la caldera
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Tubo de aleta de la caldera
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tambor de vapor de la caldera
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El panel de pared del agua de la caldera
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Cañones de cañones
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Sobrecalentador y recalentador
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Calentador Precalentador de aire
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Sobrecalentador de la caldera
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AlexanderProveedores confiables -
LouisHa sido un placer trabajar contigo.
Wood Fired Portable Steam Boiler Economizer with 1 Year Warranty for Industrial Use
Póngase en contacto conmigo para muestras y cupones gratis.
WhatsApp:0086 18588475571
En WeChat: 0086 18588475571
¿ Qué pasa?: sales10@aixton.com
Si tiene alguna preocupación, ofrecemos ayuda en línea las 24 horas.
x| Tipo | Circulación natural | Estructura | Tubos de fuego y de agua |
|---|---|---|---|
| Presión | Bajo/de alta presión | Estilo | Vertical |
| Combustible | Fuentes de energía | Producción | Agua caliente/vapor |
| Tratamiento superficial | Pintado | Tubería desnuda OD | 25-1650 mm |
| Espesor de la tubería desnuda | 2-40 mm | Grosor de la aleta | 0.6-3.0 mm |
| Altura de la aleta | 5-30 mm | Tono de tubo de aleta | 5-30 mm |
| Longitud del tubo de aleta | ≤12000 mm | Material | Acero al carbono, aleación, acero austenítico |
| Velocidad de gases de combustión | Máximo permitido | ||
| Resaltar | Wood Fired Economizer,Portable Steam Boiler Economizer,1 Year Warranty Economizer |
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The economizer plays a crucial role in enhancing overall boiler thermal efficiency by recovering low-level energy from flue gas before it's exhausted to the atmosphere. This energy recovery occurs through heating the boiler feedwater. Economizers are tubular heat transfer surfaces that preheat boiler feed water before it enters the steam drum or furnace surfaces, significantly reducing operating costs by recovering extra energy from flue gas.
Economizers minimize thermal shock risks and water temperature fluctuations as feed water enters the drum or waterwalls. They also accommodate increasingly stringent environmental regulations limiting nitrogen oxides and sulfur dioxide emissions. The design compensates for the lower gas-side heat transfer coefficient compared to water-side through finned outer tube surfaces that increase heat transfer area. The primary design objective is achieving necessary heat transfer at minimal cost, with flue gas velocity being a key criterion - higher velocities improve heat transfer and reduce capital costs.
| Name (unit) | Specification (mm) |
|---|---|
| Bare pipe (OD) | 25-1650 |
| Bare pipe (Thickness) | 2-40 |
| Fin (Thickness) | 0.6-3.0 |
| Fin (Height) | 5-30 |
| Fin tube thread pitch | 5-30 |
| Fin tube length | ≤12000 |
Material: Carbon Steel, Alloy, Austenitic Steel (Nickel and Chromium or Manganese)
- Impact test and Strength calculation report with applied materials information
- 100% NDT (non-destructive inspection) report of steel plate, tube and electrode
- X-ray, γ-ray and liquid penetrant test inspection report (welding seam) to ensure complete boiler quality
- Hydraulic test report to verify standard working pressure and safety

