Las soluciones de Armstrong International están diseñadas a la medida para facilitar el mantenimiento, mejorar la fiabilidad y el desempeño, y lograr actualizaciones y cambios más rápidos.
Contacte a Armstrong para beneficiarse de las mejores prácticas en instalación de tuberías por parte de expertos y diseñadas para satisfacer los requisitos específicos de cada unidad, refinería o de toda su empresa, en ubicaciones de todo el mundo. Como líderes mundiales en la optimización de sistemas de vapor y condensado, nuestros especialistas están preparados para ayudarle a resolver los problemas a los que se enfrenta su planta de refinación de hidrocarburos o de procesamiento de sustancias químicas.
Puntos de drenaje
Steam Trap Location Points - Steam Main Header
Instalar puntos de drenaje de condensado con trampas de vapor. Vapor saturado: cada 150 a 300 pies (25 a 50 m). Vapor sobrecalentado: cada 300 a 500 pies (50 a 75 m)
Steam Valve Station Drainage
Instalar trampas de vapor antes de las válvulas manuales que normalmente se encuentran cerradas, y antes de las válvulas reductoras de presión y válvulas de control.
Steam Trap Location Points - Steam Main Header
Instalar puntos de drenaje de condensado con trampas de vapor en la parte inferior de cualquier elevación vertical, independientemente de la dirección del flujo de vapor.
Steam Trap Location Points – End of Steam Main / Header / Line
La instalación de eliminadores de aire al final de la ubicación principal evitará que el aire quede atrapado en el cabezal de vapor, especialmente durante los períodos de puesta en marcha.
Depósitos colectores de goteo
Steam Main Header Drip Trap – Saturated (≤ 650 psig /45 barg)
Steam Main Header Drip Trap – Saturated (≤ 650 psig /45 barg)
Steam Main Header Drip Trap – Saturated (≤ 650 psig /45 barg)
Steam Main Header Drip Trap – Superheated (≤ 650 psig & 600°F / 45 barg & 315°C)
Steam Main Header Drip Trap – Superheated (≤ 650 psig & 600°F / 45 barg & 315°C)
Steam Main Header Drip Trap – Superheated (≤ 650 psig & 600°F / 45 barg & 315°C)
Steam Main Header Drip Trap – Saturated (650 ≤ 1,800 psig / 45 ≤ 124 barg )
Steam Main Header Drip Trap - Superheated Single Block and Bleed (650 ≤ 1,245 psig @ 900°F / 45 ≤ 86 barg @ 482°C)
Steam Main Header Drip Trap – Double Block and Bleed (650 ≤ 1,245 psig @ 900 °F / 45 ≤ 86 barg @ 482°C)
Steam Main Header Drip Trap – Superheated, Double Block and Bleed (650 ≤ 1,245 psig @ 900 °F/45 ≤ 86 barg @ 482°C)
Steam Main Header Drip Trap – Superheated, Double Block and Bleed (650 ≤ 1,245 psig @ 900 °F / 45 ≤ 86 barg @ 482°C)
Calentadores de proceso
Shell & Tube Heat Exchanger – Horizontal – Saturated Steam on Shell Side (≤ 650 psig /45 barg) Constant Positive Differential Pressure (Non-Stall)
Shell & Tube Heat Exchanger – Horizontal – Saturated Steam on Shell Side (≤ 200 psig /14 barg) Modulating Differential Pressure (Stall) – Closed System
Shell & Tube Heat Exchanger – Horizontal – Saturated Steam on Tube Side (≤ 650 psig /45 barg) Constant Positive Differential Pressure (Non-Stall)
Shell & Tube Heat Exchanger – Horizontal – Saturated Steam on Tube Side (≤ 200 psig / 14 barg) Modulating Differential Pressure (Stall) – Closed System
Shell & Tube Heat Exchanger – Vertical – Saturated Steam on Tube Side (≤ 650 psig / 45 barg) Constant Positive Differential Pressure (Non-Stall)
Shell & Tube Heat Exchanger – Vertical – Saturated Steam on Shell Side (≤ 200 psig /14 barg) Modulating Differential Pressure (Stall) – Closed System
Shell & Tube Heat Exchanger – Vertical – Saturated Steam on Tube Side (≤ 650 psig / 45 barg) Constant Positive Differential Pressure (Non-Stall)
Shell & Tube Heat Exchanger – Vertical – Saturated Steam on Tube Side (≤ 200 psig / 14 barg) Modulating Differential Pressure (Stall) – Closed System
Sistemas abiertos
Condensate from Multiple Sources – Saturated (≤ 150 psig / 10 barg) Negative Differential Pressure – Open System
Condensing Steam Turbine – Saturated (≤ 150 psig / 10 barg) Negative Differential Pressure – Closed System
Turbinas
Steam Turbine Saturated – Single Stage Positive Differential Pressure (≤ 650 Psig/ 45 Bar Saturated)
Steam Turbine Saturated – Multiple Stages Positive Differential Pressure (≤ 650 Psig/ 45 Bar Saturated)
Steam Turbine – Single Stage Positive Differential Pressure Low Pressure (≤ 450 Psig/ 31 Bar Superheated)
Steam Turbine – Single Stage Positive Differential Pressure High Pressure (≤ 1245 Psig/ 86 Bar Superheated)
Steam Turbine Superheated – Multiple Stages Positive Differential Pressure Low Pressure (≤ 450 Psig/ 31 Bar Superheated)
Steam Turbine – Multiple Stages Positive High Pressure (450 Psig ≤ 1245 Psig/ 31 Bar ≤ 86 Bar Superheated)
Combustiones
Flare Systems – Single Steam Supply (≤ 200 psig / 14 barg) Closed System
Flare Systems – Multiple Steam Supplies (≤ 150 psig / 10 barg) Open System
Tanques de almacenamiento
Storage Tank Coil Types
Storage Tank – Saturated – Single Steam Supply Constant Pressure (Non-Stall) (0 ≤ 650 psig / 0 ≤ 45 barg)
Storage Tank – Saturated – Single Steam Supply Modulating Pressure (Stall) (0 ≤ 200 psig / 0 ≤ 14 barg)
Multiple Storage Tanks – Saturated – Single Steam Supply Constant Pressure (≤ 150 psig /10 barg)
Rastreo
Steam Tracing Systems