fluxfire71
Chemical
The Vessel at profile is at 500 C and 550 bar containing pressurised argon. I have been tasked me to look at a scenario where the contents of the furnace may become oxidised leading to a rise in temperature.
If you assume a breach in one of the service pipes resulting in pressure loss. How would the air surrounding the furnace enter the furnace? And how exactly can i calculate the mass flow of air into the furnace? Assuming an orifice.
If the furnace has significant thermal energy i can't see air flowing back in due to the temperature gradient despite the concentration.
Much appreciated
If you assume a breach in one of the service pipes resulting in pressure loss. How would the air surrounding the furnace enter the furnace? And how exactly can i calculate the mass flow of air into the furnace? Assuming an orifice.
If the furnace has significant thermal energy i can't see air flowing back in due to the temperature gradient despite the concentration.
Much appreciated