cempass
Petroleum
- May 12, 2006
- 2
Dear Sirs,
I am working in the design of a cold vent system. We have estimated just two CO2 bottles (100# each) for the flame snuff at the end of the plant blow down event. The operation procedure is like this: Case Plant in the blow down scenario. 2.- Probable ignition of the flame of the stack. 3.- Leave the flame in the tip and Wait until the pressure of the plant reaches half of the initial pressure. 4.- Open the CO2 valves to snuff the flame. 5.- let relieve the reaimaining gas of the plant trough the stack just to avoid any flash get back into the stack.
My concern is about re ignition of the gas due to the high temperature of the tip. I know the ignition gas temperature is arround 1000 F.
I have never seen a cold vent re ignition of the flame since I ussually do not let the flame last more than 15 - 30 minutes. But in this event the flame can last up to two hours before I can open the CO2 snuff valves letting the tip reaches high temperature. It is quite dificult to estimate the TIP temperature when the remaining " purging " gas reaches the TIP. Is my concern correct?
I appreciate your help in this regard,
Sincerely,
CEMP
I am working in the design of a cold vent system. We have estimated just two CO2 bottles (100# each) for the flame snuff at the end of the plant blow down event. The operation procedure is like this: Case Plant in the blow down scenario. 2.- Probable ignition of the flame of the stack. 3.- Leave the flame in the tip and Wait until the pressure of the plant reaches half of the initial pressure. 4.- Open the CO2 valves to snuff the flame. 5.- let relieve the reaimaining gas of the plant trough the stack just to avoid any flash get back into the stack.
My concern is about re ignition of the gas due to the high temperature of the tip. I know the ignition gas temperature is arround 1000 F.
I have never seen a cold vent re ignition of the flame since I ussually do not let the flame last more than 15 - 30 minutes. But in this event the flame can last up to two hours before I can open the CO2 snuff valves letting the tip reaches high temperature. It is quite dificult to estimate the TIP temperature when the remaining " purging " gas reaches the TIP. Is my concern correct?
I appreciate your help in this regard,
Sincerely,
CEMP