rojans
Chemical
- Mar 18, 2008
- 5
I am a bit puzzled. Someone told me that a discharge pipe of relief valve for pure hydrogen should be continiously purged with an inert in order to prevent a flammable mixture during venting. Without sufficient purging, air will be present in the discharge pipe. A flammable mixture could then be formed by leaking of the relief valve or during a discharge at the hydrogen/air interface.
Auto ignition of hydrogen (pressures 10-40 bar) is quite realistic. When ignition occurs the deflagration can transition into a detonation as the discharge lines are quite long. For a deflagration the situation is safe as the relief takes place at a safe location; however a detonation is something to prevent.
I have checked NFPA 68/69 but not clear to me what to do.
A few situations exist: In general the discharge pipe itself is quite long: 10-40 meters. The diameters vary from 15mm to 100mm. In all cases L/d (length / diameter ratio) is > 100 and higher.
Please give any guidance.
Auto ignition of hydrogen (pressures 10-40 bar) is quite realistic. When ignition occurs the deflagration can transition into a detonation as the discharge lines are quite long. For a deflagration the situation is safe as the relief takes place at a safe location; however a detonation is something to prevent.
I have checked NFPA 68/69 but not clear to me what to do.
A few situations exist: In general the discharge pipe itself is quite long: 10-40 meters. The diameters vary from 15mm to 100mm. In all cases L/d (length / diameter ratio) is > 100 and higher.
Please give any guidance.