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Flamable Gas Relief
Started by Guest_mvancleave_*, Mar 19 2005 08:18 PM
9 replies to this topic
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#1
Guest_mvancleave_*
Posted 19 March 2005 - 08:18 PM
I didn't get a response to this in the relief devices forum, so I am trying again here. Hope that doesn't go too much against protocol.
I have a relief valve on the discharge of a compressor in a flammable gas system (60% methane, 40% carbon dioxide). The valves will relieve to atmosphere. Do I need a flame arrestor on the vent line? What document governs?
Thanks,
Mike
I have a relief valve on the discharge of a compressor in a flammable gas system (60% methane, 40% carbon dioxide). The valves will relieve to atmosphere. Do I need a flame arrestor on the vent line? What document governs?
Thanks,
Mike
#2
Posted 23 March 2005 - 06:32 PM
Most companies would only require a flame arrestor on an "open" vent. I believe there is a specific siting in Factroy Mutual literature.
#3
Posted 24 March 2005 - 12:49 AM
QUOTE (mvancleave @ Mar 19 2005, 08:18 PM)
I didn't get a response to this in the relief devices forum, so I am trying again here. Hope that doesn't go too much against protocol.
I have a relief valve on the discharge of a compressor in a flammable gas system (60% methane, 40% carbon dioxide). The valves will relieve to atmosphere. Do I need a flame arrestor on the vent line? What document governs?
Thanks,
Mike
I have a relief valve on the discharge of a compressor in a flammable gas system (60% methane, 40% carbon dioxide). The valves will relieve to atmosphere. Do I need a flame arrestor on the vent line? What document governs?
Thanks,
Mike
#4
Guest_mvancleave_*
Posted 25 March 2005 - 01:39 AM
Thanks Musrey.
I have actually learned a lot from API RP520 and RP521, and I will look for some FM guidance as well (does anyone know off-hand which FM document would govern here).
The vents are to atmosphere, so I will put a flame arrestor on them. However, I will likely manifold them so I only have one vent to deal with.
Mike
I have actually learned a lot from API RP520 and RP521, and I will look for some FM guidance as well (does anyone know off-hand which FM document would govern here).
The vents are to atmosphere, so I will put a flame arrestor on them. However, I will likely manifold them so I only have one vent to deal with.
Mike
#5
Posted 25 March 2005 - 06:27 PM
Unfortunately, I can remenber the exact reference. It was in a section dealing with storage of flammable liquids.
#6
Guest_Guest_*
Posted 21 April 2005 - 03:35 AM
I have never seen a flame arrestor on a relief line for a standard
hydrocarbon mixture such as you describe. Maybe if the chemical
was ethylene oxide (which can burn its way back through a pipe
against flow), you might need a flame arrestor. The relief valve
should close after relieving pressure in the vessel, and the gas
leaving the relief pipe will clear the line of oxygen.
If for some reason you do put a flame arrestor in the relief discharge
line, make sure that the pressure drop of the device is taken into
consideration. You don't want the vessel to overpressure because
you can't get gas through the arrestor fast enough. It may require
going to a larger line size on the discharge pipe.
hydrocarbon mixture such as you describe. Maybe if the chemical
was ethylene oxide (which can burn its way back through a pipe
against flow), you might need a flame arrestor. The relief valve
should close after relieving pressure in the vessel, and the gas
leaving the relief pipe will clear the line of oxygen.
If for some reason you do put a flame arrestor in the relief discharge
line, make sure that the pressure drop of the device is taken into
consideration. You don't want the vessel to overpressure because
you can't get gas through the arrestor fast enough. It may require
going to a larger line size on the discharge pipe.
#7
Posted 21 April 2005 - 07:36 AM
I would not normally put a flame arrestor on a PSV vent line.
If you have any potential for moisture condensing in the line, they are prone to plugging and especially freezing (if you are in a cold climate like I am). The dangers of over-pressuring the vent system seem to be more of a risk than accidental ignition of a PSV vent burning back to the source. Also the high CO2 content of the gas you specified (40%) will lower the heating value of this gas and also lower the likely hood of accidiental ignition.
With a flare system that has a continuous flame, I would normally put a purge gas on the flare system to prevent air ingress into the line, but for a vent system, I believe this is not required.
If you have any potential for moisture condensing in the line, they are prone to plugging and especially freezing (if you are in a cold climate like I am). The dangers of over-pressuring the vent system seem to be more of a risk than accidental ignition of a PSV vent burning back to the source. Also the high CO2 content of the gas you specified (40%) will lower the heating value of this gas and also lower the likely hood of accidiental ignition.
With a flare system that has a continuous flame, I would normally put a purge gas on the flare system to prevent air ingress into the line, but for a vent system, I believe this is not required.
#8
Posted 21 April 2005 - 12:25 PM
I agree with Guest and Shaun in their inclinations to avoid a flame arrestor. In fact, I think it totally wrong to put one on the discharge of a high pressure (setpoint >15 psig) PSV. I'm sure they're not required since you can refer to many regulations and standards dealing with LPG, Ammonia, and, I think, LNG and never see "flame arrested" PSV's. Why would you want to introduce a tortuous path (flame arrestor) in a PSV outlet. Freezing, corrosion, and probably just the random deposition of atmospheric dust could put the entire safety system at risk by restricting the flow from the PSV. What are you protecting against? Flame propagation backwards through a sonic flow nozzle into a tank with a flammable mixture? Think about that and I think you'll agree that the hazards that the flame arrestor might guard against are essentially non-existant. Keep it simple - short discharge pipe direct to atmosphere but away from any ignition sources.
Doug
Doug
#9
Posted 22 April 2005 - 07:05 AM
Please no obstructions on the PSV discharge. The entire purpose of the PSV will be defeated if that flame arrestor clogs up.
For concerns regarding fires at end of vent lines, please consult API 521. If I remember correctly this is not an issue at all. For proper dispersion of flamable vapors there is a reynolds number criteria to be met. I don't have API 521 with me right now, but I think this criteria is in there.
For concerns regarding fires at end of vent lines, please consult API 521. If I remember correctly this is not an issue at all. For proper dispersion of flamable vapors there is a reynolds number criteria to be met. I don't have API 521 with me right now, but I think this criteria is in there.
#10
Guest_Ron_tex_*
Posted 22 April 2005 - 02:07 PM
Why are you even considering relieving a flammable gas to atmosphere? May I suggest you check the company's safety standards or best practices.
Vent it to the flare and you're finished - it'll be worth the cost.
Vent it to the flare and you're finished - it'll be worth the cost.
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