My company is buying a 250 ton refrigeration machine. Our engineer is in an argument with the supplier's engineer. Our guy says the specs said that the machine was to be located in a class 1 div 2 group C&D area, meaning flammable vapors are present, and therefore the relief valves are to be designed for the fire case. The engineer for the refrigeration company says no, that's an electrical classification, their practice is not to design for the fire case, and if we want them the whole project has to be put on hold and re-estimated. Who is more correct?
Thanks,
John Moore
Noltex L.L.C.
|

Fire Case For Refrigeration Machine?
Started by Guest_John Moore_*, Dec 11 2003 04:47 PM
4 replies to this topic
Share this topic:
#1
Guest_John Moore_*
Posted 11 December 2003 - 04:47 PM
#2
Posted 12 December 2003 - 04:01 AM
John,
The refrigeration company is correct in that the classification is an electrical one and the chance of flammable vapors being present is not a reason to consider a fire relief case. However if in your plant flammable liquids can spill (either from the refrigeration unit, or from another source), and a pool fire under a vessel/heat exchanger/piping of the refrigeration unit can occur, then you're absolutely right in specifying a relief valve sized for a fire case.
In my experience you don't let a vendor size such a relief valve, but you specify the size based on your own sizing practices. If the vendor supplies you with dimensions of the unit and with the physical properties of the refrigerant, then sizing for a fire case is fairly straightforward. Afterwards you have to discuss with the vendor as to the best location on the unit. If it is an 'off-the-shelf' unit, then I can imagine that it will take some time and extra cost to add a nozzle of the right size, so a re-estimation might be required.
I hope this helps,
Diederik Zwart
The refrigeration company is correct in that the classification is an electrical one and the chance of flammable vapors being present is not a reason to consider a fire relief case. However if in your plant flammable liquids can spill (either from the refrigeration unit, or from another source), and a pool fire under a vessel/heat exchanger/piping of the refrigeration unit can occur, then you're absolutely right in specifying a relief valve sized for a fire case.
In my experience you don't let a vendor size such a relief valve, but you specify the size based on your own sizing practices. If the vendor supplies you with dimensions of the unit and with the physical properties of the refrigerant, then sizing for a fire case is fairly straightforward. Afterwards you have to discuss with the vendor as to the best location on the unit. If it is an 'off-the-shelf' unit, then I can imagine that it will take some time and extra cost to add a nozzle of the right size, so a re-estimation might be required.
I hope this helps,
Diederik Zwart
#3
Guest_John Moore_*
Posted 12 December 2003 - 09:48 AM
Many thanks, Deiderick.
#4
Guest_Ben Thayer_*
Posted 13 December 2003 - 12:21 AM
If this is truly a chiller unit and you use some decent insulation and stainless steel covering, you can also take credit for the insulation.
I agree with the basic premise that this is an electrical classification issue regarding the vapors. However, where there is vapor, there is frequently liquids. You should also be asking about how much oil is in the refrigeration package itself or is stored nearby for other equipment.
I agree with the basic premise that this is an electrical classification issue regarding the vapors. However, where there is vapor, there is frequently liquids. You should also be asking about how much oil is in the refrigeration package itself or is stored nearby for other equipment.
#5
Posted 16 December 2003 - 03:18 PM
On the chiller I have typically seen the PSV being sized for the tube rupture case which is normally higher than the fire case. However, my experience with refrigeration is specific to chilling high pressure gas, and I don't know if you are using this in the same application. If you are chilling something at low (or atmospheric) pressure then tube rupture may not be the limiting case, in which case I would see fire as the next criteria to consider.
If we are talking about the PSV on the discharge of the compressor, then the blocked flow case is usually more restrictive than fire case.
The only places in the referation system I can think of where you should have a fire case PSV would be the refrigerant accumulator.
If we are talking about the PSV on the discharge of the compressor, then the blocked flow case is usually more restrictive than fire case.
The only places in the referation system I can think of where you should have a fire case PSV would be the refrigerant accumulator.
Similar Topics
![]() Storage Tanks Diked Area Fire Protection Using Foam MakerStarted by Guest_mkhattaby_* , 30 Jan 2025 |
|
![]() |
||
Fire Relief Case - Relieving TemperatureStarted by Guest_alexzo1990_* , 06 Nov 2024 |
|
![]() |
||
Maximum Velocity For Piping In Fire Water Distribution System (Fire WaStarted by Guest_applepe_* , 06 Sep 2024 |
|
![]() |
||
![]() Fire Case Gas Expansion (Gas Filled & No Liquid)Started by Guest_moosa.akbar_* , 27 Aug 2024 |
|
![]() |
||
![]() Environmental Factor "f" Calculation In Psv Fire CaseStarted by Guest_mahmooddalvi09_* , 17 Aug 2024 |
|
![]() |