Gas cooling in a pipe and pressure drop
Gas cooling in a pipe and pressure drop
(OP)
I'm working on a design in which a cooler is used to bring down the temperature of a gas in a pipe from 80C to 50C. Is that going to cause a significant pressure drop in the pipe?





RE: Gas cooling in a pipe and pressure drop
Good luck,
Latexman
RE: Gas cooling in a pipe and pressure drop
"We don't believe things because they are true, things are true because we believe them."
RE: Gas cooling in a pipe and pressure drop
RE: Gas cooling in a pipe and pressure drop
From an ideal gas point of view, if PV = nRT and T decreases, then P or V must decrease. What will happen?
RE: Gas cooling in a pipe and pressure drop
RE: Gas cooling in a pipe and pressure drop
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RE: Gas cooling in a pipe and pressure drop
However, for an open system (flowing), I'd expect the pressure to be a function of the source pressure, destination pressure, system pressure drop, fluid physical properties, and bernouilli's law. I don't see how cooling or heating a flowing gas is going to make a pressure change by itself. Yes, the physical properties of the gas will change and that will change pressure drop somewhat, but there is not going to be a step change in pressure across a cooler or heater solely because of the temperature change.
If you blow through a straw that runs into and out of a pot of boiling water to exit to atmosphere, it will NOT come out at a pressure higher than atmospheric pressure.
Good luck,
Latexman
RE: Gas cooling in a pipe and pressure drop
I think you have a feel for the subject. The arithmetic supports it.
If we start with an ideal gas (say air) then as said above PV=nRT, so P1V1/(n1RT1)=1=P2V2/(n2RT2). Now since the continuity equation says that mass flow rate at any point in a closed system is the same as any other point in the system, we can choose a control volume (V2) so that n1=n2. Let's say that V1 equals a unit volume so:
P2V2=P1V1*(T2/T1)
It is important to note that we don't have any idea what size V2 has to be to hold the same "n" as V1. So while the product of P2V2 will have to be about 9% lower than P1V1, we have absolutely no way of knowing the magnitude of either variable (P2 could be higher than P1 and V2 a lot smaller than V1, or vice versa, or any combination).
I don't think that there is any analytical way to determine either P2 or V2, but my observations have been that pressure at the outlet of a cooler is very close to inlet pressure minus friction within the cooler.
David