patdh1028
Mechanical
- Jan 31, 2012
- 39
Hello all,
I'm attempting to work through a heat transfer problem and I was hoping to get some advice and clarity about how to model it.
I have a corrugated, double-braided SS tube carrying hot (500-800degC) gas at about 30 bar over a length of a few meters. Tube motion is minimal, so it is just sitting in standard conditions. The purpose of the calculation is to estimate temperature drop in the gas and figure out how much insulation we need to minimize it.
So I have a few heat transfer conditions. From the gas to the tube is forced convection, then conduction through the tube, then free convection to surrounding air from the outer tube surface.
The way I was thinking of approaching this was taking a small length of hose, assuming that its surface temp was equal to gas temp, and determining what the rate of heat transfer to surroundings would be, removing that energy from the gas, and then iterating that method for the full length (i.e. the temperature of the gas at the outlet of my first small length of pipe would be the new assumed surface temp of the next small length of pipe).
The thing I'm not sure about is where free vs. forced convection comes in. Does the fact that convection is free on the outside of the tube mean that the total heat transfer is limited to that rate, or does the turbulent, high temp. flow inside the tube mean that the rate of heat transfer to the surroundings is higher?
I'm attempting to work through a heat transfer problem and I was hoping to get some advice and clarity about how to model it.
I have a corrugated, double-braided SS tube carrying hot (500-800degC) gas at about 30 bar over a length of a few meters. Tube motion is minimal, so it is just sitting in standard conditions. The purpose of the calculation is to estimate temperature drop in the gas and figure out how much insulation we need to minimize it.
So I have a few heat transfer conditions. From the gas to the tube is forced convection, then conduction through the tube, then free convection to surrounding air from the outer tube surface.
The way I was thinking of approaching this was taking a small length of hose, assuming that its surface temp was equal to gas temp, and determining what the rate of heat transfer to surroundings would be, removing that energy from the gas, and then iterating that method for the full length (i.e. the temperature of the gas at the outlet of my first small length of pipe would be the new assumed surface temp of the next small length of pipe).
The thing I'm not sure about is where free vs. forced convection comes in. Does the fact that convection is free on the outside of the tube mean that the total heat transfer is limited to that rate, or does the turbulent, high temp. flow inside the tube mean that the rate of heat transfer to the surroundings is higher?