ta1234
Marine/Ocean
- Jan 24, 2012
- 15
Hi Everyone,
I would like to set up a thermodynamic/heat transfer model of the following system. The system is a closed system which cools an electronic device which is attached to a heat sink, the water circulates through tubes between the heat sink and a cold plate, rejecting heat to the cold plate. The outer surface of the cold plate will be kept at a constant temperature. I know the heat load output, cold plate outer wall temperature, device temperature limit and the wetted surface areas of the heat sink and cold plate.
I would like to generate a model which will allow me to adjust parameters such as heat sink and cold plate wetted area and surface temperature, giving me a required mass flowrate of water. I have come up with a couple of models but I still have not enough equations for the number of unknown variables.
The main thing that I'm finding quite difficult is that using the Dittus Boelter equation, the convection coefficient for a pipe wall is dependent on fluid flowrate (Link). Does anyone know a simplified way of calculating pipe convection coefficients which avoids dependency on flowrate?
Can anyone provide me with some pointers for a good way to solve this problem? I'm not totally sure where I should be drawing my system boundaries? I'm not looking for anyone to solve it for me, just a method and perhaps which heat balances to use for my system.
Many thanks in advance.
I would like to set up a thermodynamic/heat transfer model of the following system. The system is a closed system which cools an electronic device which is attached to a heat sink, the water circulates through tubes between the heat sink and a cold plate, rejecting heat to the cold plate. The outer surface of the cold plate will be kept at a constant temperature. I know the heat load output, cold plate outer wall temperature, device temperature limit and the wetted surface areas of the heat sink and cold plate.
I would like to generate a model which will allow me to adjust parameters such as heat sink and cold plate wetted area and surface temperature, giving me a required mass flowrate of water. I have come up with a couple of models but I still have not enough equations for the number of unknown variables.
The main thing that I'm finding quite difficult is that using the Dittus Boelter equation, the convection coefficient for a pipe wall is dependent on fluid flowrate (Link). Does anyone know a simplified way of calculating pipe convection coefficients which avoids dependency on flowrate?
Can anyone provide me with some pointers for a good way to solve this problem? I'm not totally sure where I should be drawing my system boundaries? I'm not looking for anyone to solve it for me, just a method and perhaps which heat balances to use for my system.
Many thanks in advance.