marcoci
Guest
Good morning.
I have been looking on the net for a few days more information about the sizing of pipes for diathermic oil plants. I found several tables, publications and articles with the calculation of load losses, diameter calculations etc. that depend (clearly) always on the flow and therefore on the speed.
the data to be fixed a priori is therefore the speed:
I have been looking on the net for a few days more information about the sizing of pipes for diathermic oil plants. I found several tables, publications and articles with the calculation of load losses, diameter calculations etc. that depend (clearly) always on the flow and therefore on the speed.
the data to be fixed a priori is therefore the speed:
- I am well that the speed in boiler gives the builder, but the speed for example in an oil/smoke heat exchanger (where the fumes give heat...) will be like that in boiler?
- what speed I choose for the connection pipes between the exchanger (oil/fume) and user, for example, an evaporator, an oil/water exchanger or an orc?