Kdolph
Chemical
- Oct 16, 2012
- 15
Hi, I attached a diagram of the situation.
We want a purge of 20 m3/hr. This purge is discarted as it is seen in the isometric view, through a 3” pipe. IN the water/steam separator of the evaporator the average pressure/temperature are 2,5 bara and 127,4°C so I assume this is the condition at the exit of the purge. This purge go to an vertical 8” pipe that works as a collector and due to the pressure reduction some steam flashes out the collector.
So if I want to measure the flowrate of the purge. Could I do it in the next way:
Installing an magnetic flowmeter downstream the collector pipe for measuring the water part of the purge and estimate the flashing with some thermodynamic correlation? I think it is not possible to measure the flowrate upstream the pipe collector because of the the closeness of the pressure vapour with the system pressure.
http://files.engineering.com/getfile.aspx?folder=f81381a2-ffd0-4dc4-8347-7344f9452c79&file=Purge.pdf
We want to measure the flowrate of the purge of an evaporator. This works as a distiller (it evaporates water), so the purge is just water with high levels of conductivity.We want a purge of 20 m3/hr. This purge is discarted as it is seen in the isometric view, through a 3” pipe. IN the water/steam separator of the evaporator the average pressure/temperature are 2,5 bara and 127,4°C so I assume this is the condition at the exit of the purge. This purge go to an vertical 8” pipe that works as a collector and due to the pressure reduction some steam flashes out the collector.
So if I want to measure the flowrate of the purge. Could I do it in the next way:
Installing an magnetic flowmeter downstream the collector pipe for measuring the water part of the purge and estimate the flashing with some thermodynamic correlation? I think it is not possible to measure the flowrate upstream the pipe collector because of the the closeness of the pressure vapour with the system pressure.