Steam flow rate (loss) through top of condensate tank
Steam flow rate (loss) through top of condensate tank
(OP)
Hi there,
I have two questions here but the first and most important is I'm trying to find out the flow of steam from the top of a return condensate tank from a sugar mill pan area so I can work out the condenstae loss. The pressure in the water tank is 75kpa and their is an open 6 inch gate valve on top of the tank which lets out the steam from the water.
The second is I want to put some sort of steam trap on this 6 inch outlet pipe to save this condensate loss. Is this a possibility for this application?
Thanks in advance,
I have two questions here but the first and most important is I'm trying to find out the flow of steam from the top of a return condensate tank from a sugar mill pan area so I can work out the condenstae loss. The pressure in the water tank is 75kpa and their is an open 6 inch gate valve on top of the tank which lets out the steam from the water.
The second is I want to put some sort of steam trap on this 6 inch outlet pipe to save this condensate loss. Is this a possibility for this application?
Thanks in advance,





RE: Steam flow rate (loss) through top of condensate tank
You might try using a heat exchanger on the vent, if you have a use for the recovered heat. I think you'll find the steam flow isn't as much as it appears. In any event, it'll all come down to economics.
Be VERY careful if you're considering installing something like a trap on this vent line. All a trap is, is an automatic valve. You could pressurize this tank to dangerous levels, or back condensate up your process due to increased back-pressure, causing problems there. The tank will need to be vented for the condensate pumps to work.
RE: Steam flow rate (loss) through top of condensate tank
Have you also got an actual formula for working out the steam flow?
RE: Steam flow rate (loss) through top of condensate tank
In the Crane literature, look in chapter 3, page 22. Another approach is to use a table in "Hook-Ups", which shows the percentage of flash steam from given pressures to atmospheric. (In the 11th edition, the table is on page 41.) The table shows 2.9% of condensate at 10 PSIG will flash to steam when dropped to atmospheric pressure.