Under a transient condition, such as a pump trip, there is a significant potential for column separation and subsequent severe water hammer as the vapor bubble collapses. We have looked into a number of options to break vacuum under this situation to prevent water hammer and have decided to install a U-tube vent. The strategy is that, under all “normal” operating conditions, the water will remain in the U-tube and act as a loop seal. At or just after column separation, the pressure in the main circ water piping will be low enough to lift the water out of the loop seal and admit air into the main piping, breaking the vacuum.
I have been asked to verify the design. I am comfortable with the concept in general, but I am concerned about the U-tube depth. It needs to be deep enough to maintain a seal under normal operation, yet shallow enough to ensure that, when there is column separation, the seal will be broken.
The problem is in deciding what temperatures (vapor pressure) and densities to use and whether to measure to the top or bottom of the “U.” The cooling water should be less than 60 F all the time. The power house (ambient) could be over 100 F for a few hours a day on some of the hottest days of the year.
My thinking is as follows:
The top of the pipe at the U must be low enough to maintain a seal. For this condition, use the lightest water (density at 100 F is 61.966 lb/ft^3) to determine the column height that would be lifted considering ambient pressure (14.55 psia for our location in Toronto) on one side and 1.35 psia on the other. For this I get 366 inches. The distance from the centerline of the main pipe to the top of the U must be more than 366 inches.
The bottom of the U must not be so deep that the column above it cannot be lifted when the pressure drops below the trigger level in the main pipe. For this condition, I would use the heaviest water expected (density at 60 F should be ok, so use 62.364 lb/ft^3), but assume that temperature at the top of the column is 100 F (use vapor pressure of 0.95 psia for water). I get a maximum column depth of 377 inches (14.55 psia – 0.95 psia pressure difference and 62.364 lb/ft^3 density). The distance from the centerline of the main pipe to the bottom of the pipe cannot be any greater than 377 inches (making the current depth of 387 inchess too deep). The designing engineer asserts that we can use the top of the pipe at the U for this condition since “that’s where the air will come through first.”
Before I push back too hard on the depth of this thing, I wanted to see if anyone here has any comments or advice.
I hope this lengthy diatribe makes some sense.
Thanks for any help,
Mike