Flashing Accross the Control Valve
I am designing the piping system for my treater desanding system. the
treater is operationg at about 80 psig and and i have 2" sch. 160 line
coming out of treater going into an atmospheric tank. the piping is on
the water side of the treater. now i have to install a butterfly valve
on this 2" line to take some pressure drop across the valve. water is at
130 C in the treater (i know this is very high temperature but i am
dealing with very heavy oil thats why temperature is too high). now as
soon as i come out of the treater and accross the valve the pressure
will drop and there will be some flashing of water due to high water
temperature and pressure drop across the valve. i cant increase the size
of my valve because i need certain pressure drop across the valve. my
questions is what else can be done to avoid flashing if i cant change
the valve size and i need lot of pressure drop? what damage flashing can
cause in the piping and valve? is there a better way to avoid this
situation?
I am not trying to control the flow here all i need is
some pressure drop across the valve. the valve is snap acting not
modulating and i cant modulate the valve because of the sand in water
which will eat away the valve seat very quickly if i try to modulate it.
any sugesstions?
Flashing WILL happen regardless of the style of valve if the discharge pressure is less than the vapor pressure.
If
you have a full line of hot fluid and snap open a butterfly valve, the
flashing might happen throughout the system. This could lead to slug
flow and steam hammer.
Usually flashing damage is erosion from
the high-velocity droplets downstream of the throttling orifice. You
did not specify what type of butterfly valve but a rubber-seated valve
is unlikely at these temperatures. I assume then they you have a
high-performane double-offset valve.
If you'll mount the
butterfly valve ON the flash tank, preferably with the shaft upstream,
most of the flashing will happen as the flow drops into the flash tank
and not inside the valve or piping. You can modulate with a butterfly
valve, just don't pick an operating point below about 30 degrees open or
the flashing and its attendant high velocity may occur across the seats
and that may cause erosion as you feared.
I ran the numbers
for water. You'll get 5.5% flash, with an expansion rate of 8.7. You
didn't specify the flowrate, but if you come into the valve at 10ft/sec,
the average velocity of the mixture out would be 87 ft/sec. That's
faster than I would want sandy water droplets flowing through MY
pipe.
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