by Thomas Vaught » Sun Mar 18, 2007 3:26 pm
Formula is:
(Large drive pulley/smaller driven pulley) times
blower step-up ratio times motor speed
(7.5"/4.75") X 4.10 X 3450 = rpm
(1.5789) X 4.10 X 3450 = 22,334 rpm.
You will have lots of cfm (1200 at 60,000) available and the Vac for the test pressure will be pretty high. In reality with the lower blower rpm the PSI will be about 1/4th what they claim but will still be quite high for a flow bench.
Normal rule of thumb is that if the blower makes 30 psi at 60,000 rpm it will make 1/4th the pressure at 1/2 the speed. Your 22,334 rpm is about 75% of the 30,000 rpm. if the rpm was 30,000 the blower would be making 7.5 psi.
28" H20 is about 2" Hg or 1 psi.
Say your deal actually made 5.6 psi, that is
over 156 inches of water delta P.
In reality you will have a lot of cfm available and a lot of test pressure available.
JMO
Tom V.
ps Every centrifugal flow bench I have seen in operation had an adjustable throttle blade valve on the discharge of the blower to keep the blower out of surge. Test pressure was set with that butterfly valve.