Venturi Meter:
Fluid
enters a venturi meter through a converging cone (angle of
15o
to 20o). It then
passes through the throat
which has the minimum cross- sectional area, maximum velocity,
and minimum pressure in the meter. The fluid
then slows down through a diverging cone (angle 5o to 7o) for the transition back to
the full pipe diameter.
Figure 1 shows the shape of a typical venturi
meter and the
parameters defined above as
applied to this type of
meter. D2 is the diameter of the throat and P2 is the pressure
at the throat. D1 and P1 are the diameter and pressure,
respectively, in the pipe
before entering the converging portion of the
meter.
Figure 1. Venturi
Meter Parameters
Due to the smooth transition to the throat and gradual transition
back to full pipe diameter, the head loss through a
venturi meter is quite low and the discharge
coefficient is quite high. For a venturi
meter the discharge coefficient
is typically called the
venturi coefficient, Cv, resulting in the
following equation:da
The value of the venturi coefficient, Cv, will typically range
from 0.95 to nearly one. In ISO 5167 (ISO 5167-1:2003
– see Reference #2 at the end of this course),
Cv is given as 0.995 for cast iron or machined venturi meters and 0.985 for welded sheet metal venturi meters meeting ISO specifications, all for Reynold’s
Number between 2 x 105 and 106. Information on the venturi
coefficient will typically be provided by the
venturi meter manufacturers.
Example #1: Water at 50 oF is flowing through
a venturi meter with a 2 inch throat diameter in a 4 inch diameter pipe.
Per manufacturer’s information, Cv =
0.99 for this meter under these flow conditions. What is the flow rate through the meter if the pressure difference, P1 – P2, is measured as 8 inches
of Hg.
Solution: The density
of water in the temperature range from 32oF to 70oF is 1.94 slugs/ft3. A2 = πD22/4 = π(2/12)2/4 = 0.02182 ft2. β = 2/4 = 0.5. Converting the pressure difference to lb/ft2: P1 – P2 = (8 in Hg)(70.73
lb/ft2/in Hg) = 565.8 lb/ft2. Substituting all of these values into equation
(3):
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