Cv with piping geometric factor consideration equations are:
Where Fp (R)
Where:
d : Valve inlet diameter
D : Internal diameter of the pipe
K : Head loss coefficient of a device,
dimensionless
N2 : constant to suit the measurement
unit, 890
The factor ∑K is the sum of the
effective velocity head coefficient of all fittings.
Where:
KB : Bernoulli
coefficient, dimensionless
K1,2 : The
resistance coefficient for the inlet and outlet fittings, dimensionless
Bernoulli coefficient is accounted to
compensate the changes of pressure due to differences in stream area and
velocity.
Inlet reducer:
Outlet increaser :
Subscripts
1 : Upstream
conditions
2 : Downstream
conditions
Example:
PV-A case 1:
Cv for Gas sizing is
1 lb/hr x (1 lb-mole/21.5 lb) x
(359.05 std cu ft/ 1 lb-mole) = 16.7 scfh
W = 21088 SCFD = (21088 ft3/day) x (day/ 24 hr) x (1 lb/hr/16.7scfh) = 52.61
lb/hr
X =
72.52/217.56 barg/bra = 0.33
P1 = 15 barg = 217.56 psig
ρ1= 12.15 kg/m3 = 0.7585 lb/ft3
Y = 1 – (x/3*(Cp/Cv / 1.4)*xT)
d
= 1 in (valve size)
D = 2
in (Line size)
Fisher catalog is used as a reference
xT = 0.67 for 80% opening Globe valve
Y = 1 – (0.33 / 3 * (1.263/ 1.4 )
*0.67) = 0.8257
Cv = 52.61 / (63.3 * (0.8257)*(√0.33*217.56*0.7585)
Cv = 0.1361 (identical value with the
Instrucalc 5.1 calculation result)
Cv with piping geometric factor consideration
= 1.5 (1 – (1)2
/ (2)2 ) 2
= 0.843
Piping Geometric factor
Cv = 17.2 from table.
N2 = 890, from
table below
Fp =
(((0.843)*(17.2)2/ (890)*(1)4 ) + 1)-1/2
=
0.883
(When possible it is recommended that
Fp factor be determined by using the specific
valve in actual tests)
Cv = 0.1361 / 0.883
Cv = 0.1546
The Cv with Fp factor consideration value is very close to the
Cv used initially for this calculation. (0.1361 versus 0.1546). therefore it
can be neglected.
The
conclusion is that 1 inch valve opened to about 80-percent of total travel
should be adequate for the required specifications.
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