C v1 , F L1
Fpv
(p −F )
Cv1= Cv 2
1
Fpv
(p − F )
L 1
2
L2
∆pm ax (1) = F
p1
∆pmax (2) =F
2
1
C v 2 ,F L 2
FL1 > FL 2
pv pvc p2I p2II p2III p2IV HANDBOOK
FOR CONTROL
VALVE SIZING
* PARCOL
HANDBOOK
FOR CONTROL
VALVE SIZING
CONTENTS
NOMENCLATURE
VALVE SIZING AND SELECTION
1
PROCESS DATA
2
VALVE SPECIFICATION
3
FLOW COEFFICIENT
3.1 KV coefficient
3.2 Cv coefficient
3.3 Standard test conditions
4
SIZING EQUATIONS
4.1 Sizing equations for incompressible fluids (turbulent flow)
4.2 Sizing equations for compressible fluids
(turbulent flow)
4.3 Sizing equations for two-phase fluids
4.4 Sizing equations for non turbulent flow
5
PARAMETERS OF SIZING EQUATIONS
5.1 Recovery factor FL
5.2 Coefficient of incipient cavitation xFZ and coefficient of constant cavitation Kc
5.3 Piping geometry factor Fp
5.4 Combined liquid pressure recovery factor and piping geometry factor of a control valve with attached fittings FLP
5.5 Liquid critical pressure ratio factor FF
5.6 Expansion factor Y
5.7 Pressure differential ratio factor xT
5.8 Pressure differential ratio factor for a valve with attached fittings xTP
5.9 Reynolds number factor FR
-1-
* PARCOL
Symbols
Description
Units (note)
Cd
Specific flow coefficient = Cv/ d2
various
Cv
Flow coefficient
U.S. gallons/min
d
Nominal valve size
mm
D
Internal diameter of piping
mm
Fd
Valve style modifier
dimensionless
FF
Liquid critical pressure ratio factor
dimensionless
FL
dimensionless
FP
Liquid pressure recovery factor for a control valve without attached fittings Combined liquid pressure recovery factor and piping geometry factor of a control valve with attached fittings
Piping geometry factor
dimensionless
FR
Reynolds number factor
dimensionless
Fγ
Specific heat ratio factor = γ/1.4
dimensionless
KB1