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PROCESS PRESENTATION ON
CONTROL VALVE DESIGN
 BY
 ELOHO ASOMBA
 26-Aug -2011
CONTROL VALVE DESIGN
TYPES OF VALVES
TYPES OF VALVE
CHARACTERISTICS
WHY IS PROPER VALVE SIZING
IMPORTANT
SIZING CONTROL VALVE
PROCEDURE
TYPES OF VALVES
Process_Presentation_on_Control_Valve_De.ppt
BALL VALVE (schematic
diagram)
GATE VALVE
GATE VALVE (schematic
diagram)
CHECK VALVE
NEEDLE VALVE
ANGLE VALVE
BUTTERFLY VALVE
BUTTERFLY VALVE
(schematic diagram)
GLOBE VALVE (schematic
diagram)
TYPES OF VALVE
OPERATION
CHARACTERISTICS
 EQUAL PERCENTAGE
 QUICK OPENING
 LINEAR
Process_Presentation_on_Control_Valve_De.ppt
SIZING CONTROL VALVE
PROCEDURE
CONTROL VALVE DESIGN
STEPS
1. DETERMINE Cv
2. DETERMINE IF THERE ARE
UNUSUAL CONDITIONS
STEP 1
DETERMINATION OF Cv
Select appropriate equation
Calculate initial Cv based on assumed Xt
Select from manufacturer’s catalogue Cv greater than calculated Cv
Re- calculate Cv based on manufacturer’s catalogue value for Xt
Iterate till calculated Cv equals manufacturer’s Cv
Process_Presentation_on_Control_Valve_De.ppt
Process_Presentation_on_Control_Valve_De.ppt
Process_Presentation_on_Control_Valve_De.ppt
Process_Presentation_on_Control_Valve_De.ppt
FACTORS AFFECTING
DETERMINATION OF CV
 Cv-Operating conditions maximum flow and
minimum flow
 Fluid properties e.g vapor pressure
 Rangeability (valve travel with relation to Cv) of
valve
STEP 2
UNUSUAL CONDITIONS
 SOURCE OF PIPE VIBRATION
 CAVITATION LEADING TO VALVE BODY
DAMAGE WHICH IN TURN PASSES ON TO
THE PIPING SYSTEM
 FLASHING IN VALVE RESULTING TO
BUBBLE COALESCE CAUSING SLUG OR
PLUG IN PIPES AT LOW DOWNSTREAM
PRESSURE
TERMINOLOGIES
Vapor pressure
Vena contracta
Cage / Trim
Cavitation
Flashing
Process_Presentation_on_Control_Valve_De.ppt
VALVE TRIM (VALVE INTERNALS)
VALVE TRIM
Process_Presentation_on_Control_Valve_De.ppt
REMEDIES
 Replace valve with TRIM of larger FL value
 Increase back pressure downstream of valve
 Install valve at a lower elevation than the inlet
and outlet lines
 Install two valves in series
 Use oversize valve body
THANKS
QUESTIONS
 (Q) What is CV factor?
 (A) CV is a dimensionless value that relates the volume of flow through a valve
in (gpm) that gives 1 psi pressure drop across a valve at 60oF .
 (Q)What is Dp (pressure drop)?
 (A) Dp is the difference between initial pressure and final pressure in a
defined system.
 Why is Dp important?
 (A) Dp is what makes flow possible Dp will enable the designer to know the
energy that would be necessary to flow a fluid to the required point at the
expected arrival pressure
 (Q)What factors determine Dp across a valve
 (A)i Flow path within the valve, ii Fluid flow rate
 (Q)A full bore 1” ball valve has a CV of 40 and a diaphragm valve of equal
nominal size (1’’) has a CV of 15. Why is the difference in CV of these valves?
 (A)A diaphragm valve has a more tortuous internal than a ball valve

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Process_Presentation_on_Control_Valve_De.ppt

Editor's Notes

  • #4: BALL VALVE
  • #6: GATE VALVE
  • #8: CHECK VALVE
  • #9: NEEDLE VALVE
  • #11: BUTTERFLY VALVE
  • #13: GLOBE VALVE