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Basic Control Valve  Sizing and Selection
DeZurik   Operation October 2005 Valve Sizing What is Valve Sizing? It is a procedure by which the  dynamics of a process system   are matched  to the  performance characteristics of a valve. This is to provide a control valve that will best meet the needs  of managing flow within that process system.
Flow Coefficient (C V ) ,[object Object],[object Object]
DeZurik   Operation October 2005 Valve Sizing Basic information requirements for effective valve sizing For the system: Pressure before and after the control valve,  Δ P Flow rate, quantity and units,  Q Process temperature with units,  T Properties of the media, (viscous, fiber suspension, gaseous its vapor pressure, sometimes molecular weight) For the control valve: Flow capacity (Cv), inherent throttling curve,  Kc (Cavitation Index), FL² (Critical Flow factor)
Delta P (  P) ,[object Object],[object Object],[object Object]
Flow Characteristics ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Why Use Equal Percentage ,[object Object],[object Object]
DeZurik   Operation October 2005 Valve Sizing - Cavitation What is cavitation and what does it do to valves ? Cavitation is a 2-stage activity where a portion of the liquid  media drops below vapor pressure. This part will boil (vaporize). In stage two, slightly downstream, pressure recovery takes place and the vapor bubbles collapse. The condition known as “critical flow” is an extension of cavitation in that it simply gets worse as the pressure drop increases. This is  to the point that changes (reductions) in downstream pressure no longer influence flow rate.
Fluid Recovery Factor (F L ) ,[object Object],Downstream of the vena contracta the fluid decelerates and consequently the pressure increases or recovers (giving us the term pressure recovery).  Different valve types exhibit different recovery  factors which becomes an important consideration in valve selection.
Fluid Recovery Factor (F L ) ,[object Object],F L ~(P 1 -P 2 )/(P 1 - P VC )
Valve sizing - Cavitation ,[object Object],[object Object],[object Object],[object Object]
DeZurik   Operation October 2005 Valve Sizing What is “Flashing”? It is a condition where the downstream pressure is below the  vapor pressure of the incoming fluid and allows some of the liquid to become vapor. Flashing does not create noise or damage in the valve as with  cavitation.  It can, however, create damage to the downstream  piping due to high velocity. A control valve will function quit well under these circumstances.  Yes!
DeZurik   Operation October 2005 Valve Sizing Characteristics Systems driven by centrifugal pumps lose pressure two ways As the flow increases the pump pressure declines As the flow increases pipeline friction losses increase Using a valve with equal percentage or parabolic characteristics will produce an installed characteristic that is more linear.
Inherent vs. Installed Characteristics ,[object Object],[object Object],[object Object]
DeZurik   Operation October 2005 Valve Sizing What is desired ? - After installation,   generally it should   be near linear. Why?  - To provide a more    predictable flow    change in response    to each incremental valve position change
 
Control Valve Seat Leakage ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Fluid Velocity ,[object Object],[object Object]
Noise and Vibration ,[object Object],[object Object],[object Object],[object Object],[object Object]
Rangability ,[object Object],[object Object]
Flow Direction ,[object Object]
DeZurik   Operation October 2005 Globe Valves
DeZurik   Operation October 2005 Globe Valves How do they work? - By linear (stroke) action - A contoured plug is lifted   out of a seat ring to allow    flow to pass - In most (not all) cases   flow comes in    “under the seat” - Conversely, pushing the    plug down into the seat causes closure Flow in
DeZurik   Operation October 2005 Globe Valves Unbalanced / Balanced Trim -  Unbalanced  has system    pressure acting against    the full area of the seat Single seated plug styles   are unbalanced   -  Balanced  has provisions for offsetting system    pressure Available in double seated    plug or balanced cage styles
DeZurik   Operation October 2005 Globe Valves Bodies & Bonnets - Configured as required   to meet valve style and    ANSI Class considerations - Removable bolted bonnets retain and/or support the    trim components
DeZurik   Operation October 2005 Globe Valves 3 Way configurations for Mixing and diverting. -Temperature control - Blending
DeZurik   Operation October 2005 Globe Valves Trim Components - Stem, plug, seat,    cage (if that style) &    guiding components - Made of alloy materials - Optional hardened seating surfaces when required  Top guided style Cage guided style
Noise and cavitation control trims By directing flow through a series of staged drops, these trims eliminate cavitation in liquid flow and provides multiple pressure breakdown for noise attenuation
 
DeZurik   Operation October 2005 Rotary Control Valves
DeZurik   Operation October 2005 Rotary Control Valves Design & Construction ANSI & ISA Face to Face
DeZurik   Operation October 2005 Rotary Control Valves V ported valves : Uses a ball segment that is  Always in contact with the seat. Up to 100:1 rangability. Eccentric type: Uses a plug that cams away  from the seat during opening Ideal solution for erosive services  Such as slurries and steam. Available with a range of flow  capacities.
DeZurik   Operation October 2005 High performance Butterfly Valve Ideal economic choice for  larger line sizes 50:1 Rangeability Modified equal percent flow Characteristic Fast accurate response to  Control signal
Actuators ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Actuators
Accessories ,[object Object],[object Object],[object Object]
Review material ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Control Valve Noise ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Hydrodynamic Noise ,[object Object],[object Object],[object Object],[object Object]
Ratings ,[object Object],[object Object]
Trim Materials ,[object Object],[object Object],[object Object],[object Object]
Materials of Construction ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Pressure Containment Materials ,[object Object],[object Object],[object Object],[object Object]
End Connections ,[object Object],[object Object],[object Object]
End Connections (cont.) ,[object Object],[object Object],[object Object],[object Object],[object Object]
Actuator Bench Range ,[object Object],[object Object],[object Object]
Instrument Control Signal ,[object Object],[object Object],[object Object]
Seat Leakage ,[object Object],[object Object],[object Object]
Generic Control Valve Types Features Comparison
RAVEN Trim Design Features ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],200:1 educing and ttenuating elocity rosion and oise
Noise Reduction ,[object Object],[object Object],[object Object],03/18/10
 
DeZurik   Operation October 2005 Rotary Control Valves

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Basic Control Valve Sizing and Selection

  • 1. Basic Control Valve Sizing and Selection
  • 2. DeZurik Operation October 2005 Valve Sizing What is Valve Sizing? It is a procedure by which the dynamics of a process system are matched to the performance characteristics of a valve. This is to provide a control valve that will best meet the needs of managing flow within that process system.
  • 3.
  • 4. DeZurik Operation October 2005 Valve Sizing Basic information requirements for effective valve sizing For the system: Pressure before and after the control valve, Δ P Flow rate, quantity and units, Q Process temperature with units, T Properties of the media, (viscous, fiber suspension, gaseous its vapor pressure, sometimes molecular weight) For the control valve: Flow capacity (Cv), inherent throttling curve, Kc (Cavitation Index), FL² (Critical Flow factor)
  • 5.
  • 6.
  • 7.
  • 8. DeZurik Operation October 2005 Valve Sizing - Cavitation What is cavitation and what does it do to valves ? Cavitation is a 2-stage activity where a portion of the liquid media drops below vapor pressure. This part will boil (vaporize). In stage two, slightly downstream, pressure recovery takes place and the vapor bubbles collapse. The condition known as “critical flow” is an extension of cavitation in that it simply gets worse as the pressure drop increases. This is to the point that changes (reductions) in downstream pressure no longer influence flow rate.
  • 9.
  • 10.
  • 11.
  • 12. DeZurik Operation October 2005 Valve Sizing What is “Flashing”? It is a condition where the downstream pressure is below the vapor pressure of the incoming fluid and allows some of the liquid to become vapor. Flashing does not create noise or damage in the valve as with cavitation. It can, however, create damage to the downstream piping due to high velocity. A control valve will function quit well under these circumstances. Yes!
  • 13. DeZurik Operation October 2005 Valve Sizing Characteristics Systems driven by centrifugal pumps lose pressure two ways As the flow increases the pump pressure declines As the flow increases pipeline friction losses increase Using a valve with equal percentage or parabolic characteristics will produce an installed characteristic that is more linear.
  • 14.
  • 15. DeZurik Operation October 2005 Valve Sizing What is desired ? - After installation, generally it should be near linear. Why? - To provide a more predictable flow change in response to each incremental valve position change
  • 16.  
  • 17.
  • 18.
  • 19.
  • 20.
  • 21.
  • 22. DeZurik Operation October 2005 Globe Valves
  • 23. DeZurik Operation October 2005 Globe Valves How do they work? - By linear (stroke) action - A contoured plug is lifted out of a seat ring to allow flow to pass - In most (not all) cases flow comes in “under the seat” - Conversely, pushing the plug down into the seat causes closure Flow in
  • 24. DeZurik Operation October 2005 Globe Valves Unbalanced / Balanced Trim - Unbalanced has system pressure acting against the full area of the seat Single seated plug styles are unbalanced - Balanced has provisions for offsetting system pressure Available in double seated plug or balanced cage styles
  • 25. DeZurik Operation October 2005 Globe Valves Bodies & Bonnets - Configured as required to meet valve style and ANSI Class considerations - Removable bolted bonnets retain and/or support the trim components
  • 26. DeZurik Operation October 2005 Globe Valves 3 Way configurations for Mixing and diverting. -Temperature control - Blending
  • 27. DeZurik Operation October 2005 Globe Valves Trim Components - Stem, plug, seat, cage (if that style) & guiding components - Made of alloy materials - Optional hardened seating surfaces when required Top guided style Cage guided style
  • 28. Noise and cavitation control trims By directing flow through a series of staged drops, these trims eliminate cavitation in liquid flow and provides multiple pressure breakdown for noise attenuation
  • 29.  
  • 30. DeZurik Operation October 2005 Rotary Control Valves
  • 31. DeZurik Operation October 2005 Rotary Control Valves Design & Construction ANSI & ISA Face to Face
  • 32. DeZurik Operation October 2005 Rotary Control Valves V ported valves : Uses a ball segment that is Always in contact with the seat. Up to 100:1 rangability. Eccentric type: Uses a plug that cams away from the seat during opening Ideal solution for erosive services Such as slurries and steam. Available with a range of flow capacities.
  • 33. DeZurik Operation October 2005 High performance Butterfly Valve Ideal economic choice for larger line sizes 50:1 Rangeability Modified equal percent flow Characteristic Fast accurate response to Control signal
  • 34.
  • 36.
  • 37.
  • 38.
  • 39.
  • 40.
  • 41.
  • 42.
  • 43.
  • 44.
  • 45.
  • 46.
  • 47.
  • 48.
  • 49. Generic Control Valve Types Features Comparison
  • 50.
  • 51.
  • 52.  
  • 53. DeZurik Operation October 2005 Rotary Control Valves

Hinweis der Redaktion

  1. Notes:
  2. Notes: