Control Valve Sizing (pdf)

Control Valve Sizing is a procedure of deciding the appropriate type and size of the control valve to optimally satisfy the requirements of fluid flow management. This article will describe the Control Valve Sizing Procedure with some details of related headings like Valve Flow Terminologies, Control Valve Characteristics, Cavitation, Flashing, etc.

Control Valve Flow Terminologies

  • Pressure Drop: It is the difference between the upstream pressure and downstream pressure of the control valve.
  • Cv (Flow Coefficient): The Cv is the number of U.S gallons of water flowing during one min. at 60 Deg F through a restriction and the pressure drop through this restriction is 1 psi.
  • Vena contracta: The vena contracta is where the jet of flowing fluid is smallest.
  • Choked or critical flow: The flow is said to be choked when:
    1. Vena contracta is filled with vapor from cavitation or flashing.
    2. Fluid velocity at vena contracta reaches sonic.
  • Vapor pressure: It is the pressure at which the given liquid will vaporize at the given temperature
  • Cf (Critical Flow Factor): The Cf factor is an indication of the valve’s vena contracta pressure relative to the valve’s outlet pressure.

Pressure Recovery Factor

Pressure Recovery Factor
Pressure Recovery Factor

Control Valve Characteristics

Control Valve Characteristics are determined by the Design of the valve Trim.

Inherent Characteristics

Expresses the relationship between the valve travel and flowrate for a constant pressure drop across the control valve.

  • Quick Opening-On-off control with no throttling.
  • Linear-Flowrate is linear with plug position.
  • Equal Percentage-Equal increment of travel produces an equal % change in the flow.

Relationship between % Flow & % Valve Opening

A typical Characteristics of Equal percentage Valve

Typical Valve Characteristics
Typical Valve Characteristics

Installed Characteristics

  • Installed Characteristics are what really matter to a process engineer.
  • Expresses the relationship between the valve travel and flowrate for a varying pressure drop across the control valve.
  • Installed characteristics of Equal percentage valve is nearly linear when pressure drop varies with the flow.

Selection of Control Valve Characteristics

Following method should be used:

  • Choose Equal percentage characteristics, if Pvalve < 70% of system Pressure Drop
  • Choose Linear characteristics, if Pvalve > 70% of system Press. Drop

Data Required for Control Valve Sizing

  • Operating Flowrates:– Maximum flow; Normal flow; Minimum flow
  • Fluid Properties:-Fluid Phase; Molecular Weight; Vapor Pressure; Ratio of specific heats; Compressibility; Specific gravity; Viscosity
  • Parameters:- Source Pressure; Destination pressure; Design pressure; Operating temperature; Shut off Pressure

Control Valve Sizing Procedure

Rangeability:

Rangeability is the ratio of maximum to minimum controllable Cv. It is common practice to select a control valve within the following range:

Maximum flow:

  • Valve opening <= 95 % for Equal Percentage Trim
  • Valve opening <= 90 % for Linear and Quick Opening Trim

Normal flow: Valve opening should be at least 60 %

Minimum flow: Valve opening >= 10 %

Control valve do, what they are told !

The need for the fail-safe position

  • Fail to Open (FO)
  • Fail to Close (FC)
  • Fail Last

FC / FO schematic

Fail Open- Fail Close

Double Acting Actuator

Double Acting Actuator

Control Valve Sizing Calculation

Sizing control valve for Maximum flow-

  • Estimate Max. required flow
  • Calculate the system pressure drop without valve
  • Choose a valve that will pass maximum flow when about 90% open.

Size for minimum flow-

  • Follow the same procedure as above and choose a valve that will pass minimum flow when about 10% open

Control Valve Sizing for Normal flow-

  • Follow the same procedure and choose a valve that will pass normal flow when about 60-70% open

Pressure Drop calculation:

Pressure Drop calculation

Cv Calculation

The flow co-efficient or Cv is an important parameter for control valve sizing. This is also known as valve co-efficient. It specifies the number of U.S gallons of water that flows through a restriction in one minute at 60 Deg F keeping the pressure drop through this restriction is 1 psi. The Cv calculation procedure for liquid flow, gaseous/steam flow and two-phase flow are provided below for reference.

Cv Calculation Liquid flow:

Cv Calculation Liquid flow

Cv Calculation Gas and Steam:

Cv Calculation Gas and Steam

Cv Calculation Two Phase flow:

Cv Calculation Two Phase flow

Effect of Reducers on Control Valve Sizing

  • Decrease in actual valve capacity
  • Creates additional pressure drop in the system
  • Flow Capacity Correction Factor (R)
Flow Capacity Correction Factor

Thumb Rules for Control Valve Sizing

Few general thumb rules prevalent in industries while sizing control valves are:

  1. Assign the system and size the control valve such that:
    • Pvalve = 25% system press. Drop (including control valve) or Pvalve = 1/3rd system press. Drop (excluding control valve)
  2. The valve to be sized to operates between 20 to 80% open at the maximum required flow rate.
  3. The minimum opening should not be less than 20% at the minimum flow rate to provide a safety margin

Cavitation and Control Valve Sizing

Cavitation is a two stage phenomena:

  • Formation of vapor bubbles
  • Collapsing of vapor bubbles

Cavitation Phenomena:

Cavitation Phenomena

Negative Effects of Cavitation:

  • Resists the fluid flow
  • Causes severe vibrations
  • Erodes metal surface
  • Generates high noise levels

Cavitation Countermeasures:

  • Select valve style that has Cf value greater than required for the application
  • Increase pressure at upstream of the control valve by reducing elevation in the piping system
  • Installation of the orifice at the downstream of the control valve

Flashing

Definition – Pressure at the valve outlet remains below vapour pressure

Negative effects-Two phase flow in the downstream of control valve; Erosion

Limitations in Control Valve Performance

Noise-

  • 85 dBA for process control and daily service applications
  • 90 dBA for infrequent letdown and recirculation
  • 5 dBA credit may be taken for insulation.

Vibration and Erosion limits

Liquid Service-

  • Trim Exit vel. < 30 m/s for single phase liquids
  • Trim Exit vel. < 23 m/s for cavitating, flashing erosive services

Gas Service

  • Trim Exit vel. Head > 480 kPa for continuous service
  • Trim Exit vel. Head > 1030 kPa for infrequent service

Positioner

A position controller (servomechanism) that is mechanically connected to a moving part of a final control element or its actuator and that automatically adjusts its output to the actuator to maintain the desired position in proportion to the input signal.

Control Valve Sizing Standard

Widely used control valve sizing standards are

  • ISA75.01.01, Control Valve Sizing Equations
  • IEC 60534-2-1
  • DEP 32.36.01.17-Gen, Control valves – selection, sizing, and specification

Few more Resources for you…

Details about control valves
Ball Valve Design Features: A Literature
A brief article on Valve Inspection & Testing
An article on ROTARY SELECTOR VALVE (RSV) and MULTIPHASE FLOW METER (MPFM)
Selection of Valves: A Few Guidelines
Piping Design and Layout Basics
Piping Materials Basics
Piping Stress Analysis Basics
Few Job Opportunities for you..

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Anup Kumar Dey

I am a Mechanical Engineer turned into a Piping Engineer. Currently, I work in a reputed MNC as a Senior Piping Stress Engineer. I am very much passionate about blogging and always tried to do unique things. This website is my first venture into the world of blogging with the aim of connecting with other piping engineers around the world.

One thought on “Control Valve Sizing (pdf)

  1. I like how you mentioned that when opened at the maximum flow rate, appropriate valve sizing should be operating around 20 to 80%. The manager of the warehouse I work in is thinking of getting a new solenoid control valve because he noticed the other day that our current valves weren’t working as efficiently as they used to. It seems like a good idea for my manager to think about getting equipment from a reputable company that allows the flow rate we need to operate our machinery as best as possible.

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