Flow control manual
Valmet
				This manual is intended to give an overview of the role of control valves in the behavior of a process control loop. It consists of information on fluid behavior, valve installed performance, and the theory and practice of control valve sizing.
Table of contents
- 
Foreword
 - 
1. Introduction to pipeline flow
 - 
2. Control valve installed performance
- 2.1 General
 - 2.2 Operating conditions
 - 2.3 Selecting a control valve
 - 2.4 Control valve flow characteristics
- 2.4.1 Inherent flow characteristics
- - A. Quickopening inherent flow characteristics
 - - B. Linear inherent flow characteristics
 - - C. Equal percentage inherent flow characteristics
 
 - 2.4.2 Installed flow characteristics
 - 2.4.3 Installed gain
 - 2.4.4 Calculation methods
- - Procedure
 - - Process model and DPm selection
 - - A. Liquid flow
 - - B. Gas flow
 
 - 2.4.5 Control valve accuracy
 - 2.4.6 Control valve characterization
 
 - 2.4.1 Inherent flow characteristics
 
 - 
3. Liquid flow
- 3.1 General
 - 3.2 Sizing equations for liquid flow
- - Factors FF, FR, FP, and FLP
 
 - 3.3 Cavitation and flashing
- 3.3.1 Cavitation phenomenon
 - 3.3.2 Investigating the existence of cavitation
 - 3.3.3 Flashing of liquids
 - 3.4 Cavitation and hydrodynamic noise abatement
- - Velocity control
 - - Acoustic noise and bubble size control
 - - Location control
 - - Flat baffle plates
 - - Orifice plates
 - - Sizing baffle and orifice plates
 - - Example of noise and cavitation abatement
 
 - 3.5. Hydrodynamic noise prediction for valves
 - 3.6 Hydrodynamic noise prediction for baffle and orifice plates
 - 3.7 Recommended flow velocities for liquids 
 
 
 - 
4. Gas and steam flow
- 4.1 General
 - 4.2 Sizing equations for gas and steam flow
 - 4.3 Aerodynamic noise
- 4.3.1 Aerodynamic noise generation
 - 4.3.2 Aerodynamic noise prediction
- - Calculation method to predict aerodynamic noise levels
 
 
 - 4.4 Atmospheric venting
 - 4.5 Aerodynamic noise abatement
- 4.5.1 Source treatment
- - Velocity control
 - - Acoustic control
 - - Location control
 - - Diffusers
 - - Attenuator plates
 - - Source treatment examples
 
 - 4.5.2 Path treatment
- - Silencers
 - - Insulation
 - - Heavy downstream pipe schedule
 
 
 - 4.5.1 Source treatment
 - 4.6. Recommended flow velocities and limits for noise levels
 
 - 
5. Multi-phase flow
- 
- 5.1 General
 - 5.2 Two-phase flow of liquid and gas
- - Sizing equations
 - - Choked flow
 - - Accuracy
 
 - 5.3 Pulpstock
- 5.3.1 Studies about pulpstock
 - 5.3.2 Pulpstock behavior in control valves
- - The effect of differential pressure on pulp flow
 - - The effect of consistency on pulp flow
 - - The effect of valve diameter and style on pulp flow
 - - The effect of other factors on pulp flow
 
 - 5.3.3 Control valve sizing for pulpstock applications
 
 - 5.4 Slurries
 
 
 - 
 - 
6. Mathematical simulation of control valve behavior
- 
- 6.1 General
 - 6.2 Use of simulation
 - 6.3 Mathematical model of control valve
 - 6.4 Control valve simulation program
 - 6.5 Friction model
 - 6.6 Testing and implementing the simulation program
- - Testing position control
 - - Studies of an installed control valve
 
 
 
 - 
 - 
Appendices
- 
- A Sizing examples
 - B Conversion tables
 - C Steam
 - D Superheated steam
 - E Physical constans
 - F Vapor pressure curves
 - G Compressibility factor z
 - H Pipe tables
 - I Pressure drop in steel pipes
 - J Correction coefficient k for pulp flow
 - K Noise prediction aspects
 - L Control valve performance terminology
 - M Manifold design guidelines for valves
 - List of symbols
 - 
 
 - A Sizing examples
 
 -