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Control Valves and the Control Loop

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    Process Instrumentation,

    part 2:Control Loops and the ControlValve

    CM4120Unit Operations Lab

    January 2010

    1

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    Outline What is a Control Loop?

    A look at Regulatory Control Valves PID Controllers and terminology

    Instrument Connections to a Distributed

    Control System

    2

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    Typical Control Loop

    3

    All elements of a loop have same loop number

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    Elements of Control Loop

    Input side:

    TE Element to measuretempRTD vs. T/C

    TT Transmitter sends signal

    Dashed line - signal

    transmission line

    4

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    Elements of Control Loop

    Controller: TIC Temperature Indicating Controller Shared Display, Analog signal

    5

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    Elements of Control LoopOutput side:

    TV Valve to regulatesteam flow

    TY Transducer converts

    electric signal topneumatic

    Solid line w/ dashes ispneumatic signal line

    F.C. is Fail position

    6

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    Regulatory Control Valve

    7

    Trim setdesirable to have

    flow linearly

    proportional to

    valve position forgood control

    Actuator

    (F.O. or F.C.?)

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    Valve Trim I nherent Characteristics

    8

    Quick Openingsafety by-pass type

    Large flow response when valve starts opening ismore important than linear response

    Equal Percentage~ 80% of all control valvesprovides linear response to valve position

    Linearused when majority of system pressure drop isdue to valve position

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    Valve Trim Sizing: Flow

    Coefficient vs. Valve Position

    0

    0.5

    1

    0 20 40 60 80 100Stem Position (% Open)

    f(x)

    =%

    QOLinear

    9

    By definition:for Cv = 1,

    1 gpm flow w/

    1 psi pressure dropacross valve

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    Valve Selection Example

    C.W.

    FT

    10

    Control flow of reflux to distillation column

    Determine pressure drop:

    @ design flow

    @ expected min/max flow

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    System Response based on

    Pump/ Piping System

    11

    Design Range of flow is 100 to 200 gpm:

    Increase in valveopening lessP

    across valve, but w/

    increased line lossesand decreased total

    available head from

    pump 0

    5

    10

    15

    20

    25

    0 50 100 150 200Flow Rate (GPM)

    PressureD

    rop(psi)

    Line Losses

    Pump Head

    Valve P

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    Installed Characteristic

    12

    Size the valve trim, then select valve characteristic

    w/ the most linear response:

    use Equal Percent Characteristic valve to achieve

    a linearInstalled Characteristic

    0

    50

    100

    150

    200

    0 20 40 60 80 100Stem Position (% Open)

    InstalledFlowRate

    (GPM

    )

    Linear Valve

    =% Valve

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    PID Controllers

    13

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    Review of Controller Terminology

    Process Variable ( PV) = Measured variable of

    interest, in EU

    Setpoint ( SP) = Desired value of the PV, in EU

    Output (OP) = Controller output, 0-100%

    Error = Difference between Setpoint and PV

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    Relating this to our Control Loop:

    15

    Process Variable

    Output

    Setpoint

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    Controller TerminologyPI D control Dynamic equation that is used to match the

    controllers response to a measureddisturbance.

    Goal is to minimize disturbance and return to

    setpoint Equation is tuned to match process

    response using up to 3 tuning constants

    16

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    Controller TerminologyTuning Constants:Proportional term Adjusts outputproportional to the error, Gain

    I ntegral term Added to output based on

    error existing over time, Reset

    Derivative term Additional adjustment to

    output based on rate of change of error, Rate

    17

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    Evolution of Controllers1930s Pneumatic Controllers air pressure w/ flappers, bellows, and valves

    adjust valve position based on measured

    process variable for P, PI, later PID control1950s Electronic Controllers transistors, resistors, and capacitors for P, PI,

    PID control capable of remote installation1960s Mainframe Computer Control Refineries were typical users

    Alarming capability and supervisory control Single point of failure, no user-friendly

    graphical interface

    18

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    Evolution of Controllers

    Late 1970s Distributed Control Systems(DCS)

    Networked computers distributed thru plant Pre-configured controllers Data archival capabilities Included an operator console Hardware is proprietaryLate 1990s DSCs built on commodity

    hardware platforms Better scalability Affordable Interactive graphical interface

    19

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    Emersons DeltaV System current state of the Technology

    20

    PID control

    Discrete logic control

    Signal conversions

    AlarmingFuzzy control, etc.

    are continuouslyexecutedby the MD controller

    http://www.easydeltav.com/index.asp
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    Wiring Systems ConnectTransmitters

    to DCS at the Instrument End:

    21

    Wiring to fieldjunction cabinet

    RTD or T/C head

    Temperature

    transmitters

    Wiring from

    transmitter to temp

    measuring element

    Level transmitter

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    Wiring Systems ConnectTransmitters

    to DCS at a Marshalling Cabinet:

    22

    Single pairs

    from field

    devices

    8 pr. Cables to

    controller

    cabinet

    8-pr. cables run from Field Junction Box (Marshalling

    Cabinet) to Distributed Control System

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    Wiring Systems ConnectTransmitters

    to DCS in the Controller Cabinet:

    23

    DeltaV MD controller

    8 pr. cables from

    field junction cabinet

    Power-limiting

    Zener barriers

    I/O cards

    2nd I/O chassis w/4-20

    mA Output cards

    http://www.easydeltav.com/index.asp
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    Wiring Systems Connect DCS to

    Transducers at Marshalling Cabinet:

    24

    Wire prs. to transducers

    Current to pneumatic

    transducers

    Air lines to

    control valves

    8-pr. cable from

    controller cabinet

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    Regulatory Control Valve

    25

    Air line from I/P transducer

    Actuator w/ positioner

    Control valve

    Block valves

    Bypass valve

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    Output Signals from Control System

    to Control Solenoids

    26

    8-pr. cable from

    controller cabinetSolenoids for 2-position

    air-actuated ball valves

    Air lines to

    ball valves

    Wire prs. to solenoids

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    Installed Field Devices:

    Ball Valve w/ Actuator

    27

    Air line from

    solenoid

    Actuator

    Ball valve body

    Process line

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    DeltaV &Foundation Fieldbus

    28

    (4) mass flows, (4) densities,

    and (4) RTD temps

    (3) 8-multiplexed RTD temps(2) temp-only transmitters

    (1) wire

    http://plantweb.emersonprocess.com/Home/index.asphttp://www.easydeltav.com/index.asp
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    ReferencesMiller, Richard W., Flow Measurement

    Engineering Handbook, 3rd Ed., McGraw-Hill,

    New York, 1996.Riggs, James B., Chemical Process Control, 2nd

    Ed., Ferret Publishing, Lubbock, TX, 2001.Taylor Instrument Division, The Measurement of

    Process Variables, no date.www.emersonprocess.com/rosemount/,

    Rosemount, Inc., Oct. 2006.

    www.emersonprocess.com/micromotion/, MicroMotion, Inc., Oct. 2006.

    www.ametekusg.com/, Ametek, Inc. Oct. 2006.

    29

    http://www.emersonprocess.com/rosemount/http://www.emersonprocess.com/micromotion/http://www.ametekusg.com/http://www.ametekusg.com/http://www.emersonprocess.com/micromotion/http://www.emersonprocess.com/rosemount/

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