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Thermowell Calculation Guide V1.3 (1)

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    ABB GroupMay 28, 2014 | Slide 1

    Thermowell Calculation GuideIn accordance with ASME PTC 19.3TW-2010

    Andrew Dunbabin March 2012

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    ABB GroupMay 28, 2014 | Slide 2

    Introduction

    ASME PTC 19.3 TW-2010 was written to replace ASME PTC 19.3-1974 following

    some catastrophic failures in non-steam service, these thermowells passedthe criteria laid out in 1974.

    The 2010 standard includes significant advances in the knowledge of

    thermowell behaviour. ASME PTC TW-2010 evaluates thermowell suitabilitynew and improved calculations including:

    Various thermowell designs including stepped thermowells

    Thermowell material properties

    Detailed process information

    Review of the acceptable limit for frequency ratio

    Steady-state, dynamic and pressure stress

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    Failure of a thermowell

    ABB GroupMay 28, 2014 | Slide 3

    In 1995 a thermowell failed in the secondary coolant loop of

    the Monju fast breeder reactor in Japan.The failure closed the plant for 15 years

    The thermowell was designed to ASME PTC 19.3 1974

    The failure was found to be due to the drag resonance induced

    on the thermowell by the liquid sodium coolant

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    ABB GroupMay 28, 2014 | Slide 4

    Stresses on a Thermowell

    Thermowells protect temperature sensors from direct contact with a

    process fluid. But once inserted into the process, the thermowell can

    obstruct flow around it, leading to a drop in pressure. This

    phenomenon creates low pressure vortices downstream of the

    thermowell.

    These vortices occur at one side of the

    thermowell and then the other, which is

    known as alternating vortex shedding. This

    effect can be seen in the example of a flag polerippling a flag in the wind

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    ABB GroupMay 28, 2014 | Slide 5

    Frequency Ratio

    Vortex shedding causes the

    thermowell to vibrate.If this vortex shedding rate (fs)

    matches the natural frequency

    (fnc) of the thermowell, resonance

    occurs, and dynamic bending

    stress on the thermowell greatly

    increases

    The vortex shedding rate for the drag and lift must be calculated. The in-line frequency

    (parallel to flow) is 2x the transverse frequency.

    Forces created by the fluid in the Y plane (in-line with flow) are called drag and

    forces created in the X plane (transverse to flow) are called lift

    X

    Y

    Flow Direction

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    Induced Frequencies

    Where the induced frequency meets the natural frequency of the thermowell the amplitude of

    vibration increases rapidly

    The drag frequency induced is twice that of the lift frequency induced.

    As such it meets the natural frequency of the thermowell at half the fluid velocity of the lift

    induced frequency

    The drag forces are smaller than the lift forces and under certain special conditions may not

    be significant.

    ABB GroupMay 28, 2014 | Slide 6

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    Resonance lock in

    Both lift and drag resonance tends to lock in on the

    natural frequency

    The low damping of thermowells exaggerates this effect

    ABB GroupMay 28, 2014 | Slide 7

    Frequenc

    y

    Fn

    Nominal lock-in

    range

    In line (drag) excitation Transverse (lift)

    Fluid velocity

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    Frequency Ratio Limit

    The frequency ratio (fs/ fnc) is the ratio between the vortex shedding rate and the

    installed natural frequency. In the old standard, the frequency ratio limit was setto 0.8. This was to avoid the critical resonance caused by the transverse (lift)

    forces

    The transverse

    resonance band isabove the 0.8 limit

    Following the inclusion of the in-

    line (drag) forces, a secondresonance band may also need to

    be avoided

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    Frequency Ratio Limit

    The frequency limit ratio

    is set at either 0.4 or 0.8.

    The criteria for which

    limit to use is defined in

    ASME PTC 19.3 TW-2010

    and the theory is

    simplified below. This isthe theory used in the

    calculation and should

    not be estimated

    without carrying out the

    full evaluation.

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    Thermowell stress location

    The thermowell is an unsupported beam and as such the

    stresses concentrate at the root of the stem

    ABB GroupMay 28, 2014 | Slide 10

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    Thermowells; when to perform a calculation

    A thermowell can be considered to

    be at negligible risk if the following

    criteria are met:

    Process fluid velocity is less

    than 0.64 m/s

    Wall thickness is 9.55 mm or

    more

    Unsupported length is 610 mmor less

    Root and tip diameter are 12.7

    mm or more

    Maximum allowable stress is

    69 Mpa or more

    Fatigue endurance limit is 21

    Mpa or more

    For all other conditions it is advised

    that a calculation is performed

    ABB GroupMay 28, 2014 | Slide 11

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    Thermowells; Assumptions and limits

    A number of assumptions are made in the

    standard:

    Surface finish of the thermowell will

    be 32 Ra or better

    The thermowell is solid drilled

    There is no welding on the stem of

    the thermowell (other than the

    attachment to the flange)

    That the flange rating and attachment

    are in compliance with established

    standards .

    That the thermowell is within the

    dimension limits given in the standard(table 4-1-1 and 4-2-1)

    That any corrosion or erosion is

    allowed for

    ABB GroupMay 28, 2014 | Slide 12

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    Thermowell; the pass criteria

    There are four criteria for a

    thermowell to pass evaluation to

    PTC 19.3 TW-2010

    Frequency limit: the resonance

    frequency of the thermowell shall

    be sufficiently high so that

    destructive oscillations are not

    excited by the fluid flow

    Dynamic stress limit: themaximum primary dynamic stress

    shall not exceed the allowable

    fatigue stress limit

    Static stress limit: the maximum

    steady-state stress on the

    thermowell shall not exceed the

    allowable stress, determined by theVon Mises criteria

    Hydrostatic pressure limit: the

    external pressure shall not exceed

    the pressure ratings of the

    thermowell tip, shank and flange

    All four of the criteria need to be

    evaluated and all four need to be

    passed.

    ABB GroupMay 28, 2014 | Slide 13

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    ABB GroupMay 28, 2014 | Slide 14

    Introduction to ABBs Wake FrequencyCalculation

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    ABB GroupMay 28, 2014 | Slide 15

    Thermowell Types

    STR/THREAD STR/SW STR/FLG STR/VAN STR/WELD

    TAP/THREAD TAP/SW TAP/FLG TAP/VAN TAP/WELD

    STEP/THREAD STEP/SW STEP/FLG STEP/VAN STEP/WELD

    KEY: STR = STRAIGHT; TAP = TAPERED; STEP = STEPPED

    THREAD = THREADED; SW = SOCKET WELD; FLG = FLANGED;

    VAN = VAN STONE; WELD = WELD-IN

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    ABB GroupMay 28, 2014 | Slide 16

    Dimension Details

    Note:

    Lsand bsare only applicable for step-shank thermowells

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    ABB GroupMay 28, 2014 | Slide 17

    Calculation Report

    Project and client details from the

    Front Page are shown here

    Input data from the Data Entry

    sheet is pulled through here

    including the thermowell type

    and material details

    The calculated results are shown

    in either Metric or Imperial units

    as selected on the Front Page

    Thermowell Suitability is the keyinformation

    The reason for suitability failure

    can be found in the comments

    section

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    ABB GroupMay 28, 2014 | Slide 18

    When a Calculation Fails

    If a thermowell fails the evaluation, the design can be changed in the

    following ways:

    Shorten the thermowell to reduce the unsupported length

    Increase the thickness of the thermowell (A and B)

    A velocity collar can be added to reduce the unsupported length althoughthis is not generally recommended. A velocity collar is used to provide a

    rigid support to the thermowell and will work only if there is an

    interference fit between the standoff wall and the collar.

    Care must be taken to ensure the collar meets the standoff wall at

    installation and is not affected by corrosion. If a velocity collar is theonly viable solution, it is the responsibility of the operator to ensure

    there is an interference fit between the standoff wall and the velocity

    collar.

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    ABB GroupMay 28, 2014 | Slide 19


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