machinery reliability-heinz bloch

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  • 8/22/2019 Machinery Reliability-Heinz Bloch

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    Second levelThird level

    Fourth level

    Fifth level

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    (1) Start with cost estimates and budgets

    Why Best-of-Class companies budget towards mostrel iable machinery and not towards their least

    expensive initial outlay options

    They start by having only the most capablevendors on their bidders (vendors) lists

    Their budgets for machinery include 5% of thecost of this machinery to perform MQA

    Have a contingency budget to pay forupgrades or things overlooked in the specs

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    of Webinar 9, (6/20/ 2013)

    Several recent texts

    include descriptionsof MQA

    The smartest budgets

    include 5% or more forperforming MachineryQuality Assessment(MQA);often a one-year payback

    Next slide: Pre-invest!

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    MQA Example: Nozzle size increases for

    D$ ~ 4 to 6 k--low gas velocity The benefits of soundly

    done pre-investment in

    contingency upgrades(as successfully done by

    Dakota Gasification;

    briefly discuss example)

    Examples of large gearbox and compressor

    nozzle sizing upgrades

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    (2) Decisions with Reliability Impact for

    Reciprocating Compressors: Or,

    small matters add up

    Suction valves were not automatically opened whenpower was interrupted--bearing bores then contact their

    pins or journals Grout support under compressor frame had been allowed

    to degrade over time--generally no issue, but crankshaftis then slightly curved

    Bearing bores then experienced edge loading With no power to compressor driver, there was no lube

    oil supply to bearings, hence no cooling; some melting

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    Edge loading means reduced areas of

    contact;pressure = force per unit area (psi) Crank pin

    Crosshead pin

    Main journal______________

    The loads (arrows) actonly on a smallarea, psi. Now the

    pressure becomestoo high; no oilfilm; high temperat.,softening of alloy(babbitt) takes

    place; bearing fails

    1

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    Edge-loading of bowed crankshaft wrecks a bearing Theowner plant allowed four deviations to become new normal: curvature

    of crankshaft, high force on bearing, no cooling oil

    2

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    Real pros always look at the entire system: Example ofKing Tool

    conventional horizontal filter-coalescer vs. self-cleaning models

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    Why reciprocating compressor moisture

    disengagement strategies are often flawed

    Example of a reciprocating machine having an

    inlet capacity of 1000 volume units (cubic feet per

    minute, or cubic meters per hour)

    Volume = Area times velocity [cfm=sq ft x ft/min]

    Volume = Area times velocity [m^3/hr = m^2 x m/hr]

    1000=10 x 100----- small area x high velocity ($)

    1000=100 x 10----- large area x low velocity ($$$)

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    of Webinar 9, (6/20/ 2013)

    (3)The merits of superior machinery storagepreservation (cost justification is not difficult)

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    Cost justification for OM storage protection

    System cost: ~$300,000 Without oil mist outdoor storage protection, must

    dismantle and inspect/clean 120 process pumps($10,000 each) = $1,200,000 and electricmotors ($3,000 ea) = $ 360,000

    Total cost avoidance is $1,560,000-$300,000 =

    $1,260,000. Operating cost of the OM storagesetup is offset by credits for future use as unit-wide oil mist lubrication system

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    (4+5) Examples of knowledge requirements:

    Lube and bearingenvironment (synonymous) Specify the correct lube viscosity: Enlist vendors

    Select film strength formulations, know about

    viscosity improvers and other additives

    What does this imply? Mineral oils versus

    synthesized hydrocarbons---synthetics

    When are the latter justified? For an experts

    answer, view the next slide

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    Liquids always tend to wash off lubricants

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    (4) Where only synthetics will do:

    (1) In bearings operating at (or developing) hightemperature, synthetics slow down oxidation and filmthickness degradation

    (2) When increased vibration alerts you to an incipient

    defect, synthetics fill micro-cracks(3) After deleting cooling water (which best-of-class

    companies have done for the past 40 years), synthetics

    greatly expand range of allowable operating temps

    (4) In gear units of all sizes (except if common w/comp.(5) In reciprocating process gas compressor cylinders

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    (5) Superior bearings

    are available

    Double-row bearingswith two inner rings (top)

    Ceramic bearings best inwet screw compressors

    API 610 is only a guide

    PumPacbrgs preventsliding and heat-related

    bearing degradation Buy only from mfrs that

    can provide applicationengineering expertise

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    Notice the REs expanding horizons

    Its not machine fail; must be machines fault

    Its not fix only what is broken. Underlyingcauses must be found and addressed

    Always an early warning; API-stds are only min.

    Rarely only one deviation; several deviationswill combine and cause a failure

    When someone says weve always done it thatway---they may have always done it wrong

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    (5a)--Sliding pipe support details

    Note that 2 polymer(Teflon) plates areneeded

    Consider whathappens if money issaved using onlya single poly plate:Rust forms on thesteel surfaces andnothing moves!

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    (5b) Effect of pulling pipe into place: Distress

    Bearing is designedto make contourcontact

    Pipes pulled into

    place to matchcasing nozzles willcause casings todistort

    Bearings are point-loaded and the oilfilm is no longeradequate

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    (6) Rotary valve stuffing boxes and pump bearing housings

    need protection against intrusion of debris

    Remember: Modernbearing housing seals

    for pumps are designed

    as rotating labyrinths

    Advanced seals do not

    have an O-ring that

    contacts a sharp edge or

    O-ring groove Unless specified, youll

    always get the cheapest

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    (7) Spare parts management: New 3D

    printer methods make patterns for

    castings; contour measuring machines

    Getting primed for implementing modern 3D PrinterMethods of pattern production for certain spare parts(buying very few spare parts). A good project decision!

    Thus: Linking up with a knowledgeable provider will beadvantageous to the owner-purchaser or design firm, andalso for existing plants that need to consolidate spares.

    Contour-measuring allows superb reverse-engineering

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    (8) Old traditional oil mist lubrication: Some OMescaped before it had an opportunity to reach the bearings

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    (8) Oil mist applied per API-610 (2009)

    allows flow entirely through bearings

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    (9) Grouting and hold-down bolt issues

    avoided with epoxy-filled base

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    Anchor bolt, on left, must have a free length (non-

    encased, allowed to stretch) equal to 10 diameters

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    Typical as-installed baseplate cost

    comparison:Conventional vs. Pre-Filled

    $ 6,259

    $ 4,194

    $ 2,065

    IMMEDIATE

    PAYBACK!

    Equipment Installation: Baseplates

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    (10) Seal-related upgrade opportunities

    Enlist an expert to optimize your mechanical sealSpecifications and buy seals from 2 or 3 suppliers

    Make a competent vendor your failure reduction

    partner, not merely your supplier of inexpensivemechanical seals

    Plan to upgrade to dual seals and closed-loopwater management systems wherever possible. Itis sure to decrease repair frequency and will savemuch money

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    Sometimes it is advantageous to interrupt the flow

    around the seal faces; one could use Vortex Breakers

    Option 1: Changing the seal environment

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    Option 2: Change to dual sealsbut beware

    Some seal designs do not optimize the exchange of fluid.

    Parallel slots move little, if any, of the barrier fluid

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    Change the environment with a superior dual

    seal; add value with better pumping rings

    Some dual seal designs truly optimize the exchange of fluid.

    This one uses a wide-clearance tapered pumping ring

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    Mechanical seal with internal flow baffle(shown here with a flow guide, but w/o tapered pumping ring)

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    Bi-directional internal flow device (Buffer Fluid

    Impeller) incorporated in mechanical seal

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    Bi-directional barrier fluid pumping device---a

    highly effective Tapered Barrier Fluid ImpellerTHREE ADVANTAGES

    Efficient No cost impact

    Moves more

    cooling fluid to

    critical regionof mechanical seal

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    API 682 / ISO 21409Awareness of

    Standards and deviations from same

    All seals should operate continuously for

    25,000 hours without need for replacement

    The minimum performance requirements and

    permitted leakage detailed in Section

    10.3.1.4.1 of the standard specifies an average

    leakage rate of less than 5.6 grams / hour perset of seal faces

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    Air Testing Protocol outlined in Section10.3.4.2 of the standard

    Each sealing section shall be independently

    pressurized with clean air to a gauge pressure of0.17 Mpa (1.7 bar) ( 25 psi). The volume of eachtest setup shall be a maximum of 28 liters (1 cu. ft.)

    Isolate the test setup from pressurizing source and

    maintain the pressure for at least 5 minutes The maximum pressure drop during the test shall be

    0.014 Mpa (0.14 bar, or 2 psi)*

    API 682 / ISO 21409

    T t

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    of Webinar 9, (6/20/ 2013)

    Test 125 L Vessel plus

    1.5 approximate air volumein rig providing total of

    26.5 liters, or95% of the

    maximum air volume per

    10.3.4.2 pressure tested.Result: Pass

    Tests

    Test 226.5 Liter air

    volume fitted with a NPT plug with a 0.008

    hold drilled through the

    center. Pressure tested.

    Result: Pass

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    of Webinar 9, (6/20/ 2013)

    Test 326.5 L Air volume

    connected to mechanicalseal fitted with the NPT

    plug with 0.008 hole.

    Pressure tested

    Result: Pass

    Tests

    Test 41.5 L Air Volume

    connected to Mechanical

    seal fitted with the NPTplug with 0.008 hole.

    Pressure tested

    Result: Fail

    T t 6 7 & 8 O ifi d f th l d tt h d

    F il

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    of Webinar 9, (6/20/ 2013)

    Test 6, 7 & 8 Orifice removed from the seal and attached

    to nitrogen pressurized water vessel to measure the leakage

    at different pressures against the 5.6 grams /hour (g/h)

    specification in API 682 / ISO 21409

    1,500 g / h270 x allowable test

    Fail

    3,000 g / h

    540 x allowable test

    Fail

    7,500 g / h

    1,300 x allowable test

    Fail

    of Webinar 9, (6/20/ 2013)

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    Summary

    1. Decision to deal only with the best vendors;MQA and pre-investment in risk reduction

    2. Decisions with impact on reliability of

    reciprocating compressors3. Oil mist for superior storage preservation

    4. Use synthetics where only synthetics will do

    5. Bearings for highest reliability: from vendorswith application engineering know-how!

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    Summary

    6. The right bearing protection is part of built-inreliability. Specify it in the project

    7. Fewer spare parts: Use 3D print pattern library

    8. Plant-wide oil mist includes electric motors!Rapid payback is possible (SKF/Colfax Ind., etc)

    9. Pre-grouted epoxy-filled base plates make

    economic sense and give long trouble-free life10. Better and smarter mechanical seal options exist

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    QUESTIONS?