Transcript Slide 1

Maintaining the Flow !
Testing of Nuclear Feedpumps
(and other important pumps)
Feedwater System Reliability Improvement Meeting
The subject today is feedwater pump testing ‘methodology’.
Testing occurs initially in the shop following fabrication but
eventually and repeatedly monitored under site conditions for many
years.
Bases for testing is to confirm degradation from design condition
(COS), usually one point but could be over a range of conditions
assuming:
 Stable and repeatable conditions process conditions.
 Equipment free of ‘defect’.
 Stable suction/NPSHA and speed conditions.
Initial pump design, shop and plant test requirements are
interconnected.
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Importance of Testing
Important pumps need to be tested based upon plant reliability and
plant safety criteria.
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Applies to CNP, HDP, SGFWP/RFWP and safety-related
pumps.
Less important for CWP.
Less still for ‘miscellaneous’ pumps.
Shop testing of all the pumps precede site acceptance testing. There
are rarely ‘typical’ test results.
‘Full assembly’ testing of complete pumpset units at full speed at
design process conditions.
There are more deviations/errors in installed pump testing due to
plant limitations..
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‘New Feedwater Pump Testing’
What is New?
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Hydraulic Institute Test Standard 14.6 – 2011.
 Larger Tolerance Bands (> 3% - 5%).
 Bilateral Tolerances (+/-).
What Hasn’t Changed?
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Addressing levels of uncertainty vs. fluctuation.
 Shop vs. system requirements.
Need to determine the onset and degree of degradation.
 Define the test point vs. COS and curve shape.
 Compare degradation vs. deviation.
Connection between shop and site testing.
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Determining Baseline Conditions
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EPU - Feedpump Curves
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Comparison Of Test Locations
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Testing Deviations
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Identifying FIE
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Flow -Induced Errors
Measurement of pump performance with installed pumps is often a
difficult process.
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Affected by the location of flow measuring types.
Line-size impact on velocity.
Type and location of upstream and downstream fittings
affecting turbulence.
Site installed test equipment cannot duplicate the accuracy and
duplication of shop test results.
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Baseline testing and data evaluation is vital.
A newly-tested pump is typically more accurate that permanently
installed instrumentation.
Speed verification is vital (design of pump/motor @ shop speeds).
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Validating Performance Margins
Monitor :
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Speeds on ASD (adjustable speed drive) pumps.
Control valve positions (% open & ∆P) with constant speed
pumps.
Correcting and validating pump performance under shop conditions
is always easier than at the site.
When to address reduction of ‘wasted’ energy, shop vs. site.
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Testing Guidelines are Common for All Pumps
Testing any pump for Nuclear Service should be based upon the
same bases:
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Confirming mechanical assembly.
Demonstrating hydraulic performance.
Verifying condition following initial operation.
The Shop Test Program is the last opportunity to:
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Confirm compliance to specification requirements.
Permit changes prior to shipment and installation.
Anticipate start-up and commissioning issues.
Eliminate unknowns about the equipment before being exposed to
installation and site conditions:
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OEM compliance.
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Test-Or-Not-To-Test
Range of Testing:
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Accepting data from similar or earlier testing.
Non-witnessed testing of job hardware.
Witnessed testing of all job hardware.
Costs of Testing:
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Based upon the ‘delay’ and ‘cost’ of not performing tests.
Missing documentation for site use.
Shop vs. Site Testing.
Evaluation of Test data:
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Conducting adjustments.
Pumps normally in operation at/near the COS are less likely to
deviate or degrade. Test data is also likely repeatable.
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Site Testing of Existing Units
Establishing priority of Test Parameters.
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Capacity
 Type and location of instrument.
 Correction factors.
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Developed Pressure (TDH)
 Type and location of instrument.
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Power
 Amps, kW.
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Speed
Temperature
Assuring fidelity/reproducibility.
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Uncertainty and fluctuations, shop vs. site.
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Pump & Process
Allowances, Margins & Tolerances
Allowance are the values added to pump capacity and TDH due to
initial sizing uncertainty.
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Can be defined.
Margins are the values added to pump capacity and TDH due to
degradation.
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Can be defined.
Tolerances are values of either capacity or TDH provided by industry
standards due to degradation.
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Cannot be defined or guaranteed.
Pumps can be made smaller, systems can’t be.
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Degradation of Pump Performance
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Testing Standards
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Project Test Criteria
Define:
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Test Temperature.
Test Speed.
Time of Test.
Scope of Equipment:
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Job vs. Shop Hardware.
Instrumentation.
Transient Requirements:
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Range of Upset Conditions.
PTI:
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Acceptance Criteria.
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History of Hydraulic Institute Standards
The Institute came into being in 1917.
1st Edition in 1921-Trade Standards in the Pump Industry.
3rd Edition in 1925- Standards of the Hydraulic Society.
7th Edition in 1937-Standards of the Hydraulic Institute.
9th Edition in 1951- Copyrighted.
10th Edition in 1964
13th Edition in 1975
14th Edition in 1983
HI 1.6/2.6 in 2000
HI 14.6 in 2011
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Early HI Standards
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Previous Test Standards
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Current Tolerances - API
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Current Tolerances
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Current HI Tolerances
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Impact of New HI Shop Test Tolerances
Design Engineering
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Defining minimum performance for pumps in nuclear service
will require adherence to unilateral bases.
Positive tolerances will affect driver required rating and
discharge piping ratings.
Shop Testing
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Acceptance criteria will require redefinition.
Initial Site Baseline Testing
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Once the values are accepted, there should be no changes.
Deviations
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Similar to present.
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Horizontal Pump Shop Test Setup
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Vertical Pump Shop Test Setup
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‘Edge Engineering’
The issue of precision or accuracy should be addressed to
aid in understanding the impact on pump, motor, piping
and valve sizing, system efficiency and reliability.
Avoid the tendency to ‘over-specify pumps’ and fluid systems.
Avoid the tendency to design or specify at or near the MOP
(minimum operating or design point).
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