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8/20/2019 Type VS1 and VS6 Vertical Turbine Pumps Wet Pit and Double Casing
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8/20/2019 Type VS1 and VS6 Vertical Turbine Pumps Wet Pit and Double Casing
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Calgary Pump Symposium 2013
Calgary Pump Symposium 2013
Marc Buckler
Product Manager - Vertical Pumps
Flowserve Corporation
Taneytown, MD, USA
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Topics
Configurations & Construction
Pump Features
Design & Analysis
Sump Design
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Configurations
&
Construction
Engineered Flexibility
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Open – Product
Lubrication
Enclosed – Oil
Lubrication
OR
Open or Enclosed
Lineshaft Construction
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Cast Discharge Head Fabricated Discharge Head
OR
Discharge Head Configurations
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Above Ground
Suction
Below Ground
Suction
Below Ground
Discharge
Above Ground
Discharge
Suction & Discharge
Configurations
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EnclosedSemi-Open
Impeller Constructions
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Positively locked to shaft
Stainless steel slotted keys preventradial movement
Stainless steel split ring keys preventaxial movement
Commonly used for extremetemperature applications
Keyed Impeller
Colleted Impeller
Provides interference fit between bowlshaft and impeller
Impeller Mounting
Configurations
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Available on enclosed impellers
and most bowls
Installed with interference fit
Roll pins positively lock the rings
in place
Wear Ring Construction
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Provides a positive seal of all
flanged joints
Located at rabbet fits on bowl
and column joints
Also included at discharge head
to suction can fit
O-Ring Construction
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Various Mechanical Seals
Single, dual, split seals
Balanced or unbalanced
Piping plan 13 minimum
Stuffing Box (Packed Box)
Low, high, extra high packed
boxes
Plan 13 required for 100 psi
or greater
Sealing Configurations
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Motors, Solid or Hollow Shaft
Variable Frequency Drives
Engines with Right Angle GearDrives
Steam Turbines
Driver Configurations
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Question:
I have an application where the
pumping liquid is municipal water.
What pump configuration do I select?
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Answer:
Consider a Wet-Pit VS1
with Product Lubrication
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VS1
Standard Features
Product Lubrication
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• Basket Strainer (Optional) Prevents unwanted debris from entering pump
Design exceeds HI standards
• Bell Bearing Provides maximum shaft support
Permanently grease lubricated for reliability
• Suction Bell Provides efficient flow into eye of first stage
impeller
• Sand Collar Prevents grit from entering into bell bearing
• Wear Rings (Optional) Renews clearances and efficiency
VTP Standard Features
Open-Product Lubrication
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Lock Collet
Provides interference fit to hold impeller to bowl shaft
Impellers - Enclosed & Semi-Open
Designed for maximum coverage of all applications Bowl Bearings
High length to diameter ratio on both sides of the
impeller to provide rigid support for the bowl shaft
Discharge Case or Bowl/Column Adapter
Hydraulic adapter ensures efficient transfer of flow tovarious column sizes
VTP Standard Features
Open-Product Lubrication
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• Open Lineshaft Construction
Allows lineshaft bearings to be lubricated by pumped
liquid
• Bearing Bracket with Rubber Lineshaft Bearings Fits integrally between column sections to maintain
alignment
Spaced to provide adequate shaft support
• Column Pipe
Available threaded as shown to minimize well casingdiameter
VTP Standard Features
Open-Product Lubrication
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Discharge Head
ASME 125# or 250# flat face flange
Provides smooth transition of pumped liquid to
discharge piping
Functions as mounting base for driver
Pre-lubrication Connection
Allows external lubrication for deep set pumps
High Pressure Stuffing Box
Allows working pressures up to 20 bar (300 psi)
Vertical Hollow Shaft Motor Extends head shaft through the motor
Provides impeller adjustment with an adjusting
nut at the top of the motor
VTP Standard Features
Open-Product Lubrication
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Question:
What if my pumping liquid contains
some abrasives?
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Answer:
Consider a Wet-Pit VS1
with Enclosed Lineshaft /
Oil Lubrication
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VTP
Standard Features
Enclosed Lineshaft
Oil Lubrication
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Tension Bearing Assembly with Oil
Tank
Holds the enclosing tube and lineshaft
bearings in alignment
Provides a chamber for the lubricant to
as it enters the enclosing tube
Oil tank provided with shut off valve,
sight feed regulator and lubrications lines
VTP Standard Features
Enclosed-Oil Lubrication
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Discharge Case with Bypass Port Allows positive flow of the lubricant
into the enclosing tube to lubricate
lineshaft bearings
VTP Standard Features
Enclosed-Oil Lubrication
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Fresh Water Injection Lubrication
Uses injection assembly with packing in lieu of tube tension assembly
Flush Line to Suction Bearing (up to 20 feet)
Provides fresh water flush to bowl bearings
Rifle Drilled Pump Shaft
Provides fresh water flush to bowl bearings
Optional Standard Features
Enclosed Lubrication
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Question:
What if my application has limitedNPSH available?
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Answer:
Consider a Double Casing VS6
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Standard Features
Non-API VS6 Pump
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Solid Shaft Motor with Thrust Bearing
Shaft extension allows motor to be coupled to pump
Includes thrust bearing to withstand the total
hydraulic thrust as well as the rotor weight
Motor Alignment Precision rabbet fit aids in the alignment of the
motor to the pump shaft
Pumps with larger motors are supplied with motor
alignment screws
OSHA Non-Spark Coupling Guards Provides safety while allowing visual inspection of
the coupling without guard removal
VPC Standard Features
Non-API Can Pump
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Fabricated Discharge Head Fabricated with ANSI 150# or 300# slip-on flanges
Functions as a mounting base for driver
0.50” NPT discharge pressure gauge, suction vent,
and drain taps
Lifting Lugs Permits economical two point lifting method of
pump during installation and maintenance
Rigid, Adjustable Flanged Coupling
Provides the proper impeller clearance adjustment
A spacer coupling allows access to the mechanical
seal without removing the motor
High Pressure Seal Chamber
Accommodates low, high and extra high packed
boxes or mechanical seal arrangements
VPC Standard Features
Non-API Can Pump
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Fabricated Suction Can
Creates optimum hydraulic conditions through the
suction flange inlet into the suction bell
Threaded or Keyed Lineshaft Couplings
Positively locks sections of lineshaft together
Open Lineshaft Construction
Allows lineshaft bearings to be lubricated by the
pumped fluid
Flanged Column Assembly
Utilizes precision rabbet fits to ensure properalignment of each section
Provides transition from bowl assembly to discharge
VPC Standard Features
Non-API Can Pump
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Bearing Retainers with Bearings
Provides shaft support in column assembly
Retainers are spaced between column sections
Pumps with larger column sizes ( >16”) are supplied
with integral retainers
Enclosed or Semi-Open Impellers
Cast to provide smooth passageways for more
efficient fluid flow
First stage impeller available with low NPSH design
Colleted or Keyed Impellers Provides method of fasting impeller to shaft with an
interference fit or a positive locking design
VPC Standard Features
Non-API Can Pump
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Question:
What if my application has limitedNPSH available and compliance to
API specifications are required?
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Answer:
Consider a DoubleCasing API VS6 Pump
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Standard Features
API VS6 Pump
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Motor Alignment Screws
Provided for use with motors over 500 pounds
Aids in the alignment of the motor to the pump
shaft
Solid Shaft Motor with Thrust Bearing Motor shaft runout of 0.001 inch total indicated
runout (TIR) contributes to the low vibration and
overall pump and motor rotor balance
Precision, Rigid Adjustable Spacer
Coupling Provides easy rotor lift adjustments for renewing
critical impeller clearances and pump efficiency
Allows seal removal without disturbing the motor
VPC Standard Features
API Can Pump
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Cartridge Mechanical Seal with Plan 13 Seal chamber is suitable for single or dual seals
Plan 13 provides continuous seal chamber venting
Seal Chamber with Jackscrews
Used to separate mating parts easily during disassembly
Weld Neck Flanges
Used for suction and discharge connections
Increase maximum allowable working pressure
Provide higher nozzle loading capabilities then threaded
or slip-on welded flanges
Flanged Vent Connection (Not Shown) Allows pump to be vented upon initial operation
Can be pressurized to purge liquid from suction can
when a suction can drain is supplied
VPC Standard Features
API Can Pump
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Lineshaft Bearing Spacing
Optimized to ensure long bearing life, low
vibration and increased mechanical
seal life
Separate Sole Plate (Optional) Allows removal of suction can without
disturbing the foundation
Internal Suction Can Drain (Optional)
Allows the suction can to be drained of
pumping liquid prior to removing the pump
Studs & Nuts
Prevent thread damage common with
capscrew removal
VPC Standard Features
API Can Pump
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One Piece Shaft
Eliminates threaded shaft couplings which cause
increased shaft runout, higher vibration and
weaker joints
Available up to 6 m (20 ft)
Open Lineshaft Construction
Keyed Impellers
Key and split-ring design positively locks the
impeller to the shaft, eliminating undesired
movement
O-Ring Construction Provides a positive seal of all flanged joints
Located at rabbet fits on bowl and column joints
Also included at discharge head to suction can fit
VPC Standard Features
API Can Pump
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Pressure Casing
Consists of suction can and discharge head
Designed to ASME standards
Able to withstand API’s specified corrosion
allowances Dynamically Balanced Impellers
Enclosed impellers balanced to ISO 1940-1
Gr G2.5
Bowl & Impeller Wear Rings
Provide a quick and easy way to renewclearances and pump efficiency
Roll pins positively lock the rings in place
Impeller wear rings are integral as standard
VPC Standard Features
API Can Pump
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Pump Intake
Design
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Hydraulic Institute StandardsSection 9.8
• Provides guidelines for
• Sump design
• Model studies
• Remedial measures
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Sump Design
• Recommended design
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Intake Model Study
• Model study recommended for:
• Single pump with flow > 40,000 gpm
• Total station flow > 100,000 gpm
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Acceptance Criteria
• No organized free surface and/or subsurface
vortices should enter the pump
• Pre-swirl limited to 5° from the axial direction
• Velocity fluctuations at the impeller less
than 10%
• Time averaged velocities within +/- 10% of
the mean velocity (Turbulence)
Model Pump
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Baseline Test
Sidewall Vortex
Floor Vortex
Surface Vortex
d l
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Remedial Measures
Modifications at entrance to pump bay Modifications in pump bay
Curtain Wall
Baffles
Grating
FilletSplitter
d l
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Remedial Measures
Vane grating baskets
i l i
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Final Testing
Flow along floor with modifications
Flow streamlines entering pump
Flow streamline along sidewall fillet
S i C D i
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Suction Can Design
• Guidelines for:
• Can length
• Suction flange location
• Flow vanes
• Can diameter
S
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Summary
• Potential problems identified and corrected using physical modeling
• The approach of using HI Standards with physical modeling provides thebest chance for success
• The approach minimizes performance problems, O&M costs, and outages
P A l i
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• Structural Analysis Includes:
Reed Critical Frequency (RCF)
– Above Ground
– Below Ground
Nozzle Load Calculations
Foundation Load Calculations
Seismic Calculations
Anchor Bolt Calculations
Lifting Lug Calculations
• RotoDynamic Analysis
Includes:
Torsional
Lateral
• Thermal Analysis
Elongation and stresses
Temperature gradient
Pump Analysis
P A l i
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Pump Analysis
Reed Critical Frequency Analysis
Why is it done? Determine the natural frequency of the combined motor & pump system
Prevent excessive vibration
P A l i
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• When is it required?
All VFD applications
To meet Hydraulic Institute and API 610 vibration limits
Motors > 260 kW (350 HP)
Design speeds ≤ 900 rpm
Design speed ≥ 3000 rpm AND > 7.5 m (25 ft) Customer request
• Inputs required
Motor Outline Drawing, Weight
Motor RCF (+/- 10%), CoG
Foundation stiffness / spring rates
Discharge head size
Discharge head type (TF, HF, etc)
Pressure rating (wall thickness, etc)
Pump Analysis
Reed Critical Frequency Analysis
Design Standards
Required Modifications
Discharge head wall thickness
Ribs/gussets
Customer foundation Possible lockout speed range
P mp Anal sis
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Calgary Pump Symposium 2013
• Operating Speed Range From a hydraulic standpoint, 30% of the operating speed can be
considered a reasonable operating speed range Greater than 30% should allow for lockout speeds
The predicted lockout speed will be defined in a +/-20% range; however, theactual lockout typically only requires a +/-5% speed range to be avoided.
Need to avoid sub-synchronous whirl (below ground instability) Typically 30%-50% of maximum design speed Critical for pumps with hard bearings
Need to avoid second critical frequency Issues typically occur on high speed pumps with TF style discharge heads
• Separation Margin Minimum of separation factor above and below the running speed range is
standard for the reed critical analysis +/- 20% separation for speeds 1200 rpm and greater +25% / -20% separation for speeds 900 rpm and less
This is not a guaranteed factor or operating speed range
Pump Analysis
Reed Critical Frequency Analysis
Design Standards
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Pump Analysis
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Pump Analysis
Reed Critical Frequency Analysis
Flexible System (No Lockout Speeds)
SpeedSpeed
Operating Speed Range
Predicted
RCF Range
Actual
Blockout
Range
Pump Analysis
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Pump Analysis
Reed Critical Frequency Analysis
Rigid System
SpeedSpeed
Operating Speed Range
Predicted
RCF Range
Actual
Blockout
Range
Pump Analysis
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• System frequency varies by: Motor manufacturer
Base Diameter
Frame Size
Weight
Center of Gravity
Reed Critical Frequency
Pump Analysis
Reed Critical Frequency Analysis
Design Factors
Pump Analysis
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• Cast Heads have limited use for VFD applications.
Cast heads always have a system natural frequency below theoperating speed (flexible system)
Better for higher RPM applications (1800-3600rpm)
Not much can be done to stiffen the system
• 100% of Operating Speed Range
Must have system natural frequency higher than the operating speed(rigid system)
Requires proper selection of the motor to even be physically possible
Pump Analysis
Reed Critical Frequency Analysis
Cases To Avoid
Pump Analysis
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• A standard RCF analysisis only on the aboveground portion
• Below ground analysisperformed only on specialcase basis
Ex. Can pump, 35’long, small pump size
Pump Analysis
Reed Critical Frequency Analysis
Special Case
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Pump Analysis
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• Inputs Required:
Pump loading
Foundation design
Motor weight
Customer imposed loads
• When is it required? If the imposed reaction forces or
moments exceed the allowable load
When nozzle position differs from
standard (PRM)
Customer request
• Required Modifications:
Add ribs to the discharge head
Thicken the discharge head riser
More difficult to obtain higher loads on
TF style heads vs HF heads.
Discharges heads with 3-piece elbow
design. Pumps in a flexible system
Nozzle Load Calculations
Pump Analysis
NOTES:
Pump Analysis
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Foundation Load Calculations
Pump Analysis
Why is it done?
Determines load imparted onfoundation.
Allows proper sizing of anchor bolts,foundation, etc.
Pump Analysis
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Foundation Load Calculations
Pump Analysis
• Inputs required
Pump and motor weight
Nozzle loads
Pumpage weight
• Optional inputs
Start-up and locked rotor torque
Unrestrained piping
Motor imbalance
Other
• Required modifications
N/A – For reference only• When is it required?
Customer request
Pump Analysis
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Seismic Calculations
Pump Analysis
• Why is it done?
System anchorage is designed to
withstand a seismic event
• Inputs required
Foundation loading (optional)
Specific design code (IBC isstandard)
Site seismic data
• Required Modifications
Anchor bolt size or quantity
Foundation (size, embedment,
strength)
• When is it required?
Customer requestExample per IBC
Analyzed in X, Y, & Z directions
Pump Analysis
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Anchor Bolt
Pump Analysis
Example per ACI
(American Concrete Institute)
• Why is it done?
System anchorage is designed towithstand operating loads
• Inputs required
Pump and motor weight
Nozzle loads
Pumpage weight
• Required Modifications
Anchor bolt size or quantity
Foundation (size, embedment,strength)
• When is it required?
Customer request
When anchor bolts are supplied byFlowserve
Pump Analysis
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Lifting Lug
Pump Analysis
• Why is it done?
To ensure the pump can be safely lifted usingthe provisions provided
• Inputs required
Pump weight
Discharge head style
Pump components (column size, etc) Intended installation method (fully assembled,
components, etc)
• Required Modifications
Lug redesign
Discharge head wall thickness
• When is it required?
If Flowserve standards are exceeded
Weight and diameter dependent
Customer request
Pump Analysis
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Torsional Analysis
Pump Analysis
• Why is it done? Reduce induced torques and stresses
Prevent fatigue
• Inputs required
Motor inertia & stiffness
• Required Modifications Shaft material change
Increase shaft size
Modify speed range
• When is it required?
Customer request
When required by API 610
Pump Analysis
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Lateral Analysis (Critical Speed)
Pump Analysis
• Why is it done?
Prevent displacement
Minimize vibration
• Inputs required
– Only pump data
• Required Modifications
Modify speed range
Change bearing material or
spacing
• When is it required?
Flowserve standard
Optional analysis method
using FEA per customer
request.
Pump Analysis
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Reed Critical Frequency vs Critical Speed
Pump Analysis
• Structural Analysis
Determines system frequency
based on combination of pump,
motor and foundation data.
Both above and below ground
frequencies exist
• Rotodynamic Analysis
Determines bearing spacing
Inputs from pump only
No impact from motor or
foundation
Reed Critical Frequency Analysis Critical Speed Analysis
Pump Analysis
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Thermal Analysis
Pump Analysis
• Why is it done?
Predict temperature gradient Determine pump growth rates and
total elongation
• Inputs required
– Ambient conditions
– Vendor temperature limits (motor,
coupling, etc)
– Cooling provisions
– Operational conditions (temperature
cycles)
• Required Modifications
– Custom design per application
• When is it required?
– Applications > 260 C (500 F)
– Customer request
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