Mark 3 Asme Pumps.pdf

FLOWSERVE CORPORATION

Mark 3 ANSI Pumps Product Training Program

April 2017

Table of Contents •

Pump Description

•

Nomenclature

•

Operating Parameters

•

Range Chart

•

Standard materials of construction

•

Feature/Function/Benefit

•

Pump selection

•

Markets Served and typical application

•

Main customers

•

Competition

•

Design centers and Manufacturing locations Page 2

Mark 3 Product Family

Lo-Flo

Sealmatic

Standard

Vertical Inline Guardian Mag-Drive

Unitized Self-Primer

Recessed Impeller

Page 3

Pump Description  End Suction Overhung  Radially split  Single stage  Wide flow and head range  200+ hydraulics  High operation efficiency  Low NPSH requirement  Easy maintenance

Page 4

Pump Description

ASME B73.1M & H.I.1.1-1.5 Standards    

Horizontal End Suction Foot Mounted Single Stage

   

Centerline Discharge 150 / 300 lb Flanges Back-pull-out Dimensions set by standard

Page 5

Pump Description

ASME B73.1M Pumps (continued)  Designed for corrosives  External impeller adjustment  Limit exposed threads and crevices  Mechanical seal protection  Bearing isolation  Wide range of materials

Page 6

Flowserve ANSI History    

Mark 2 Mark 3 Mark 3A Mark 3 ANSI 3A

Page 7

Mark 2 Power End •

Created in 1962

•

Bearing Cap Fixed

•

Cork or EPR gasket

•

Impeller Setting via shims between bearing snap ring and housing

•

No Sight glass oil level set by Trico Oiler

•

Oil Flinger required because oil level not visually set

•

Bottom Vented Breather

•

Bearing span setting required no I.B. Bearing shaft shoulder

•

Standard Lip Seals Page 8

Mark 3 Power End •

Impeller adjustment via micrometer threaded bearing carrier

•

Standard Lip seals

•

Oil level set visually with ½” sight glass and Trico Oiler

•

Oil Flinger not required

•

Top Vented Breather

•

GP2 & 3 shafts and power end interchangeable with MK2

•

Shafts machined with shoulders for bearing span location

•

Gp1 shafts 1 3/8” through seal chamber

•

Larger oil sump

•

MK3 1J Power End created for MK2 replacement on GP1 using 1.125”

Page 9

Mark 3A Power End •

Threaded carrier changed to use small dia. O-rings

•

Threaded carrier uses cast lugs at hold down bolts for use of wrench to adjust

•

Removed lugs on O.D. of carrier removing need for spanner wrench

•

Larger Oil return slots provide in bearing Carrier

•

Bearing housing designed for larger 1” bulls eye sight glass

•

Oil sump increased over Mark 3

•

Standard lip seals

•

Trico Oiler combination Watchdog style standard Page 10

Mark 3 ANSI 3A Power End •

Same Power end as MK3A with added features

•

Labyrinth Bearing Isolator – Flowserve Bearing Gard – Inpro VBXX-D Oil Seals

•

Magnetic Drain Plug

•

Plugged bearing housing no breather

•

No Trico Oiler

•

Lifetime Power end Warranty Page 11

Nomenclature: Mark 3 Pump Size Code • Example: – 2 K 3 x 2() - 10A / 8.25 RV        

2: Group2 K: Mark III 3: 3” suction 2: 2” discharge 10: Max. impeller dia. 8.25: Imp. trim RV: Reverse vane imp. HD: Heavy Duty Shaft

() =  _: Standard  M: Sealmatic  R: Recessed impeller  US: Unitized self-priming  V: Vertical in-line  LF: Lo-Flo  L: Non-metallic  H: High Silicon Iron  T: PTFE lined  E: Durcon  S: Old style self-priming Page 12

Mark 3 Nameplate Information

• • • • • • • •

Standard Nameplate Serial No. Equipment No. Purchase Order No. Model Size MDP Material Date

• • • • •

Secondary Nameplate Serial No. Capacity TDH RPM Impeller dia.

Page 13

Nomenclature: Pump Group 1 Pum p Size

A N SI designation

1.5x1LF-4

---

1.5 x 1-62

AA

3 x 1.5 – 62

AB

3 x 2 – 62

---

1.5 x 1 – 82

AA

1.5x1LF-8

---

3 x 1.5 – 82

---

Page 14

Nomenclature: Pump Group 2 Pump Size ANSI Desig

Pump Size ANSI Desig

Pump Size

ANSI Desig

3x2-82

A60

3x2-10A

3x1.5LF-13

---

4x3-82

A70

4x3-10

A70

3x2-13

A30

2x1-10A

A05

4x3-10H

A40A

4x3-13

A40

2x1LF-10

---

6x4-10

A80A

4x3-13HH

A40

6x4-10H

A80

6x4-13A

A80

3x1.5-13

A20

3x1.5-10A A50

A60

Page 15

Nomenclature: Pump Group 3 Pump Size ANSI desig

Pump Size ANSI desig

8x6-14A

A90

8x6-16A

A110

10x8-14

A100

10X8-16

A110

6x4-16

----

10X8-16H A120 10X8-17

A120 Page 16

Operating Parameters 

Flow: 0.3 to 2,270 m3/h (2 to 10,000 gpm)



Head: up to 300 m (985 ft)



Power: up to 373 kW ( 500 hp)

 Pressures: up to 31 bars (450 psi)  Temperatures: up to 370°C (700°F)  Suction nozzle sizes: 38 mm (1.5 in) to 305 mm (12 in)

Page 17

Range chart MK3 – max impeller – max speed 60 Hz

Page 18

Range Chart In-Line – max impeller – max speed 60 Hz

Page 19

MK3 Standard Materials Pump

Material Specification (PROS)

Component

DCI

D/C

D4

CD4MCuN

D20

DC3

TI

Casing

Nodular Cast Iron (Ductile Iron)

Nodular Cast Iron (Ductile Iron)

316 SS

CD4MCuN

Durimet 20

Chlorimet 3

Titanium

Impeller

Nodular Cast Iron (Ductile Iron)

CD4MCuN

316 SS

CD4MCuN

Durimet 20

Chlorimet 3

Titanium

Rear Cover - Seal Chamber

Nodular Cast Iron (Ductile Iron)

Nodular Cast Iron (Ductile Iron)

316 SS

CD4MCuN

Durimet 20

Chlorimet 3

Titanium

Shaft

Steel

Steel

ZH

ZC20

ZC20

Stainless w/ DC3 Sleeve

Stainless w/Ti Sleeve

Seal

Mechanical Seal: Balanced/unbalanced/catridge/split or Gland Packing

Bearing HousingAdapter

Cast iron - Ductile Iron (SS is optional)

Bearings

Antifriction grease or oil bath lubricated (optional oil mist)

Application

standard application

Page 20

MK3 Standard Material

Page 21

Mark 3 Features ANSI 3A

Reverse Vane

SealSentry

Features Designed to Optimize the Seal Enviroment Page 22

True Back Pullout Design

Page 23

Features

Causes of ANSI Pump Failures 80 70 60 50 40 30 20 10 0 Shaft seal

Bearings

Other Page 24

Reverse Vane Impeller • • • • • •

Low NPSHR Low, unidirectional thrust loads Hydraulic balance holes Wear Surface is the Rear Cover, Not Casing Low, predictable seal chamber pressure Running clearance set to rear cover, not casing – Impeller and seal setting performed in the repair shop, not under adverse field conditions. True Back Pullout Design.

Page 25

Front Vane Open Impeller • Optional • Clearance adjusted between impeller and case (field adjustment) • Recommended where there are fibrous, stringy materials in the liquid Page 26

Front Vane Open Impeller

Page 27

Reverse Vane Impeller  One setting to maintain: • • • •

Performance Efficiency Thrust Seal chamber pressure

Page 28

Reverse Vane Impeller Seal Ring wear has less than 1.5% effect on performance TDH vs. Radial Clearance 2K4X3-10 at BEP +/- 1.5% 400

TDH

390 380 370 360 350 0.03

0.05

0.07

0.09

0.11

0.13

Radial Clearance

Page 29

MK3 Inducer •

Sizes Available – – – – –

•

Guidelines – –

•

2K6x4-10 2 & 4 Pole 50/60Hz 2K6x4-10H 2 pole 50/60HZ 2K6x4-13 – 2 & 4 Pole 50/60 Hz 3K8x6-16 – 4 & 6 Pole 50/60 Hz 3K10x8-16H – 4 & 6 Pole 50/60 Hz

Average 30-40% reduction from PROS/Flowselex NPSHa values Flow rates 90% of BEP and lower

Contact Distribution Support Group for Application & Pricing Requests

Competitive Advantage – Don’t Oversize

Page 30

Rear Cover / Seal Chamber Designs

Page 31

FML SealSentry™ Chambers  Flow Modified Large Bore (FML)  Turns centrifugal flow caused by the seal into axial flow by the ribs along the chamber

 Handle up to 60% solids  Can be field machined to restore wear surface  Vast Sealing Options  Single, Double, Gas, Split

 Self-flushing, self-venting, selfdraining  Can eliminate expensive piping plans

 Good solids handling capability  Extends the overall life of the mechanical seal

Page 32

™

FML SealSentry Chambers  Flowserve Test of FML Design  50% Titanium Dioxide Slurry  Heavy Erosion on Cover Surface  Flow Modifiers remain intact  Mode of Failure: Pressure Containment  Dime size blowout on cover surface  Seal Inspection Performed  Little signs of wear  No Leakage during testing

Page 33

Features: FMS

 Flow modified  Small gland and gasket circles  Self-flushing, selfventing, self-draining

Page 34

Features: CBL  Cylindrical bore  Large gland bolt and gasket circles  Recommended when seal chamber isolation is desirable

Page 35

Features: CBS

 Cylindrical bore  Small gland bolt and gasket circles  Recommended when seal chamber isolation is desirable

Page 36

Jacketed Seal Chamber (standard bore - CBS)

Page 37

Jacketed Seal Chamber (FM chamber)

Page 38

Mark 3A Power End Standard Features  Bearing seals  Standard Lip seals  Optional Isolators  Deep, Groove Conrad Type Ball Bearings  Top vented baffled breather  Trico constant level oiler  1” Oil Sight glass  Rigid adjustable foot piece  Shaft shoulder for both bearings  Oil return slots, both bearings  Lifting Eye  Side mounted oil drain plug

Page 39

Features

Micrometer Impeller Adjustment Very accurate Very easy Calibrated bearing carrier Maintains near perfect parallelism  Threads protected  Each notch equals  0.10mm (0.004”)    

Page 40

Features

Mark 3A Power End Options  Labyrinth seals  Magnetic seals  Duplex Angular Contact Thrust Bearing  Oil mist option  Magnetic drain plug  Bearing housing oil cooler  Shaft options

Page 41

Features

Mark 3 Power End ANSI 3A Design  Bearing isolators (Flowserve Bearing Gard or Inpro VBXX-D)  Magnetic drain plug  Clean room assembly  Vent and oiler holes plugged  Lifetime Power End warranty  Bearings are normal wear item

 Extended oil change intervals  Mineral Oil 18 mo.  Synthetic 36 mo. Page 42

Features

Inpro VBXX-D Bearing Isolator

Page 43

Features

Shaft Options  Solid  Hook Sleeve  Composite  Friction-Welded

Page 44

MK3 Heavy Duty Power End • • • • • • • •

Option: All Mark 3 Group 3 Pumps Pumps can be Field Converted 550 BHp rating vs 325 BHp of existing Mark 3 design Duplex Angular Contact Bearings Large Roller Radial Bearing Minimum 5 year L10 Bearing Life Cartridge Seals Only Heavy Duty 3” Steel and 2205 Duplex Solid Shaft –

• • •

Improved L3/D4

Shaft Coupling End dia. Matches Current GP3 Belt-Drive Capable Offers 3K10x8-16H Full Impeller Diameter Range @ 1800 RPM Page 45

Features

Mark 3 Casing •

Integral Foot mount design

•

Centerline discharge

•

150# flanges (300# optional)

•

Flat Face Flange (RF optional)

•

Single volute on most sizes – Double volute on larger pumps

•

Drain, Suction, Discharge taps available Page 46

Features

Mark 3A Bearing Housing Adapter •

Mates wet end to housing

•

Allows parts interchangeability reduced inventory

•

Metal-to-metal fit to housing and to rear cover.

•

Standard is DCI (ductile iron), alloy is available

•

Integral on Group 1 pumps. Page 47

Jacketed Casings • Provides temperature control • Integral (as shown) • Bolt-on jackets available

Page 48

Features

Centerline Mounting Casings •

Reduces loads caused by thermal expansion

•

Cradle Design Std.

•

Optional - Jacketed feet allow temperature control

Page 49

High Temperature Applications • Temperatures greater than 300°F (149°C)    

Grafoil impeller and casing gaskets ZH shaft Oil Lubrication ANSI 3A Powerend

• Temperatures greater than 350°F (177°C)  C-face motor adapter  Jacketed Rear Cover. Preferably CBL with throat bushing.  Finned Oil Cooler

• Temperatures greater than 500°F (260°C)  Centerline mounted Casing  316ss Bearing Housing Adapters

Page 50

Features

C Flange Adapter  Holds alignment even with changes in temp. & pipe loads  Eliminates foot mounting of the motor

Page 51

Features

C-Plus Precision Alignment System

 For alignment within 0.002 in (0.05 mm)

Page 52

Features

Baseplate Options

Page 53

Type A Standard    

Typically in stock Multi-Drilled for several NEMA size motors Primer suitable for epoxy grout Dimensions to ANSI B73.1

Page 54

Type B Polycrete      

Low installed cost Superior vibration dampening Excellent corrosion resistance – Material Options Available Designed to be flat with excellent rigidity Catch basins and grout holes Inserts give infinite configuration possibilities

Page 55

Type C Stilt Base  Multiple Stilt arrangements available  Multi-Drilled for several NEMA size motors  Dimensions to ANSI B73.1

Page 56

Type D Heavy Duty Base  End Caps, Machine Pads, Full Drip Rim Options  Multi-Drilled for several NEMA size motors  Dimensions to ANSI B73.1

Page 57

Type E PIP Baseplate “Ten Point” Heavy Duty Design

Meets the intent of API 610 and Fully complies with PIP RESP002

0.002”/ft mach coplanar pads Cross Member Support Continuous seam weld Tapped Leveling Holes Integral Lifting Lugs Integral Grout Anchors ½” Vent Holes 4” Grout Holes Integral Sloped Drip Rim with Drain Port  Post-Type Motor Adjusters         

Page 58

Baseplate Considerations • Type A – Bent Form Baseplate  No Welding on Group 1 and 2 size bases.  Drip Rim Option – non-sloping on pump end only  303ss Catch Basin is a good option. Less Money.

• Type B  Non-Metallic for Foundation or Stilt Mounting  Consider when corrosive environment or when request is for SS baseplate

• Type C  Consider in High Temperature Applications above 300°F (149°C)  Consider when Temperature range is greater than 100°F (∆38°C)

• Type D  Adds extra bracing, lifting lugs, and leveling holes over Type A  Offers End Caps, Machine Pads, Full Drip Rim Options

• Type E  API style baseplate Page 59

Features

Polyshield •

Traditional baseplate systems do not offer a full solution to our customers.

Picture shows great pump and baseplate, but just look at the issue below (concrete pad). How does a customer address this problem? Page 60

Features

Total Installed Cost Total installed cost comparison 7000 6000 5000 4000

Foundation Protection

3000

Installation cost Baseplate

2000 1000 0 PIP Style Baseplate

Steel Baseplate

Polybase Baseplate

Polyshield

Page 61

Polyshield            

Quick Installation Reduction Total Install Cost Corrosion Resistance Material Options Reduces Vibration One-piece Construction Available heights Flat mounting surface One-piece motor mounting block 4” Grout Hole Integral Grout Anchors Integral Drain Basin and Connection Page 62

Features

Standard Metal Coupling Guard  Carbon steel, stainless steel, aluminum  “Clamshell” design  Trimmed for exact fit  Heavy-duty support legs

Page 63

Features ™

™

ClearGuard and DurcoShield

Page 64

Flowserve ClearGuard

™

 Constructed of yellow-tinted, UV stabilized polycarbonate  Excellent corrosion resistance

 Provides physical safety barrier around coupling, protecting against:  Person’s body and/or clothing contacting rotating components  Components flying off a damaged coupling

 Extremely tough  Stronger than aluminum or steel guard  Can support 370 lbs.

 Allows static and dynamic inspection without removal  Allows rotational speed and direction inspection  DurcoShield™ is also available Page 65

Features  Envelopes area between housing & casing  Deflects spray from a malfunctioning seal  Provides protection from rotating shaft  Very easy to install and remove  Constructed of yellow (ClearGuard™) polycarbonate  Allows visual inspection of seal area  Application -70oF to 300oF (-57oC to 150oC)  Available in PVDF  Easy to drill or cut slots and holes for piping  Patented design

DurcoShield

TM

Page 66

Features

Mark 3 Inline Pump  Standard Mark III power end  Minimizes floor space  Lower installation cost.  Better able to accommodate piping loads  With Reverse Vane impeller, thrust is reduced  Shaft alignment fully adjustable Page 67

Features

Mark 3 Lo-Flo  Low flow  Heads to 985 feet (300m)  Conforms to standard ASME B73 dimensions  Standard Mark 3 power end  Radial vane  Pump out vanes  Balance holes  Maintains low seal chamber pressure Page 68

Features

Lo-Flo Casing  Reduces radial loads  Reduces shaft vibration

Circular Concentric Casing

Expanding Volute Casing Page 69

Features

Sealmatic Repeller Operating  Dynamic sealing  Eliminates the need for conventional seal

Static    

FXP TFE Disc Seal “Checkmatic” lip seal Flexible graphite packing Dry-running “lift-off” gas seal Page 70

•

The FXP Seal is made up of a 316 SS Rotor, a stationary Glass Filled PTFE Disk, and a 316 SS Gland to retain the Disk.

•

The Rotor face is tapered to provide a good match between the two parts and has concentric grooves machined into the sealing face. The concentric grooves provide sealing dams with high loading on each, providing consistent performance whether static or dynamic.

•

The Disk is piloted to insure good concentricity of the sealing surfaces, thereby minimizing leakage.

Figure 1

FXP Seal - Large-Bore Box Page 71

Features

Sealmatic Applications  Hard to seal services (Caustic, slurry)  Where water flush is undesirable (Evaporator feed, sulfuric acid)  Continuous duty

Page 72

Features

Self Priming  Compact  Motor and pump out of pumped liquid  Better alignment than cantilevered pumps  Relatively inexpensive  Easy installation and maintenance  Unitized casing includes  priming chamber  air separator  volute Page 73

Features

Applications  Sump Services  Waste water  Tank car unloading  Dike Sumps  Coal Pile Run Off  Suction Lift: 25 feet  Air bleed line required  Priming time varies by application Page 74

Features

Self-Priming Tank  Makes any pump self-priming  Materials  Steel  316SS  FRP  Proper sizing required  Operates under vacuum. Not suitable for pressure.

Page 75

Features

Recessed Impeller        

Vortex Maintains integrity of solids Pumps large solids Minimizes shear, abrasion, clogging Impeller clearance set at rear cover Tangential discharge casing Standard Mark 3 Power End Pump out vanes control seal pressure and minimize solids in the seal chamber Page 76

Features

Recessed Impeller Applications  Solids  Slurries  Corrosives  Abrasives  Waste streams  Shear-sensitive liquids  Less than 20% solids contact impeller Page 77

Features

High Silicon Iron  The most universally corrosion resistant alloy in the pump industry  Low mechanical shock resistance (treat like glass)  Low thermal shock resistance (keep temperature change within 100F per hour) Page 78

Features

Guardian  ANSI B73.1 dimensions  Wet end interchangeable with Mark 3  Power end pullout without breaking sealed containment  Uses standard NEMA motor  Sealless  Magnetic drive  MK3 RV Impeller  Provides consistent flow and pressure in containment shell  No wear rings or close clearances needed to maintain hydraulic balance or recirculation flow Page 79

Features  Solids

Limitations

   

300 micron (0.012”) Less than 3% by weight No ferrous particles 2 Moh maximum hardness  Talc = 1 Moh  Diamond = 10 Moh

 Viscosity  0.3 to 300 cp  others by review

 Temperature (process temperature PLUS rise in containment shell)

 G series: Minus 100F to plus 250F  H series: Minus 100F to plus 550F

 Magnetism decrease with temperature rise Page 80

Features

Power Protection Monitor  For overload protection    

Excessive wear or rubbing Bearing failure Decoupled magnets Motor overload

 For under-load protection       

Dry run Blocked suction Decoupled magnets Failed spacer element Air entrainment Minimum flow Loss of prime Page 81

Total Cost of Ownership • MAINTENANCE COST •Labor •Parts •Service

• OPERATION COST •Auxiliaries •Energy costs

• INITIAL COST •Equipment

Mark 3 Maximizes Reliability (MTBPM) and Save $$$ Page 82

FML SealSentryTM •

Flow Modified Large Bore (FML) – Turns centrifugal flow caused by the seal into axial flow by the ribs along the chamber

• •

FML handles up to 60% solids Goulds design is limited to 10%

Page 83

Oil Consumption Size

Mark 3 (oz) 3196i (oz)

• ANSI 3A Power End

Group 1 / STi

8.5

16

Group 2 / MTi

32

47

 Superior Reliability

Group 2 l LTi

N/A

47

Group 3 / XLTi

48

100

 Purchase / Disposal Cost

3 Years

2 Years

Intervals

 Cool Running Bearings  No Viscosity Breakdown  Goulds uses 2 times the amount of lubrication for the same performance  Goulds requires a shorter lubrication cycle

Page 84

Myth # 1 Two Times More Wear Area = Longer Life, Reduced Repair Costs

Goulds Claims…

The Truth Is… •

•

• • •

•

More working area being worn does not reduce the wear rate – it just damages more parts Adjusting open impellers towards the casing to compensate for wear increases the thrust loads from larger gap on backside causing seal chamber pressures to increase Cost to replace a rear cover is nearly 1/3rd the casing price Rear covers are much easier to replace than a casing (and can be resurfaced) Balance holes in the Reverse Vane impeller ensure hydraulic loads are similar in magnitude to open impellers If open impeller is required, the Mark 3 has this option available Page 85

Myth # 2 Enclosed Impellers Cannot be Adjusted

Goulds Claims…

The Truth Is… • •

•

•

Reverse Vane impellers are not fully enclosed Reverse Vane impellers are easily adjusted using micrometer adjustment Nose ring wear does not affect performance until it is almost gone (this is not a wear ring) With open impeller adjustment Goulds has to choose either performance or seal chamber pressure renewal. They can’t get both. With the Reverse Vane impeller, one adjustment renews both! Page 86

Myth # 3 Back Pump Out Vanes Control Axial Thrust

Goulds Claims…

The Truth Is… •

•

Goulds back pump out vanes wear too, so they become less effective and controlling thrust loading and seal chamber pressure over time Pump out vane wear combined with moving the impeller away from the rear cover for “performance renewal” means that significant pressure increase occurs behind the Goulds open impeller which adds to the thrust loads and seal chamber pressure

Page 87

 Max Sphere Size • Percent of Sizes with the Largest Passage Way – Flowserve: 86% – Goulds: 14%

Page 88

Better Interchangeability • Interchangeability  Only 3 Mark 3 Power Ends cover all sizes.  If customer has 6x4-10, then only shaft is different.

• Less Stock Required    

Only 3 Power Ends – Goulds has 4 sizes Only 3 Seal Sizes – Goulds has 4 sizes All Group 1 pumps use the same rear cover size Goulds has 2 cover sizes for Group 1 pumps

Page 89

Shaft Comparisons

Page 90

Competitive Product - ITT Goulds i-ALERT Features:

Weaknesses:

•

Small and compact

•

Field activated following start up

•

Temperature alert: • 175 F preset (two consecutive readings) • 195 F (91 C) max

•

Vibration in horizontal mode only

•

No Internal Memory Access

•

Measures overall vibration

•

Not User Configurable

•

Initial learn mode sets baseline

•

Green Light Normal, Red Light Alarm

•

No Data Logging Capability

•

Built into the pump frame

•

Battery life less than 1 year in alarm mode

•

No indication of past alert notification

• • •

Temperature Limit – factory set Vibration Limit – 2X baseline Polling Rate – 1 minute

Page 91

IPS Beacon: Straight Forward Monitoring and Alert System for Vibration and Temperature

IPS Beacon

TM

–

Patent Pending

–

–

LEDs Mounting Hole On / Off or optional IPS Beacon TAM (Take Away Memory)

–

Blinking green indicates normal condition Blinking red indicates either temperature and / or vibration is above the preset limit Alternate blinking red and green indicate that the equipment has returned to normal but that an alert condition had occurred within the last 14 days. Last Alert is time stamped and can be downloaded with optional Docking Station.

Standard High Level Thresholds For ANSI and ISO Pumps

Vibration: 9.4 mm/sec (.38 in/sec) RMS Temperature: 85C (185F) Sampling at 5 minute interval LED blinks at 5 second interval User Configurable w/ Optional Docking Station and Software Utility or

TAM for Extended Data Logging Page 92

IPS Beacon - Specifications • Three Axis Vibration Sensor measures vibration in either acceleration or velocity • Onboard Temperature Sensor measures temperature readings from -40 F to 200 F (-40 C to 93 C) • Material of Construction is a 316L Stainless Steel housing with borosilicate glass-protected LEDs providing vivid status indications.

• 14-Day Fault Indication provides extended visual notification of an alert condition over time • Battery Life can be more than four years depending on the environment and operating parameters • Certifications: CE, CSA (CL1, DIV 1, A,B,C,D,F&G,) ATEX and IECEx (CL 1, Zone 0)

Page 93

Questions?

Page 94