Six Critical Things You Can Learn From a Flow Spot Check Speaker: Dan - - PowerPoint PPT Presentation

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Six Critical Things You Can Learn From a Flow Spot Check Speaker: Dan - - PowerPoint PPT Presentation

RAECO Customer Webinar Six Critical Things You Can Learn From a Flow Spot Check Speaker: Dan Kilpatrick GE Measurement & Control Agenda Ultrasonic Meter Basics Application Considerations Six Things You Could Learn Questions Dec. 2002


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SLIDE 1

RAECO Customer Webinar

Six Critical Things You Can Learn From a Flow Spot Check

Speaker: Dan Kilpatrick GE Measurement & Control

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SLIDE 2

Agenda

Ultrasonic Meter Basics Application Considerations Six Things You Could Learn Questions

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SLIDE 3
  • Dec. 2002

GE Panametrics

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 Transducer is Both Transmitter and Receiver  Ultrasonic Pulses  Transit Times

Upstream direction, tup

Downstream direction, tdn

 tup = Ultrasound is Decelerated by Flow  tdn = Ultrasound is Accelerated by Flow  Analogous to a Flowing River

t t t t t V f( t) Q V A

up dn up dn

       

UP DOWN V

Theory: Transit Time Technique

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SLIDE 4
  • Dec. 2002

GE Panametrics

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NO FLOW

DISTANCE RATE TIME TIME DISTANCE RATE   

t P c t P c t t t

up dn up dn

     

WITH FLOW

t P c -Vsin t P c+ Vsin t t t

up dn up dn

      

V V     c c

DN UP

V

L P

Theory: Transit Time Technique

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SLIDE 5
  • Dec. 2002

GE Panametrics

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Theory: Transit Time Technique

VELOCITY

V P 2L t t t t

2 up dn dn up

          

SOUND SPEED

t t t 2 c = 2P t

avg = dn up avg

Q = Velocity  Cross- Sectional Area Q = V  A VOLUMETRIC

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SLIDE 6
  • Dec. 2002

GE Panametrics

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Full Pipes Only

Accuracy Signal Loss

Q = V  A

Liquid Flow Application Considerations

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SLIDE 7
  • Dec. 2002

GE Panametrics

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Pipe Condition

 Single versus Double Traverse Configuration

Liquid Flow Application Considerations

As the drawing above shows, the location at which the signal coming from the first transducer bounces off the wall towards the second transducer is an area with high potential for attenuation.

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SLIDE 8
  • Dec. 2002

GE Panametrics

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Pipe Condition

 Clean Outside Surface (to eliminate “bumps”caused by rust and excessive amount of paint)  Also, don’t forget to use couplant (for good contact)

Liquid Flow Application Considerations

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SLIDE 9
  • Dec. 2002

GE Panametrics

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Liquid Flow Application Considerations

Pipe Size

 Overall Range: 1/2” to 200” (12 mm to 5 m)  Transducer Selection

1/2” to 2” 2” to 200”

 Clamping Fixture Selection  Transducer Frequency

1.0 MHz for standard applications 0.5 MHz for large pipes 4.0 MHz for small pipes 2.0 MHz for special applications

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SLIDE 10
  • Dec. 2002

GE Panametrics

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Large Pipes

2” to 200” OD Standard & Special Clamping fixtures

Liquid Flow Application Considerations

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SLIDE 11
  • Dec. 2002

GE Panametrics

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Liquid Flow Application Considerations Pipe Material

Metals

Carbon Steel Stainless Steel Copper Aluminum Cast Iron Brass Ductile Iron

WT

Plastics

  • Polypropylene
  • Polyethylene
  • PVC
  • CPVC
  • PVDF
  • Nylon
  • Acrylic
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SLIDE 12
  • Dec. 2002

GE Panametrics

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GOOD LOCATIONS BAD LOCATIONS

Straight Run Requirements

Liquid Flow Application Considerations

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SLIDE 13
  • Dec. 2002

GE Panametrics

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Straight Run Requirements

 Fully Developed Flow Profile  10 Upstream/5 Downstream Diameter  What If I Don’t Have 15 Diameters?

 2/3 up, 1/3 down  Multipath  Flow straighteners  Accuracy cannot be

quantified

 Repeatability

Liquid Flow Application Considerations

10 5

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SLIDE 14
  • Dec. 2002

GE Panametrics

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Straight Run Requirements

The more diameters

  • f straight run

available, the better the measurement will be

Liquid Flow Application Considerations

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SLIDE 15
  • Dec. 2002

GE Panametrics

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BEFORE... AFTER...

Straight Run Requirements

The good vs. the “not-so-good” locations

Liquid Flow Application Considerations

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SLIDE 16
  • Dec. 2002

GE Panametrics

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Viscosity Range

Maximum ~300 centistokes Attenuation Low Reynolds Number

Attenuation Viscosity

300

less more

Liquid Flow Application Considerations

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SLIDE 17
  • Dec. 2002

GE Panametrics

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Liquid Flow Application Considerations

Velocity Range

 Minimum Detectable Velocity = 0.1 ft/s (0.03 m/s)  Maximum Detectable Velocity = 40 ft/s (12m/s)  Resolution of t: Higher Velocity, More t  Good: V > 1.0 ft/s (0.3 m/s)  Use the Slide Rule

Equations

Area = Q = VA

 ID 2      

2

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SLIDE 18

18 GE Title or job number 3/13/2015

Number 1

Validate Pump /Control Valve Operation & Performance

Capable of measuring up to 750 F Boiler Feedwater Applications Utility and PowerGen

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SLIDE 19

19 GE Title or job number 3/13/2015

Number 2

Identify Leaks

Same set of Transducers can measure 2” to >36” Datalogging allows for comparative analysis over time between multiple meters installed on same line Verify positive valve shutoff

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SLIDE 20

20 GE Title or job number 3/13/2015

Number 3

Verify Other Flowmeters within Facility

Magmeters, Vortex meters, Impeller, DP Use USM diagnostic data to confirm measurement Signal Strength (SS) Sound Speed (SDSP)

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SLIDE 21

21 GE Title or job number 3/13/2015

Number 4

Balance CW or HTHW Loops

Energy Management Feature Converts Flow to BTU’s, and Tonnage Campus Energy/Central Utility Plants Technicians use for troubleshooting other meters as well as identifying locations for permanent ultrasonic flowmeters

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SLIDE 22

22 GE Title or job number 3/13/2015

Number 5

Help Properly Size Ancillary Plant Equipment

Facility Upgrades Heat Exchangers Cooling Towers Enable Process/Plant Engineers to Make Informed Decisions Regarding Upgrade Projects

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SLIDE 23

23 GE Title or job number 3/13/2015

Number 6

Chemical Plant Mass Balance

Ultrasonic meter can be programmed for measurement of variety of chemicals Chemical compatibility not an issue due to non- contact measurement

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SLIDE 24

24 GE Title or job number 3/13/2015

Bonus

Confirm Flow Direction and Pipe Line Conditions

Old undocumented pipes Meter measures bi-directional flow Water/Wastewater Industry Verify if pipe is full by meter diagnostics

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SLIDE 25

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