Midterm Preparation Flashcards
Causes of flow
Fluid velocity depends on
differential head pressure
Causes of flow
Increase pressure or force
increases fluid flow rate
Causes of flow
ΔP Forces fluid to
flow through pipe
Causes of flow
ΔP created by
physical (height difference) or mechanical means, pumps/compressors
factors that affect selection of flow measuring method
- Pressure
- Temperature
- Velocity
- Density
- Viscosity
Force per unit area
Pressure
Pressure Effect
Liquids generally _______, little change in _____ when pressure exerted
- incompressible fluids
- volume
Pressure Effect
Gases are ________
compressible
Temperature
Boiling Water at STD =
212o F, 100oC
Temperature
F ̊ + 459.69 =
Rankine (R)
Temperature
C ̊ + 273.15 =
Kelvin (K)
Temperature
Freezing =
32 ̊ F , 0 C ̊ (absolute temp 491.69R & 273.15 K)
Most flow problems require the use of absolute temperature
Temperature Effect
In general fluids will decrease in density as the temperature ____
increases
Temperature Effect
As the density _____ with the rise of temperature the volume of the fluid will increase
decreases
Temperature Effect
Increase in the volume due to temperature will need to be _____ for accurate Flow measurement
compensated
Mass of substance per unit volume
Density
Weight due to g per unit volume
Specific Weight
SI term for Specific Gravity is
RELATIVE DENSITY
Density Effect
Use density of a fluid to calculate the ____
mass flow
Resistance of flow of a fluid
Stickiness of a fluid
Common unit is centipoise (cP) 1/100 of a poise
Dynamic Viscosity
ratio of thedynamic viscosity (μ)
to the Density (ρ) of the fluid
Common units are centistokes (cS)
Kinematic Viscosity

laminar flow

Turbulent flow
Properties of Pipe & Flow
Rough inside of pipe will ___ flow of fluid along pipe wall
slow
Properties of Pipe & Flow
Most meters need profile to be flat as in____
turbulent flow
Properties of Pipe & Flow
Smooth pipe preferred ________
upstream of meter
Purpose of Pump & Compressor
If the fluid is incompressible such as a liquid needs a _____ to move it
pump
Purpose of Pump & Compressor
If the fluid is compressible such as a gas need a ______ to move it
compressor

Orifice plate with flange taps for gas or liquid flow

Orifice plate c/w orifice plate changer, to change orifice while on line

Venturi tube for gas or liquid flow

Flow nozzle normally used for steam flow

Pitot tube, normally used for flue gases in stacks or
water flow in large pipes

Weir, for flow in large aqueducts, i.e. irrigation canals

Flow straightening vane, used before or after orifice to remove turbulence

Turbine or propeller type meter for gas or liquid

Variable area flow indicator or rotameter

Mass flow with integer transmitter

Vortex meter sensor for liquid or gas

Magnetic flowmeter with integral transmitter for conductive liquids

Magnetic Flowmeter

Thermal mass flowmeter

Coriollis flowmeter

Sonic / Ultrasound flowmeter

Positive displacement meter c/w totalizer and indicator

Ultrasonic (sound frequency) flowmeter,
Doppler or Transit Time

Averaging pitot tube for very large flue stacks
Primary Elements - Flow

Generic orifice plate
Restriction plate
Primary Elements - Flow

Orifice plate in quick-change fitting
Primary Elements - Flow

Concentric circle orifice plate
Restriction orifice
Primary Elements - Flow

Eccentric circle orifice plate
Primary Elements - Flow

Circle quadrant orifice plate
Primary Elements - Flow

Multi-hole orifice plate
Primary Elements - Flow

Integral orifice plate
Primary Elements - Flow

Generic venturi tube, flow nozzle, or flow tube
Primary Elements - Flow

Venturi tube
Primary Elements - Flow

Flow nozzle
Primary Elements - Flow

Flow tube
Primary Elements - Flow

Standard pitot tube
Primary Elements - Flow

Annubar
Primary Elements - Flow

Turbine / propeller flowmeter
Primary Elements - Flow

Vortex shedding flowmeter
Primary Elements - Flow

Target flowmeter
Primary Elements - Flow

Positive displacement flowmeter
Primary Elements - Flow

V Cone meter
Primary Elements - Flow

Wedge meter
Primary Elements - Flow

Variable area flowmeter
Primary Elements - Flow

Open channel Weir / Flume
Types of Differential Pressure instruments:
- Elbow
- Flow Nozzle
- Orifice
- Pitot Tube
- Pitot Tube (averaging)
- Venturi
- Wedge
Types of Positive Displacement instruments:
- Nutating disc
- Oscillating Piston
- Oval Gear
- Roots
Types of Ultrasonic instruments:
- Doppler
- Transit time
Types of Variable Area instruments:
- Movable Vane
- Rotameter
- Weir, Flume
Coriolis (Miscellaneous)
Measures Accelerations and the result is
mass
Differential Pressure (Pressure)
measures pressure and the result is
volume
Magnetic (Electronic)
Measures Electromagnetic Field and result is
velocity
Positive Displacement (mechanical)
Measures volume and the result is:
volume
Target (mechanical) measures force
and the result is
velocity
Thermal (Miscellaneous)
Measures heat transfer and the result is
velocity
Turbine (mechanical)
Measures volume and result is
volume
Ultrasonic (Electronic)
Measures accostic waves and result is
velocity
Variable area (pressure)
measures pressure and result is
volume
Vortex (mechanical)
Measures frequency and the result is
velocity
is the only flow measurement technology that directly measures the volume of the fluid passing through the flowmeter.
Positive displacement flowmeter technology
repeatedly entraps fluid in order to
measure its flow
Positive displacement flowmeters
- float of given density’s establishing an equilibrium position for a given flow rate
- the upward force of the flowing fluid equals the downward force of gravity
Rotameter
Principle of Operation
Mag Meters
Fluid must be conductive
Coils generate magnetic field
The higher the flow speed, the higher the voltage
Principle of Operation
Vortex Shedder
The alternate shedding of vortices is the basis of meter operation.
Principle of Operation
Turbine flow meters
like a windmill, utilize angular velocity (rotation speed) to indicate a flow velocity
K factor units =
pulses/unit volume
K factor
defines the relationship between flow rate and ___
The frequency
Principle of Operation
Doppler
Principle of Operation
Transit Time
Principle of Operation
Coriolis
_______flowmeters that produce a pulse output
use a k-factor
Vortex and Turbine
Orifice Plate Types :
Concentric
Eccentric
Segmental
For differential flow meters; flow varies directly as the _____
square root of the differential pressure
DP Meters
Orifice Advantage
Use on liquid, gas, and steam
Suitable for extreme temperatures and pressures
No moving parts
Low material cost
Changeable without de- pressuring process
Low cost
DP Meters
Orifice Disadvantage
Limited range ability
Affected by changes in density, pressure, and viscosity
Maintenance intensive
High pressure loss
Non-linear output, square root extraction required
DP Meters
Nozzle Advantage
Use on liquid, gas, and steam
Nozzle used in Steam applications
Low system pressure loss
Do not require upstream flow profiling
DP Meters
Nozzle Disadvantage
Limited range ability 6:1 & accuracy ±2%
Expensive to install Requires high Reynolds numbers (>10,000)
Less permanent pressure loss than orifice, more than Venturi
Non-linear output, square root extraction required
DP Meters
Venturi Advantage
Venturi principally used in Water & Wastewater apps Lower non-recoverable pressure loss than orifice
DP Meters
Venturi Disadvantage
Initial cost more expensive than orifice plate
**Non-linear output, square root extraction required **
DP Meters
V-Cone Advantage
Less straight-run upstream piping required than orifice plate
DP Meters
V-Cone Disadvantage
Non-linear output, square root extraction required
DP Meters
Pitot Tube Advantage
Very small pressure loss
DP Meters
Pitot Tube Disadvantage
Non-linear output, square root extraction required
Used with clean fluids
Variable Area
Rotameters Advantage
No external power required for local reading
Simple design able to be mass produced, low cost
Scale is linear due to variable area design
Variable Area
Rotameters Disadvantage
Mounted in vertical position only, flow moving upwards Floats designed for specific gravity, correction required when used in other medium
PD Meters
Nutating Disc Advantage
Ideal for viscous fluid
High accuracy & repeatability
Minimal straight piping runs
May be constructed from a variety of materials
PD Meters
Nutating Disc Disadvantage
Mechanical parts on flow indication wear
Accuracy is adversely affected by viscosities below the meter’s designated threshold.
PD Meters
Oval & Gear Advantage
Measurement independent of viscosity(high)
Ease of installation(tight areas, no straight pipe runs required )
PD Meters
Oval & Gear Disadvantage
Not recommended for water or water like fluids (slippage) Mechanical parts wear
PD Meters
Sliding Vane Advantage
Sweeping action of vanes prevents buildup of sediment and keeps compartment clean.
Wide choice of construction materials.
High accuracy and repeatability.
Low pressure drop over entire range of flow measuring capabilities
PD Meters
Sliding Vane disadvantage
Mechanical parts wear
PD Meters
Piston Advantage
High accuracy and repeatability.
Only one moving part to cause wear.
Can be made of materials to ensure sanitary needs of food and beverage processing.
PD Meters
Piston disadvantage
Can only be used with relatively clean liquids.
Meter Type :
Turbine Advantage
Easy to install and operate Easy to service in the field High Accuracy &Repeatability Self-clearing design Instantaneous flow rate Indicator & totalizer on every
model
Flow range of up to 10:1 No Power Needed
Used with Gas or liquid
Meter Type :
Turbine disadvantage
Requires clean low viscosity fluid Upstream conditioning (straightening vanes) Vibration sensitive Numerous moving parts that could clog, bearings wear out Frequent calibration required Loss of linearity at low flow rate
Meter Type :
Paddle Wheel Advantage
Low cost for certain degree of accuracy
Measure flow in either direction
Axles and paddles easily replaced
Meter Type :
Paddle Wheel disadvantage
Use with clean fluid Solids in fluid can damage paddles
Avoid low flow
Linear
Magnetic Advantage
No obstructions to the flow No moving parts to wear or break
Maintenance free
Debris or solids will not clog the meter, ideal for slurries No head loss
Bi-directional flow Unaffected by changes in density and viscosity
Linear output Large turndown
Linear
Magnetic Disadvantage
Mag meters require a conductive process fluid
No gases or steam Entrapped air, foam, or two- phase flow cause errors
Liner pressure/temperature limits
Power consumption of 4-wire device
Special installation requirements Grounding/Valve liner requirements
Meter must be full
Linear
Ultrasonic Advantage
No moving parts Unobstructed flow path Wide range ability
Linear
Ultrasonic Disadvantage
Reynolds number constraints Entrained gas or particles for Doppler
Clean liquids for time of flight Straight run piping requirements
Linear
Vortex Advantage
No moving parts Regular calibration not required
Liquid, gas or steam Wide range ability
Linear
Vortex Disadvantage
Span limitations due to viscosity
Flow profile sensitive(high Reynolds number)
Mass
Coriolis Advantage
Direct mass flow measurement
Gives density measurement also
Works with viscous fluids Low Pressure drop Corrosive liquids measurement possible
High turndown ratio (100:1)
Able to work with high pressure and temperature High repeatability and accuracy
Mass
Coriolis Disadvantage
High purchase Cost
High installation cost
Mounting position requirements
Mass
Thermal Advantage
Relatively inexpensive Turndown 100:1
Monitoring low flow
Easy to install remove under pressure
Mass
Thermal Disadvantage
Gas application only (monitor liquid flow)