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Accurate, reliable, cost effective
flow measurement is more
important today than it has ever
been. The years have seen many
styles and grades of flowmeter
developed, because the first
problem in meter specification is
to define what the measurement
has to achieve. Dispensing a
volume of juice concentrate to
within 2% is a different problem
to knowing and alarming when
the cooling water flow drops to
50% of the desired flow, with a
system shutdown operating at
25%. Both are different to
measuring whisky or beer or
petrol delivery in a financial
transaction. This article presents
one view of the different
techniques that can be used for
liquid measurement: it does not
include every type of flowmeter
on the market, just some of the
more familiar ones.
Cost of ownership is often an
issue for end users and suppliers,
but, for an OEM (original
equipment manufacturer) maybe
a better phrase should be
“consequential costs of use”. The
cost of ownership is not just its
purchase price, but includes the
cost of any breakdown in the
warranty period; performance
loss resulting from measurement
uncertainty; and the power or
equipment cost of running both
the flowmeter and the fluid
pressure drop it introduces. The
cost of use for an OEM can also
include any separate wiring
needed, the positioning and
space taken up in the equipment,
including the straight line pipe
requirements, the weight and the
mounting arrangement, and any
separate display or output
interface.
Adding all these consequential
costs to the function required can
often lead to the choice of a
simple mechanical vane or paddle
wheel indicator, or a mechanical
totaliser - today this might
include self-contained battery
powered micro-electronics: think
of the modern electronic gas
meter, for example. The right
flowmeter for the job is the one
that will perform the task actually
required, satisfactorily, at an
acceptable fully installed cost.
Flowmeter Types
While all flowmeters can make
use of the latest technology, the
basic techniques are fairly well
established. Flowmeters will be
described falling into six broad
groups:
- Differential pressure devices:
(including variable area meters
and mechanical flap devices),
- Inferential devices such as
turbine meters, propeller meters
- Positive displacement meters,
including oval gear, nutating
disc, oscillating piston)
- Fluidic devices, vortex meters
- Velocity measuring devices such
as electromagnetic and
ultrasonic,
- Mass flow measurement meters
(Coriolis, thermal)
Each of these flowmeters has its
own strengths and weaknesses:
every different flowmeter style within these categories was
developed for one particular OEM
or customer application!
Differential Pressure
DP flow measurement is the
original method, but not
necessarily the best! It can be
used for the most mundane, and
the most critical duties. The Pitot
tube uses the differential
pressure generated by fluid
impacting the open end of a
tube facing the direction of flow,
a second tapping at ninety
degrees to the first measures the
"static" pressure. Used on an
aircraft this measures the
airspeed: some years ago a
maintenance engineer left some
masking tape over the static
pressure tappings on an aircraft
Pitot tube: the flight engineer
duly set his instruments to the
ground static pressure. As the
plane took off in poor weather,
the instruments gave nonsensical
readings: and the plane crashed.
This highlighted the
consequences of inadequate end
user installation and
maintenance procedures!
The most common method of
using this principle is with an
orifice plate, a hole in the bore of
the pipe that creates an
obstruction to flow: the square
root of the pressure differential is
proportional to the flow rate.
This is where one of the problems
with this type of device is
encountered. If the pressure
sensors have a 50:1 range the
resulting flow range of the
flowmeter is only 7:1, after the
square root extraction.
It is often quoted that DP cells
with orifice plates are the most
popular form of flow
measurement in the world today:
but this is probably not so for
OEMs. Not unless they buy the DP
cell with integral orifice complete,
calibrated, pressure tested and in
one unit, but then it will most
likely be too costly. Without the
integral unit the technique
involves too many connections
and parts to assemble.
Techniques derived from DP principles
There are many places that OEMs
would use other "DP devices": a
classic is a V-notch weir or flume
in an open channel, with a liquid
level measuring device that can
be a float or an ultrasonic level
meter or similar. Flumes are
available for such applications in
How to specify liquid flowmeters, particularly for OEM projects 2
the form of fibreglass moulds
from specialist suppliers. Far more
usual with OEMs are 'Variable
Area' flowmeters that consist of a
movable 'float' in a widening
aperture, but in this case the
differential pressure is used to
balance the 'float' against a force.
This is typically gravity as seen in
a bench top glass tube laboratory
VA meter, but some meters
balance a float, flap or vane,
against a spring, either in a metal
or glass housing, or as an
insertion device: this makes them
orientation independent, but
results in a higher operational
pressure drop. The forces
balancing the float are the mass,
velocity and viscosity of the
liquid. Simple visual devices are
capable of ±1% accuracy, but
±5% is more likely. All such
devices can have electronic 'bolton'
analogue outputs these days,
or alarm trips, driven by a magnet
in the float or flap.
There are many specific designs:
like metal bodied VA units for
high pressure, using magnetically
driven indicators, PTFE lined tubes
for corrosive liquids, single alarm
set point low flow switches for
domestic water heaters. All
tolerate any installation pipework
format, and dirt in the liquid,
since the aperture just opens
further if the pressure is available.
Some are really low cost and easy
to troubleshoot: flow range is
typically between 7:1 and 10:1,
and a 1% device is possible.
Turbine and Propeller meters
A turbine meter is the most
common and easiest to
understand of all the different
inferential meters. The axial
turbine meter is basically a
propeller in a pipe; with careful
design the speed of the turbine
is directly proportional to the
flow rate. Accuracies of ±0.25%
are achievable. They have many
advantages: they are relatively
small and are usually the same
diameter as the pipe in which
they are fitted, and pressure loss
is quite low. Because of this
tubular construction high
pressures and temperatures are
readily accommodated. All
turbines are sensitive to viscosity
changes and should be
manufactured and calibrated
with the final application in
mind. They are only as good as
their bearings and the smaller
the axial turbine the more
important the bearing characteristics, as
the energy available
to overcome the
bearing friction is
somewhat reduced -
and the bearings,
being smaller, are
more sensitive to
degradation.
Pelton wheel or
radial flow turbines
are therefore better
suited to low flows
as the bearings can
be very robust: the
energy available
from the liquid flow
around this type of
enclosed 'water
wheel' is far greater
than available with
the axial device.
They are particularly
suited to OEM
applications such as
beverage dispensing
or monitoring. A disadvantage
of this type of meter is the
relatively large body compared
to the line size, greater
pressure drop and reduced
accuracy. Advantages however
include low manufacturing
costs, a larger dynamic range
and the ability to meter very
low flows, 10 mL/minute or
lower.
Electronic outputs are provided
either by a magnetic or optical
pick off to count the rotation of
the wheel or turbine. Pick-offs are
moulded into the body housing:
even the electronics for a totaliser
or flowrate display can be housed
within the meter body. Typically
axial or Pelton wheel devices are
produced in moulded modern
engineering plastics,
which are corrosion
resistant and can be
fitted with push-on
fluid connectors, hose
barbs or screw
threads. Custom
engineering of these
connections allows
them to incorporate
panel or bulkhead
mounting
arrangements to suit
the application, and
the electrical wiring
loom and
terminations can be
similarly customised.
Positive Displacement meters
There are many
different types of
positive displacement
meter, gear, oval
gear, sliding vane,
nutating disc, oscillating piston,
helical screw and many more. All
have the same basic mode of
operation in that they take a
discrete volume of liquid and pass
it from the inlet to the outlet
without loss or slippage.
The better types are capable of
±0.1% linearity over a wide flow
range. By nature these devices
How to specify liquid flowmeters, particularly for OEM projects 4
The range of Pelton wheel based low flow metering sensors from Titan
measure flows from 0.05 to 30 LPM. Units with built in battery powered
LCD totalisers have been adapted for use in vending and drinks dispensing
machines, and also to monitor beer flow totals in busy bars and clubs.
perform better at
higher viscosities as
the increasing fluid
thickness reduces the
leakage rate even
further and extends
the useful operating
range to lower flow
rates. Globally the
most common form
of this device are
likely to be domestic
water meters and the
meters found in
petrol dispensing
equipment. Because
of the way these
meters operate they
often have a highpressure
drop,
particularly with
more viscous fluids,
but some types
including the oval
gear design operate
with a very low
differential pressure,
only millimetres of
head in some cases.
They are very suitable
for measuring oils, although some
models are manufactured
specifically for corrosive media:
for example there is a version of
an oval gear meter made from
totally non-metallic plastic and
ceramic components. In all cases
the fluid should not contain any
solid particles or stringy materials,
as these would possibly jam the
meshing gear or other
mechanisms. The bodies for larger
pipe sizes are very large, and
housings suitable for high-pressure
use become heavy. In
the smaller sizes they
are a very economic
and accurate metering
solution.
The output of these
devices is a simple
pulse, which defines
the passage of a
defined volume of
liquid. They are
therefore easy to
interface with simple
counting electronics.
Several versions have
integral electronic
displays and
transmitters, some
being battery
powered.
Fluidic and Vortex flowmeters
These flowmeters use
the natural
oscillations that can
occur as fluids flow
past an obstruction,
such as make a flag
flap on a flagpole. The sensing of
these oscillations is fairly difficult,
particularly if the pipeline itself
has extraneous noise, so they are
used on some specific flowmeter
applications, and not typically by
OEMs.
Ultrasonic and Electromagnetic flowmeters
In an ideal world the flowmeter
would be a section of pipe with no
intrusions and so no pressure drop.
Two types of commercially
available meter have come very
close to this: electromagnetic and
ultrasonic flowmeters both use full
pipe bores, measure the liquid
velocity and are inherently bidirectional.
Electromagnetic meters have good
rangeability, are available in a wide
range of pipe sizes, have low
pressure loss, and power
requirements are constantly being
reduced as better magnetic and
electronic techniques are being
found. They will handle sewage,
slurries and paper pulp. If the
materials are selected carefully the
“electrodes” are capable of
handling very aggressive materials.
They require the flowing liquid to
be electrically conductive, but the
lower limits on this are constantly
decreasing. While prices are falling,
they still tend to be expensive, and
would only be used on slurries or
such difficult liquids. Electromagnetic
meters measure liquid flow velocity,
averaged across the flow profile:
they can tolerate some flow profile
disturbance and retain reasonable
accuracies.
The main type of ultrasonic
flowmeter uses two or more
transducers that fire a pulse of
ultrasound at an angle both with
and against the flow; the
difference in time between the
signals is effectively the flow rate.
Multi-beam units are used for
very large pipes and in most sizes
they are available as clamp-on
devices. Special designs are used
in small lines, to increase the path
length by several reflections, or
the flow path is made to run
along the pipe axis, as in the
domestic gas meter. Suitable for
cleaner liquids rather than
slurries, this type of meter is
currently forecast to show the
greatest growth in the next ten
years. The multi-path units are
used to improve the flow profile
averaging, across the pipe, and to
correct for skew flow, which can
produce large inaccuracies.
The original ultrasonic meters,
introduced in around 1978, used
one clamp-on transducer, and
sensed reflected signals returned
by particles or suspended solids in
the flow, which shifted the
transmitted frequency according
to the Doppler effect. In a
vibration free pipe, with a firmly
clamped or bonded transducer,
these units could achieve a
reasonable flow indication or
flow failure alarm, particularly for
monitoring reasonable velocity
slurry or sewage flows.
Unfortunately, as the first clampon
reasonably priced meter
system introduced, the Doppler
was sometimes applied to
unsuitable applications, which led
to a poor reputation: there are
still some suitable applications
today, alongside meters that
measure flow noise or particle
impact sounds.
Mass Flowmeters
Most mass flowmeters are Coriolis
meters, using the fact that when a
fluid is accelerated in a curve
there is a reaction force at ninety
degrees to the acceleration. If the
resultant force or movement can
be measured, the result is a mass
flowmeter. This is different to all
of the previously listed meters, as
they have all been volumetric or
velocity measurement devices, and
often use an electronic package to
convert velocity into volume flow,
given the flowmeter dimensions.
These Coriolis systems measure
mass flow directly, separately
measure the fluid density, and can
then deduce volume flow. They
are very accurate: with
homogenous fluids accuracies of
±0.1% are often quoted, and
calibrations that can achieve
How to specify liquid flowmeters, particularly for OEM projects 6
0.01% are being discussed. The
only restriction such meters
commonly put to the flow is the
bend in the pipe, although
straight tube models are available.
These meters are very expensive:
but prices are falling. Some
versions are very sensitive to
errors induced by two-phase flow
conditions, such as vapour
included with the liquid. This is
true for all types of flowmeter but
the errors can have serious
implications for mass flow meters
that are designed to achieve the
ultimate in accuracy.
Thermal mass flow systems
commonly used for controlling
low gas mass flows are now being
introduced for liquids. The
technique uses a measure of the
power required to maintain a
temperature increase in the
flowing liquid down a bypass
capillary, usually in a side flow
path routed around an orifice in
the main line. It is typically used
with an integral flow controller
such as a valve, to maintain a
fixed flow dictated by an
electronic input.
Flowmeter recommendations by duty required
The chart below gives a brief
summary of the different types of
meter and their suitability for
various applications.

Installation Effects
Having purchased a flowmeter it
is very easy to compromise its
performance with poor
installation. With the exception
of the positive displacement
meters and small Pelton wheels,
upstream and down stream pipe
work configuration can drastically
affect the meter performance.
Two bends at ninety degrees to
each other can stop a turbine
meter at some flow rates, as the
liquid can swirl at the same angle
as the turbine blades and just slip
past. Conversely if the swirl is in
the opposite direction the meter
will over register. Bends, valves,
regulators, tees, pumps and
almost anything else introduced
into the pipe work will disturb
the flow. Manufacturers specify
the meter for ideal installations
and any variation from this
negates the performance
characteristics.
Even when the pipework is
perfect many applications are
compromised with poor electrical
installation. Signal wires should
where possible be screened,
routed away from and shielded
from mains supplies, inverters,
relays, solenoid valves, highly
inductive loads and switching
apparatus, as these can all modify
the signals. Correct signal
conditioning and protocol
reduces these problems
dramatically.
Footnote
This article was first published in the European Design Engineer, April 2005.
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