Filtering samples to on-line analyzers
Use these guidelines to ensure proper filtration and delivery of samples to on-line process analyzers.
Ken Perrotta, Division Engineering Manager
Allan Fish, Product Manager
Parker Hannifin
Corporation
Filtration and Separation Division
Haverhill, Massachusetts
Increasingly precise process control strategies,
often linked to computer control,
have accelerated the use of sophisticated
on-line chemical composition analyzers
in plant applications. Instruments
such as gas and liquid chromatographs,
ion chromatographs, laser optic instruments,
atomic absorption instruments and
specific ion analyzers, which were rarities
in laboratories ten years ago, are now
found routinely in plant settings.
While
continuing miniaturization and “ruggedization”
of the electronics are making the
instrumentation circuitry more tolerant of
the plant environment, a problem that will
not diminish is the level of contamination
in plant samples compared to laboratory
samples.
Factors in plant operation that magnify the
difficulty of delivering acceptable samples
to on-line process analyzers are:
• The sample stream must be processed
and fed to the analyzer continuously, rather
than the batchwise method permissible in
the laboratory.
• Test frequency in the plant is far greater
than in the laboratory. Where a laboratory
analyzer might perform 100 tests a
month, an on-line plant analyzer could do
100 tests a day. In the high frequency plant
usage, trace contaminants that would not
be a problem in the laboratory can rapidly
build up and cause instrument failure.
Filter requirements.
It is not surprising
that contaminants in the plant samples are
reported to be the most frequent cause of
problems with on-line analyzers.
While the requirements for an effective filter in the
sampling line is generally recognized, it is
also important to recognize that it is usually
necessary to use a filter specifically
designed for sampling applications, rather
than trying to make do with a general purpose
or homemade filter.
The characteristics that a sample filter
should have, in addition to filtering out
contaminants, are:
• The filter must not change the composition
of the sample, other than to remove
unwanted impurities. Therefore, the choice
of filter media generally is limited to a few
chemically inert materials: glass, stainless
steel and PTFE.
• Since the sample filter often is in a
remote or inconvenient location, it must
be capable of operating for a reasonable
period between scheduled maintenance
checks. Even more important, it should not
be susceptible to unscheduled problems,
such as filter element plugging or rupturing,
between regular maintenance checks.
• Sample filter maintenance in the field
usually is performed under adverse conditions
by personnel who are not trained
chemists; therefore, the filter should be
designed for easy and uncomplicated
maintenance. Filter elements should be
rugged and not susceptible to handling
damage; the unassembled housing should
have a minimum number of loose parts,
and the housing should be designed so
that it is virtually impossible to install a
filter element incorrectly.
• A filter should introduce minimum lag
time into the system. Lag time can be dealt
with in the sample system design (slipstream
sampling, for example), but sizable
dead volume in the filter housing should
be avoided. Since large reservoir volume is desirable in many filter applications - such
as compressed air or water filters - filters
not specifically designed for sampling usually
are not suited for analyzers.
Requirements for sample filters range so
widely that specifying a filter is best done
on a case-by-case basis.
There is, however,
one generalization that applies to all
sample filter requirements: the filter must
be able to separate efficiently a noncontinuous
phase contaminant from the continuous
sample stream phase. Specifically, the
filter must be able to make the following
separations, in addition to removing solid
particles:
• Gas samples - remove liquid droplets
• Liquid samples - remove immiscible
liquid droplets and gas bubbles.
Most filter media will do an adequate job
of removing solid particles from liquids
or gases, but the only practical commercial
media that will separate liquids from
gases, gas bubbles from liquids, and two
immiscible liquids is resin-bonded glass
microfiber media. All recommendations
in this paper are based on resin-bonded
glass fiber media.
Figure 1: External reservoir for high pressure applications
Figure 2: Slipstream or bypass filtration
Figure 3: Slipstream plus coalescing filtration
gases. The filter fibers capture the fine liquid droplets suspended in the gas and cause the droplets to run together to form large drops within the depth of the filter tube.
The large
drops are then forced by the gas flow to
the downstream surface of the filter tube,
from which the liquid drains by gravity.
This process is called “coalescing”. Since
the coalesced liquid drains from the tubes
at the same rate that liquid droplets enter
the tubes, the tubes have an unlimited life
when coalescing liquids from relatively
clean gases, and the filters operate at their
initial retention efficiency even when wet
with liquid.
The flow direction is inside-tooutside
to permit the liquid to drip from the
outside of the filter to the housing drain.
The filter tube grade should be selected
for maximum liquid drainage rate, rather
than maximum filtration efficiency rating.
Since liquid drainage rate decreases with
increasing filtration efficiency rating, this is
a clear case where overspecifying filter efficiency
will lead to unsatisfactory results.
If liquid is carried into the filter in slugs
rather than dispersed as droplets in the
gas, a filter that is properly sized for
steady-state conditions can be flooded
and permit liquid carryover.
If slugging
of liquid is expected, a filter with a relatively
large bowl should be selected to
provide adequate liquid holding capacity,
and positive provisions should be made
to drain the liquid automatically from the
bowl of the housing as fast as it accumulates.
An automatic float drain can be
used if the pressure is in the 10 to 400 psig
range. Above 400 psig, the upper limit for
commercially-available float drains, the
possibilities are: a constant bleed drain, a
valve with an automatic timed actuator, or
an external reservoir with manual valves
(see Figure 1).
The external reservoir can
be constructed of pipe or tubing with sufficient volume to hold all the liquid that is
expected to be collected during any period
of unattended operation.
To drain liquid
while the filter is operating at pressure or
vacuum conditions, valve #1 is closed and
valve #2 is opened.
If the filter is under vacuum, the external
reservoir is a practical method of collecting
coalesced liquid for manual draining
periodically.
Alternatively, if any external
vacuum source is available, such as an aspirator,
the liquid may be drained continuously
from the housing drain port.
Separating two liquid phases.
In principle, glass microfiber filter tubes separate suspended droplets of a liquid which is immiscible in another liquid by the same process as they separate droplets of liquid form a gas.
The liquid droplets suspended
in the continuous liquid phase are trapped
on the fibers and run together to form
large drops, which are then forced through
the filter to the downstream surface.
The
large drops separate from the continuous
liquid phase by gravity difference, settling
if heavier than the continuous phase and
rising if lighter.
The coalescing action of
glass microfiber filters is effective with
aqueous droplets suspended in oil or other
hydrocarbons, and also with oil in water
suspensions.
In practice, however, liquid-liquid separations
are much more difficult than
liquid-gas separations. The specific gravity
difference between two liquids is always
less than between a liquid and a gas, and
therefore, a longer phase separation time
is needed.
Either the filter housing must be
oversized or the flow rate greatly reduced
to avoid carryover of the coalesced phase.
As a rule of thumb, flow rate for liquidliquid
separation should be no more than
one-fifth the flow rate for solid-liquid
separation.
Even at low flow rates, if the specific gravity difference between the two liquids is less than 0.1 units (for example, if an oil suspended in water has a specificgravity between the two liquids is less than 0.1 units (for example, if an oil suspended in water has a specific gravity between 0.9 and 1.1), the separation time for the coalesced phase may be impractically long.
In that case, if there is only a small quantity of suspended liquid, the filter tube can be used until saturated with the suspended liquid and then changed.
Another practical problem with liquid-liquid separations is that small quantities of impurities can act as surface-active agents and interfere with the coalescing action. For that reason it is not possible to predict accurately the performance of a liquid-liquid coalescing filter, and each system must be tested on site.
The general guidelines for the system to start testing are to use 25 micron filter tubes and flow inside-out at very low flow rates. If the suspended liquid is lighter than the continuous phase the housing should be oriented so that the drain port is up.
Removing gas bubbles from liquids. Glass microfiber filter tubes readily remove suspended gas bubbles from liquid, eliminating the need for de aeration tanks, baffles or other separation devices. Flow direction through the filter is outside-to-inside, and the separated gas bubbles rise to the top of the housing and are vented through the drain port.
If slipstream sampling is used (see below), the separated bubbles are swept out of the housing with the bypassed liquid. Filter tubes rated at 25 micron are a good choice for gas bubble separation.
Slipstream or bypass sampling. Instrument sample use rates are invariably quite low, yet it is essential to minimize lag time in the sample system. Since analyzers often are located some distance from the sampling point, samples usually are transported to the analyzer at a relatively high flow rate to minimize lag time. The sample is divided at the analyzer, with the analyzer using the portion it requires (usually a very small fraction of the total sample), and the balance recycled to the process or vented.
If the sample filter is located in the low-flow line to the analyzer, it will have good life between filter element changes because the solids loading rate is very low; however, the filter must be carefully selected to avoid introducing unacceptable lag time.
If the filter is located in the high-flow portion of the sample system, its effect on sample lag time can be relatively low, but the life between filter changes may be inconveniently short because the element is filtering a much greater volume of material than the analyzer is using.
Ideally, a filter should be located at the point where the low-flow stream is withdrawn to the analyzer (see Figure 2). This arrangement permits the main volume of the filter to be swept continuously by the high flow rate system, thus minimizing lag time.
At the same time, only the low-flow stream to the analyzer is filtered, thus maximizing filter life. A slipstream filter requires inlet and outlet ports at opposite ends of the filter element to allow the high flow rate of the by-passed material to sweep the surface of the filter element and the filter reservoir, and a third port connected to the low flow rate line to the analyzer, which allows filtered samples to be withdrawn from the filter reservoir.
If bubble removal from a liquid is a requirement; this function may be combined with slipstream filtration, since the recommended flow direction for bubble removal is outside-to-inside, and the separated bubbles will be swept out of the housing by the bypass stream. In this case the liquid feed should enter at the bottom of the housing and the bypass liquid exit at the top of the housing. A special problem arises in slipstream
Figure 4: Stack gas sampling
Hydrophobic membrane sampling.
Many online instruments are susceptible to corrosion and skewed analysis from any water and moisture contamination. Gas chromatographs, mass spectrometers, oxygen analyzers and other sensitive on-line instruments require complete removal of all moisture.
Instrument sensitivity levels range from PPM to PPB and “percent level” component concentrations. As a result, it is good practice to install a hydrophobic membrane filter in line to the instrument to protect and safeguard it from any moisture contamination.
A stainless steel filter housing with a hydrophobic membrane allows the sample gas to flow on the upstream side of the membrane and exit through the outlet port on the downstream side (see Figure 6
Fig.6 - Stainless steel filter housing with a hydrophobic membrane
Slipstream or bypass filtration
Entrained moisture will not flow through the membrane and will exit out the by-pass port on the upstream side of the membrane completely protecting the instrument from moisture. If the sample gas contains excessive amounts of moisture and particulates it is recommended to use a stainless steel filter housing that incorporates a coalescing prefilter and the hydrophobic membrane (see Figure 7). The coalescing prefilter will protect the membrane from premature blinding and extend its useful life.
Fig.7 Stainless steel filter housing that incorporates a coalescing prefilter and the hydrophobic membrane
Minimal panel space, permanent line mount sampling. As more and more sample lines and instruments are added to instrument sheds, the need to utilize the space in the most efficient way has become critical. In addition, the need to maintain sample filters without having to “break” the sample line and expose it to ambient conditions has also become quite important to most facilities. By not having to “break” sample line the need to flush the lines prior to start up is eliminated.
For this application, it is recommended
a stainless steel filter designed to be
horizontally mounted at a 10 degree angle
be installed to minimize the amount of foot
print on the panel (see Figure 8).
Fig.8 Stainless steel filter designed to be horizontally mounted
This design incorporates the inlet ,outlet and drain ports all in the head of the filter enabling filter element change outs without disrupting the sample line.
Fig.8 Stainless steel filter designed to be horizontally mounted
This design incorporates the inlet ,outlet and drain ports all in the head of the filter enabling filter element change outs without disrupting the sample line.
Filtering Samples to On-Line Analyzers
©Copyright Parker Hannifin Corporation 2013 September 2013.