Drying Your Compressed Air System Will Save Real
Money
Fluid Power
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The cost of replacement parts, labor, standby inventory, and
downtime can have a devastating effect on a plant's bottom
line. Eliminating even one of them by drying a system's compressed
air will offset the cost of installing and operating the equipment.
When pneumatic components wear or become corroded as a result
of moisture, they consume more compressed air - and lose energy
efficiency. When this wear or corrosion becomes great enough,
components must be repaired or replaced - increasing operating
expense.
Types Of Dryers
Dryers remove water vapor from the air, which lowers its dew
point - the temperature to which air can be cooled before water
vapor begins to condense. In broadest terms, there are four
basic types of industrial compressed air dryers: deliquescent,
regenerative desiccant, refrigeration, and membrane.
Deliquescent dryers contain a chemical desiccant which absorbs
moisture contained in the air, whether the moisture has already
condensed or is still a vapor. The desiccant is consumed in
the water-removal process and must be replenished periodically.
The solution that must be drained from these dryers contains
both liquid water and the deliquescent chemical, so disposal
may be a problem. Local environmental regulations should be
checked before disposal of this solution.
Deliquescent dryers reduce the dew point of the air 15° to
25° F below the inlet air temperature. If the incoming air
has a dew point of 90° F, it will leave a deliquescent dryer
with a dew point of about 65° F. Depending on operating conditions,
some deliquescent dryers can produce dew points as low as -40° F;
new deliquescent chemicals may produce even lower dew points.
Two important points: desiccant level should not be allowed
to fall below that recommended by the dryer manufacturer, and
inlet temperature should be limited to 100° F or less to prevent
excessive desiccant consumption.
Regenerative desiccant dryers remove water from air by adsorbing
it on the surface of a microscopically porous desiccant, usually
silica gel, activated alumina, or molecular sieve. The desiccant
does not react chemically with the water, so it need not be
replenished. However, it must be dried, or regenerated, periodically.
Heatless regenerative dryers use two identical chambers filled
with desiccant. As wet air moves up through one chamber, a
portion of the dry discharged air is diverted through the second
chamber at close to atmospheric pressure, reactivating its
desiccant. The moisture-laden purge air is vented to atmosphere.
Some time later, air flow through the chambers is reversed.
Standard industry dewpoint ratings for these dryers is -40° F
at pressure. By adjusting the flow rates and volume of purge
air, -100° F pressure dewpoints can be achieved. These dryers,
as with all desiccant dryers, should be supplied with oil-free
air. Oil will greatly reduce the life expectancy of the desiccant.
Heat regenerative dryers also use two identical chambers.
In this type, however, air flows through one chamber until
its desiccant has adsorbed all the moisture it can hold. Then
air flow is diverted to the second chamber. Internal heating
elements or an external source of heat (steam or electricity)
then dries the saturated desiccant in the first chamber. Because
desiccant's adsorption capacity decreases as temperature increases,
the dried desiccant bed must be cooled from the temperature
it reaches during regeneration before it can be used again.
The regeneration cycle in these dryers usually lasts several
hours - 75% heating and 25% cooling.
Regenerative desiccant dryers can produce pressure dew points
as low as -100° F. The type of desiccant used has a definite
effect on the final dew point.
Refrigeration dryers condense moisture from compressed air
by cooling the air in heat exchangers chilled by refrigerants.
These dryers produce dew points in a range from 35° to 50° F
at system operating pressure.
Most 20-scfm and larger refrigeration dryers reheat the cooled
air after it has been dried, usually by routing it through
heat exchangers in contact with the hot incoming air. Reheating
the cooled air prevents condensation from forming on the exterior
of air lines downstream from the dryer and also precools incoming
air.
Standard refrigerating dryers should not be used where ambient
temperature can drop below 40° F because lower temperature
can freeze condensate. This will block air passages and could
damage the dryer's evaporator. Dryers may be equipped with
heat tracing packages for operating in ambient temperatures
as low as 50° F.
Refrigeration dryers should not be operated in conditions
where the incoming air and ambient air heat load is 15 to 20%
of the rating - a 100-scfm rated dryer (100° F inlet and ambient)
can freeze up if operated at 20 scfm and 40° F.
Refrigeration Dryer Types
Refrigeration dryers can be further classified into three
types:
Tube-in-tube refrigeration dryers operate by cooling a mass
of aluminum granules or bronze ribbon that in turn cools the
compressed air. As the tube-to-tube refrigeration dryer cycles,
a thermometer in the granule mass senses its temperature. As
the temperature rises, a switch turns on the refrigeration
unit. When the temperature drops to a cut-off point, refrigeration
stops. These dryers are designed to produce dew points of 35° or
50° F.
Water-chiller refrigeration dryers use a mass of water for
cooling. An extra heat exchanger is needed to maintain chilled
water flow through the condenser, as well as a water pump.
Dew points can be between 40° and 50° F. Water-chiller dryers
cycle as they operate.
Direct-expansion refrigeration dryers use a refrigerant-to-air
cooling process to produce pressure dew points of 35° F below
standard operating conditions. (100° F temperature at compressor
inlet, 100 psig, 100° F ambient - from the NFPA standard).
No recovery period is necessary, so direct-expansion refrigeration
dryers run continuously. The cost difference between cycling
and continuous operation is difficult to calculate. The difference
in electrical power consumption between cycling and non-cycling
refrigerated dryers is outweighed by the value of continuous
operation of the plant's pneumatic equipment
Membrane-Type Dryers
Membrane-type dryers are gas-separation devices. They consist
of miniature membrane tubes made of plastic materials compounded
to allow water vapor to pass through when there is a vapor
pressure differential. They work as your lungs do, venting
water vapor each time you exhale.
Typically this membrane material is formed into bundles of
thousands of individual fibers from one end of the dryer to
the other. Water vapor escapes through the walls of the fiber
to a sweep chamber from where it is continually vented to atmosphere
as a gas. A fraction of the dried air is routed through the
sweep chamber to continuously purge and exhaust moisture vapor.
Industrial-grade membranes can be used for years to dry air
continuously. They respond spontaneously to any change in inlet
conditions. They perform at temperatures between 40° and 150° F
(ambient or inlet), and handle pressures from about 60 to 300
psig. They will deliver a consistent outlet dew-point reduction
anywhere between these extremes. The inlet flow rate and pressure
determine the outlet dew point suppression. In other words,
membrane air dryers deliver a consistent level of drying protection
that follows the rise or fall of the inlet dew point temperature,
and can easily be sized to follow the ISA recommended 20° F
pressure dew point suppression below ambient. Outlet pressure
dew points can also be selected as low as -50° F. Flow capacities
are relatively low, but modules can be installed in parallel
for higher flows.
Prefilters mounted immediately upstream from the membrane
dryer keep out liquids and solids to allow an almost unlimited
service life. Because water vapor passes right through the
membrane material, it does not accumulate there, so membranes
do not become saturated and never need to be regenerated. Membranes
have no moving parts to wear out. They are non-electric and
suitable for most hazardous locations. They require no RF shielding
or protection. They use no refrigerant gas or potentially dusty
desiccants.
They make no noise. And, they can be mounted in any orientation.
Their low-mass components are inherently vibration-resistant.
Because they are static, inert devices, they never need service
or adjustment and don't require monitoring devices. Made of
plastic and aluminum, they do not rust or corrode and don't
need painting. They have almost no pressurized volume, so most
pressure code restrictions do not apply.
Note: membrane gas separators will remove other gases too.
Some membrane-type compressed air dryers can reduce outlet
oxygen concentrations (or not permeate oxygen at all). Consult
the manufacturer to determine if membrane can be used for breathing
air.
Importance of Dew Point
As pointed out earlier, wet air adds to plant operating expenses
through the cost of:
- repair parts,
- repair labor,
- product damage, and
- production downtime.
The economic advantages of reducing or eliminating these
detriments of moisture build a strong case for installing
a dryer. Once
the decision to install a dryer has been reached, two questions
arise: how dry must the air be, and what type of dryer should
be used?
The most important criterion in choosing an air dryer is
the pressure dew point that it must produce. The required dew
point of an air system determines how dry the air must be and
to a great extent, which type of dryer to use. Dew point varies
with pressure. For example: the dew point conversion chart
at left shows that air at atmospheric pressure with a dew point
of -12° F has a pressure dew point of 35° F at 100 psig. Dryer
manufacturers may specify the dew point that a particular model
can attain at atmospheric pressure or at a typical system pressure,
such as 100 psig. If performance is specified at atmospheric
pressure, use a chart like ar right to find what the minimum
dew point will be at the system's operating pressure.
The required dew point varies with each application. If preventing
condensation in compressed air lines is the main concern, then
the lowest ambient temperature to which air lines will be exposed
will be the controlling factor. However, for some applications,
dew point requirements will be more stringent, possibly as
low as -100° F at line pressure. An example might be the air
used for spraying a powdery substance. Even the slightest trace
of moisture in such air could condense and cause particles
to stick together.
If all the compressed air will be used inside a building where
temperature is maintained at a stable level, then the required
dew point can be fixed within a few degrees. But if some or
all of the compressed air is subjected to outdoor temperature
variations, the required dew point can change from day to day,
or even hour to hour.
Do not be too aggressive by estimating an unjustifiable margin
for error. Stating a dew point much lower than that actually
required wastes money. A rule-of-thumb margin for error is
about 20° F maximum.
Extremely low dew points may be required at only a few isolated
locations. If this is the case, consider using individual small
heatless regenerative dryers at locations requiring pressure
dewpoints below 35° F. A less-expensive dryer to dry the air
to less-stringent requirements can then be installed for the
rest of the air system.
Evaluating Flow Capacity
An air dryer not only must dry compressed air to the required
dew point, but also must be able to handle the required air
flow without causing excessive pressure drop. Flow capacity
of a dryer depends on:
- operating pressure,
- inlet air temperature,
- ambient air or cooling water temperature, and
- required dew point.
When any of the above conditions changes, flow capacity of
the dryer also changes. Dryer manufacturers can supply performance
curves that show the relationship of their dryer's flow capacity
to these four factors. Evaluating characteristics of the different
types of dryers will help indicate which is best for a particular
application. This is where cost finally can be considered.
Purchase price of the dryer is only one factor to evaluate
when choosing an air dryer. A deliquescent chemical dryer,
for example, has a relatively low initial cost, but its chemical
must be replaced periodically, adding to the operating cost.
This cost is offset somewhat because the deliquescent chemical
dryer requires no external power source.
Other dryer types may cost more initially, but have lower
operating costs because they can run for long periods with
little or no maintenance required. It should be clear, then,
that cost analysis should be conducted based on manufacturers'
specifications as they relate to an individual application's
physical and economical requirements.
Installation and Maintenance
Location can affect how well an air dryer performs. The site
for an air-cooled dryer should be well ventilated, so heat
can be carried away, and readily accessible to aid maintenance.
The maximum ambient temperature for a refrigerated dryer is
about 100° to 120° F. Higher temperatures prevent the dryer
from exchanging heat with its surroundings and keep it from
operating properly. Dryers with water-cooled condensers can
tolerate higher ambient temperature because they transfer heat
to the cooling water instead of to the surrounding environment.
Refrigerant dryers, whether air- or water-cooled, should not
be exposed to ambient temperature below 32° F unless optional
low-ambient-temperature controls are installed.
If a deliquescent dryer is used in a central compressed-air
system, bypass piping should be installed around the dryer
to maintain air supply whenever the dryer is taken off line
to add desiccant. There should also be no set of operating
conditions that permit system pressure to drop low enough to
allow high, turbulent air flow through the dryer that might
carry chemicals into system air lines. It is important to shut
off the water in water-cooled aftercoolers when the air system
is shut down. A leak in the aftercooler could flood the deliquescent
dryer and fill downstream piping with desiccant, making all
pneumatic components inoperable.
Refrigeration and deliquescent dryers should be drained regularly,
depending on the volume of liquid accumulated. Most refrigeration
dryers have automatic drains, at least as an option.
It should be noted that dryers remove water vapor, while
filters remove liquid water. A good drying system always has
a filter with an automatic drain installed upstream from the
air dryer. Air dryers of all types are not stand-alone components.
The cost of adequate prefilters, both particulate and oil coalescing,
is a wise investment to protect the more expensive dryers.
Postfilters are necessary for several reasons. For refrigerated
dryers, a coalescing filter can catch any oil from a refrigerant
leak. For deliquescent dryers, a particulate filter downstream
will catch any carryover of the corrosive desiccant. For regenerative
dryers, a 0.5-µm postfilter is necessary to catch desiccant
dust, which is common to all adsorptive desiccants. |