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| Energy Efficiency and Air Handling Units
TThe air handling unit (AHU) is a complicated device involving
many interrelated design selections that affect its energy efficiency.
The overall efficiency of an AHU is determined by the energy it
takes to move a given quantity of air against the system. Three
major energy choices for the AHU design must be considered..
Reducing AHU pressure drop
The AHU pressure drop can be reduced by:
Lowering face velocity
Lowering face velocities necessitates larger area coils
and filter elements and bigger AHU housings than conventionally
used. These larger items increase the AHU's cost, but a
resulting decrease in face velocity from 500 fpm to 400
fpm usually makes up for the increased cost over the life
of the AHU. Face velocity reductions from 500 fpm to 400
fpm can have a simple payback of about three years. A comparable
decrease in face velocity at filters can have a simple payback
of one year or less. [Brown, 1990]
Considering filter loading and VFDs
Variable system resistance, primarily resulting from filter
loading, can be efficiently corrected for with a VFD on
the fan. AHU pre-filter pressure drop will typically vary
from 0.5 in. H2O (125 Pa) when "clean" to 1.7
in H2O (423 Pa) when "dirty." The system design
point is usually sized for the "dirty" condition.
However, on average, about 90 percent of the design head
and energy is actually required. The energy saved by a VFD
will pay for the drive in two to five years, depending upon
system capacity. [Brown, 1990]
Adding bypass dampers
Some AHU components are only utilized during a portion of
the year; therefore, bypass dampers should be used to reduce
parasitic energy losses when these components are not needed.
[Brown, 1990]
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Ductwork System Effect
The heart of the HVAC system is the fan. Improper fan design
or installation can cause serious degradation of performance
because of "system effects." System effect factors
for connections between fan and duct system are presented
in "Fans and Systems" (AMCA, 1973), the ASHRAE Fundamentals
Handbook [ASHRAE, 1997], and the DFDB [ASHRAE, 1994]. System
effects cause changes in a fan's aerodynamic characteristics
that result in an entirely new fan performance curve. They
appear when inlet and outlet connections cause non-uniform
inlet and outlet flow and swirl at the fan inlet.
An engineer designing ductwork should provide uniform straight
flow conditions at the fan inlet and outlet. An elbow at
a fan's inlet causes turbulence and uneven flow into the
fan opening. An elbow at a fan's discharge causes a non-uniform
backpressure. An engineer can only estimate how much pressure
will be lost as a result of system effects by reviewing
the air distribution system design.
System effects are rarely measured during system start-up
procedures. They become evident only when not enough air
is delivered to the building. Start-up personnel must then
speed up the fan by changing pulleys or even increasing
the fan's motor size in order to get design air-flow rates.
System effects can be reduced or largely avoided by a few
easy precautions for centrifugal fans, as follows:
With a free inlet fan (no inlet duct), a minimum of one
half the fan wheel diameter, D, clearance should be maintained
from the inlet to the wall or structure.
An elbow entrance to the fan should be at least two times
the inlet diameter distance from the flex connector at the
fan, C=0.15 (remember, the fan entrance is a high-velocity
duct).
A 2D cone to the inlet flex (vibration isolator) should
be used to decrease friction losses (C=0.10).
If this 2D inlet cone is attached to a rectangular, vertical
duct, its dimensions should be two times the fan's inlet
diameter by one half the fan's inlet diameter and extend
one diameter past the center line of the fan's inlet (Figure
1).
A duct expansion from the fan discharge should be at a 10°
angle up on a top horizontal discharge fan (Figure 2). Down
angles and increases in the width of the duct are less efficient.
A straight duct for a distance of three to six duct diameters
from the fan discharge should be used in order to develop
a full dynamic head. Branching and turning sooner causes
system effect losses.
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Incorporating the most efficient fan "system"
The fan "system" includes the following:
Fan type
Centrifugal fan efficiencies range from 50 percent to about
70 percent depending upon blade configuration and vane-axial
fan efficiencies range from 80 percent to over 90 percent.
However, the energy engineer must keep in mind that all
fans add heat to the air stream. The air stream temperature
typically rises between three degrees F and six degrees
F for inefficient fan types. Also, actual installed efficiency
is typically worse than the manufacturer's rating data indicates,
dropping the fan's efficiency by 10 to 30 percent in some
cases.
Drive mechanism
Direct drive fan/motor combinations are the most efficient
at 100 percent. Standard V-belt drives are about 93 percent
efficient when first installed but drop over time. Synchronous
belt systems offer an energy-efficiency increase to about
96 percent for the life of the belt.
Motor efficiency
Premium efficiency motors that have full-load efficiencies
of greater than 94 percent depending upon horsepower are
preferable. It is also important to consider the part-load
motor efficiency and its operation with a VFD in VAV systems.
Sound Power Requirements
Acoustical attenuators, used to reduce a fan's sound, increase
the pressure drop of the AHU. Therefore, engineers should
consider the disadvantages of high-efficiency but noisy
fan that will require acoustical attenuation devices. These
devices can negate the energy savings from face velocity
reductions.
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Evaporative cooling
Evaporative cooling is an alternative to conventional compressor-type
cooling systems. Direct and indirect evaporation systems or
a combination can supplant or displace conventional cooling
systems. Evaporative cooling systems have been used to condition
facilities since before refrigerated cooling was invented.
There are two types of evaporative cooling techniques: indirect
and direct. The indirect approach removes sensible energy
only from the air stream with an exchanger that has the air
stream flow on one side of a plate and water on the other.
The direct approach removes energy from the air stream adiabatically
by adding moisture to the air stream. These approaches can
be combined to provide cooling and humidification that displaces
energy from a conventional compressor-type HVAC system. Annual
energy savings of more than 15 percent for a one-stage, direct
system and over 38 percent for a two-stage indirect/direct
system can be realized when compared to a conventional HVAC
system. Brown (1993) says, "The use of direct evaporative
cooling to humidify increases the opportunity to recover heat
by 36 percent and reduce energy consumption during the heating
season." One- to two-year paybacks are possible. The
justification of evaporative cooling should not be based solely
on the ability to replace mechanical cooling but should be
considered as an opportunity to displace mechanical cooling/humidification
energy. [Brown, 1992; Brown, 1993]
Evaporative cooling should always be considered for all
make-up air systems, regardless of geographic region, as
noted in the descriptions of the approaches below:
Indirect
Indirect evaporative cooling is applicable when there is
a large process equipment-cooling load, the HVAC system
operates on a continuous basis, and a direct evaporative
cooling opportunity exists. [Brown, 1993]
Direct
Direct evaporative cooling can be justified on the basis
of eliminating the need for a steam humidification system,
enhancing economizer operation, reducing humidification
energy used in conjunction with heat recovery, and controlling
the temperature of a space independent of controlling its
humidity. Direct evaporative cooling for both make-up air
and recirculation-type systems should always be considered
when the outdoor wet-bulb temperature is 53°F (11.7°C)
or less for 3,500 or more hours per year. Direct evaporative
cooling of air conditioning condensers, which are normally
simply air-cooled, can reduce electrical energy and demand
consumption by 20 to 40 percent. [Knebel, 1997] [Brown,
1990; Brown, 1993]
Two-stage
Typically, a two-stage evaporative cooling system comprises
a direct evaporative cooler downstream of an indirect evaporative
cooler. The two coolers can be combined in a myriad of arrangements
to increase energy efficiency
Economizers
When mixing of the facility's exhaust air with make-up fresh
air is permitted, economizers can save energy in both cooling
and heating modes.
Coil placement
Brown (1993) points out that placement of the fan upstream
from the cooling coil and evaporative cooler has two energy
advantages. In cooling mode, fan heat enhances operation
of the cooling coil, and, in heating mode, the same fan
heat is used to provide humidification energy and to displace
preheat energy input. [Brown, 1993]
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