The direct stage, shown in the figure below, consists of a
rigid media evaporative pad, with water recirculated from a
reservoir. The water is pumped from the reservoir to a water
distribution header, for water feed by gravity from above the
media. The evaporative pad provides the area for the adiabatic
saturation of the air. While the process provides a lower
dry-bulb temperature, the moisture content of the leaving air
is higher than the entering condition. The direct stage is
used for comfort cooling in a building where adding humidity
to the air can be tolerated.
Direct Stage Evaporative
Cooler
The thermodynamic process is a simultaneous heat and mass
transfer, or adiabatic cooling, and follows a constant
enthalpy line on the psychrometric chart, it is shown in the
figure below as a process from A to B. Since the deviation of
the constant wet-bulb line and the constant enthalpy line is
small, it is assumed that the wet-bulb temperature is constant
across the direct evaporative stage.
Psychrometric Chart – Constant
Enthalpy
If the direct evaporative process were 100% efficient, the
leaving dry-bulb temperature would equal the entering wet-bulb
temperature. The efficiency of the direct evaporative process
is less than 100% and by defining saturation efficiency (\(\varepsilon\) se) for the direct
stage or evaporative pad, the leaving dry-bulb temperature can
be expressed by the following equation.
The name of a schedule which defines when the evaporative
cooler is available. A schedule value of 0 indicates that the
evaporative cooler is off for that time period. A schedule
value greater than 0 indicates that the evaporative cooler can
operate during the time period. If this field is blank, the
schedule has values of 1 for all time periods.
The face area of the evaporative pad in m2. With
the area and mass flow rate, the air velocity is calculated
and is used to determine the saturation efficiency. This field
is autosizable.
This field is optional. It is used to describe where the
cooler obtains water used for evaporative cooling. If blank or
omitted, then the cooler will obtain water directly from the
mains. If the name of a WaterUse:Storage
object is used here, then the cooler will obtain its water
from that tank. If a tank is specified, the cooler will
attempt to obtain all the water it uses from the tank. However
if the tank cannot provide all the water the cooler needs,
then the cooler will still operate and obtain the rest of the
water it needs from the mains.
An IDF example showing how this object is:
EvaporativeCooler:Direct:CelDekPad,
Evaporative Cooler, !- Name
System Availability Schedule, !- Availability Schedule Name
0.6, !- Direct Pad Area {m2}
0.2, !- Direct Pad Depth {m}
225, !- Recirculating Water Pump Power Consumption {W}
Evap Cooler Inlet Node, !- Air Inlet Node Name
Supply Outlet Node; !- Air Outlet Node Name
The effectivenss, or saturation efficiency, is the
temperature change of the supply air divided by the difference
between the inlet air dry-bulb and wet-bulb temperatures. In
other words, it is a measure of the approach to the inlet air
wet-bulb temperature.
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when mains water is supplied to the
cooler.
This is the source of the water consumed. This output
variable appears when mains water is supplied to the
cooler.
Evaporative
Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when storage tank water is supplied to
the cooler.
Evaporative
Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that
could not accually be met by the storage tank. This output
variable appears when storage tank water is supplied to the
cooler.
Evaporative
Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the
evaporative cooler that could not accually be met by the
storage tank. This output variable appears when storage tank
water is supplied to the cooler.
This cooler is similar in principal to the EvaporativeCooler:Direct:CelDekPad.
The model differs in that it gives the user a simple way of
specify the cooler effectiveness. Using the ResearchSpecial
input object also allows the cooler to control the amount of
cooling based on node setpoints (controlled by
SetpointManagers). This avoid problems from over cooling when
conditions are such that loads are low and cooling power is
high. Water pump power is assumed to vary linearly when the
cooler is operating at less than full capacity.
The name of a schedule that defines when the evaporative
cooler is available. A schedule value of 0 indicates that the
evaporative cooler is off for that time period. A schedule
value greater than 0 indicates that the evaporative cooler can
operate during the time period. If this field is blank, the
schedule has values of 1 for all time periods.
This field specifies the effectiveness that is applied to
the wetbulb depression to determine the conditions leaving the
cooler. This model assumes that the effectiveness is
constant.
Field:
Recirculationg Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the
water pump that circulates water in Watts.
This field specifies the name of a node that will provide
system air temperature setpoint information. A separate
SetpointManager object should be setup to update this
node.
This field is optional. It is used to describe where the
cooler obtains water used for evaporative cooling. If blank or
omitted, then the cooler will obtain water directly from the
mains. If the name of a WaterUse:Storage
object is used here, then the cooler will obtain its water
from that tank. If a tank is specified, the cooler will
attempt to obtain all the water it uses from the tank.
However, if the tank cannot provide all the water the cooler
needs, then the cooler will still operate and obtain the rest
of the water it needs from the mains.
This field is optional and can be used to model additional
water consumed by the cooler from drift. Drift is water that
leaves the cooling media as droplets and does not evaporate
into the process air stream. For example, water may get blown
off the evaporative media by winds and escape the air system.
The value entered here is a simple fraction of the water
consumed by the cooler for normal process evaporation. The
amount of drift is this fraction times the water evaporated
for the normal cooling process. This field can be left blank
and then there will be no added water consumption from
drift.
This field is optional and can be used to model additional
water consumed by the cooler from blowdown. Blowdown is water
that is intentionally drained from the cooler’s sump to offset
the build up of solids in the water that would otherwise occur
because of evaporation. The value entered here is
dimensionless. It can be characterized as the ratio of solids
in the blowdown water to solids in the make up water. Typical
values are 3 to 5. The default is 3.0.
An example IDF entry is
EvaporativeCooler:Direct:ResearchSpecial,
Direct Evap Cooler, !- Name
ALWAYS_ON, !- Availability Schedule Name
0.7 , !- Cooler Effectiveness
30.0 , !- Recirculating Water Pump Power Consumption
OAIndRDD Evap Cooler- OADirect Evap CoolerNode , !- Air Inlet Node Name
OADirect Evap Cooler- OAMixing BoxNode, !- Air Outlet Node Name
OADirect Evap Cooler- OAMixing BoxNode, !- Sensor Node Name
, !- Water Supply Storage Tank Name
0.0, !- Drift Loss Fraction
3; !- Blowdown Concentration Ratio
The output variables that are available for this direct
evaporative cooler are shown below:
HVAC,Average, Evaporative Cooler Electric Power[W]
HVAC,Sum, Evaporative Cooler Electric Energy [J]
HVAC,Sum, Evaporative Cooler Water Volume[m3]
HVAC,Sum,Evaporative Cooler Mains Water Volume [m3]
HVAC,Sum,Evaporative Cooler Storage Tank Water Volume [m3]
HVAC,Sum,Evaporative Cooler Starved Water Volume [m3]
HVAC,Sum,Evaporative Cooler Starved Mains Water Volume [m3]
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when mains water is supplied to the
cooler.
This is the source of the water consumed. This output
variable appears when mains water is supplied to the
cooler.
Evaporative
Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when storage tank water is supplied to
the cooler.
Evaporative
Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that
could not accually be met by the storage tank. This output
variable appears when storage tank water is supplied to the
cooler.
Evaporative
Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the
evaporative cooler that could not accually be met by the
storage tank. This output variable appears when storage tank
water is supplied to the cooler.
The dry coil indirect evaporative cooler, shown in the
figure below, has a rigid media pad, similar to the direct
evaporative stage, where the adiabatic cooling takes place.
The secondary air leaves the rigid media pad and enters an air
to air heat exchanger where it cools the supply air flowing
through the heat exchanger tubes. The moist secondary air is
then exhausted to the environment. The secondary air stream
has its own fan and consists of a rigid media evaporative pad,
with water recirculated from a reservoir. The water is pumped
from the reservoir to a water distribution header, for water
feed by gravity from above the media. The evaporative pad
provides the area for the adiabatic saturation of the air.
Evaporative Cooler – Indirect
Dry Coil
The process that the secondary air goes through, A to C to
D, is shown by the dashed lines in the following figure.
Process A to C is adiabatic cooling in the rigid media pad.
Then the air enters the shell side of the heat exchanger and
is sensibly heated from C to D by the warm supply air passing
through the tube side. The secondary air inlet is modeled as a
separate stream of outdoor air and the user has the option of
defining the name of an outdoor air node.
Secondary Air Process –
Indirect Dry Coil Evap Cooler
The advantage of the dry coil heat exchanger is that the
heat exchanger does not have the evaporation taking place on
the outside of the tubes, thus no mineral deposits are left on
the heat exchange surface to reduce the efficiency of the heat
exchanger. The rigid media pads are designed to flush the
mineral deposits to the sump, so the saturation efficiency of
the pad stays relatively constant.
The name of a schedule which defines when the evaporative
cooler is available. A schedule value of 0 indicates that the
evaporative cooler is off for that time period. A schedule
value greater than 0 indicates that the evaporative cooler can
operate during the time period. If this field is blank, the
schedule has values of 1 for all time periods.
The face area of the evaporative pad in m2. With
the area and mass flow rate, the air velocity is calculated
and is used to determine the saturation efficiency on the
secondary side of the evaporative cooler. This field is
autosizable.
The depth of the evaporative pad in meters. The pad depth
is used to determine the saturation efficiency on the
secondary side of the evaporative cooler. This field is
autosizable.
Field:
Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the
evaporative cooler recirculating pump in Watts.
This value is the overall efficiency of the fan, i.e., the
ratio of the power delivered to the fluid to the electrical
input power. It is the product of the motor efficiency and the
impeller efficiency. The motor efficiency is the power
delivered to the shaft divided by the electrical power input
to the motor. The impeller efficiency is power delivered to
the fluid (air) divided by the shaft power. The power
delivered to the fluid is the mass flow rate of the air
multiplied by the pressure rise divided by the air density.
This input value must be between 0 and 1.
This field is optional. It is used to describe where the
cooler obtains water used for evaporative cooling. If blank or
omitted, then the cooler will obtain water directly from the
mains. If the name of a WaterUse:Storage
object is used here, then the cooler will obtain its water
from that tank. If a tank is specified, the cooler will
attempt to obtain all the water it uses from the tank. However
if the tank cannot provide all the water the cooler needs,
then the cooler will still operate and obtain the rest of the
water it needs from the mains.
This field is optional. It is used to explicitly define an
outdoor air node for the inlet for secondary air stream.
Defining an outdoor air node here allows using the
height-dependent model for outdoor air conditions.
And an IDF example showing how this object is
specified:
EvaporativeCooler:Indirect:CelDekPad,
IndirectEvapCooler1, !- Name
FanAndCoilAvailSched, !- Availability Schedule Name
0.6, !- Direct Pad Area {m2}
0.2, !- Direct Pad Depth {m}
225., !- Recirculating Water Pump Power Consumption {W}
1.0, !- Secondary Fan Flow Rate {m3/s}
0.7, !- Secondary Fan Total Efficiency
200.0, !- Secondary Fan Delta Pressure {Pa}
0.67, !- Indirect Heat Exchanger Effectiveness
EvapCoolerIndirectInletAirNode, !- Primary Air Inlet Node Name
EvapCoolerDirectInletAirNode, !- Primary Air Outlet Node Name
, !- Control Type
, !- Water Supply Storage Tank Name
Secondary side OA inlet node; !- Secondary Air Inlet Node Name
The dry evaporation saturation efficiency is the saturation
efficiency of the secondary or wet side air stream defined as
the temperature change of the supply air divided by the
difference between the outdoor dry-bulb and wet-bulb
temperatures. In other words, it is a measure of the approach
to the outdoor wet-bulb temperature.
Evaporative
Cooler Total Stage Effectiveness[LINK]
The total stage efficiency includes the sensible heat
exchanger effectiveness of the heat exchanger in the supply
air stream. It is the saturation efficiency multiplied by the
heat exchanger effectiveness.
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when mains water is supplied to the
cooler.
This is the source of the water consumed. This output
variable appears when mains water is supplied to the
cooler.
Evaporative
Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when storage tank water is supplied to
the cooler.
Evaporative
Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that
could not accually be met by the storage tank. This output
variable appears when storage tank water is supplied to the
cooler.
Evaporative
Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the
evaporative cooler that could not accually be met by the
storage tank. This output variable appears when storage tank
water is supplied to the cooler.
The wetted coil evaporative cooler shown in the figure
below, has water sprayed directly on the tubes of the heat
exchanger where latent cooling takes place. The vaporization
of the water on the outside of the heat exchanger tubes allows
the simultaneous heat and mass transfer which removes heat
from the supply air on the tube side. Then the moist secondary
air is exhausted. The secondary air stream has its own
fan.
Evaporative Cooler - Indirect
Wet Coil
The process that the secondary air goes through, A to C on
the following figure, is a path of simultaneous heat and mass
transfer, but it does not follow a line of constant enthalpy
as in the direct stage. The process is not adiabatic due to
the heat gain from the supply air flowing through the tubes of
the heat exchanger.
Secondary Air Process -
Indirect Wet Coil Evap Cooler
The wet coil heat exchanger can have a higher stage
efficiency than the dry coil due to a higher heat transfer
rate on the outside of the heat exchanger tubes. Over the
operating lifetime of the heat exchanger, the vaporization
taking place on the heat exchange surface can leave mineral
deposits which will decrease the effectiveness of the heat
exchanger.
The name of a schedule which defines when the evaporative
cooler is available. A schedule value of 0 indicates that the
evaporative cooler is off for that time period. A schedule
value greater than 0 indicates that the evaporative cooler can
operate during the time period. If this field is blank, the
schedule has values of 1 for all time periods.
The maximum efficiency of the stage is a combination of the
efficiency due to the simultaneous heat and mass transfer on
the outside of the tube and the efficiency of the heat
exchanger. This value can be higher than the dry coil overall
efficiency since the convective coefficients on the outside of
the tube are larger.
The Coil Flow Ratio is determined from performance data.
The Coil Flow Ratio tells how quickly the efficiency of the
stage would decrease with a mismatch of the supply and
secondary flows.
Field:
Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the
evaporative cooler recirculating pump in Watts.
This value is the overall efficiency of the fan, i.e., the
ratio of the power delivered to the fluid to the electrical
input power. It is the product of the motor efficiency and the
impeller efficiency. The motor efficiency is the power
delivered to the shaft divided by the electrical power input
to the motor. The impeller efficiency is power delivered to
the fluid (air) divided by the shaft power. The power
delivered to the fluid is the mass flow rate of the air
multiplied by the pressure rise divided by the air density.
This input value must be between 0 and 1..
This field is optional. It is used to describe where the
cooler obtains water used for evaporative cooling. If blank or
omitted, then the cooler will obtain water directly from the
mains. If the name of a WaterUse:Storage
object is used here, then the cooler will obtain its water
from that tank. If a tank is specified, the cooler will
attempt to obtain all the water it uses from the tank. However
if the tank cannot provide all the water the cooler needs,
then the cooler will still operate and obtain the rest of the
water it needs from the mains.
This field is optional. It is used to explicitly define an
outdoor air node for the inlet for secondary air stream.
Defining an outdoor air node here allows using the
height-dependent model for outdoor air conditions.
This field is optional and can be used to model additional
water consumed by the cooler from drift. Drift is water that
leaves the cooling media as droplets and does not evaporate
into the process air stream. For example, water may get blown
off the evaporative media by winds and escape the air system.
The value entered here is a simple fraction of the water
consumed by the cooler for normal process evaporation. The
amount of drift is this fraction times the water evaporated
for the normal cooling process. This field can be left blank
and then there will be no added water consumption from
drift.
This field is optional and can be used to model additional
water consumed by the cooler from blowdown. Blowdown is water
that is intentionally drained from the cooler’s sump to offset
the build up of solids in the water that would otherwise occur
because of evaporation. The value entered here is
dimensionless. It can be characterized as the ratio of solids
in the blowdown water to solids in the make up water. Typical
values are 3 to 5. The default is 3.0.
And an IDF example showing how this object is
specified:
EvaporativeCooler:Indirect:WetCoil,
IndirectEvapCooler1, !- Name
FanAndCoilAvailSched, !- Availability Schedule Name
0.8, !- Coil Maximum Efficiency
0.16, !- Coil Flow Ratio
225., !- Recirculating Water Pump Power Consumption {W}
1.0, !- Secondary Fan Flow Rate {m3/s}
0.7, !- Secondary Fan Total Efficiency
200.0, !- Secondary Fan Delta Pressure {Pa}
EvapCoolerIndirectInletAirNode, !- Primary Air Inlet Node Name
EvapCoolerDirectInletAirNode, !- Primary Air Outlet Node Name
, !- Control Type
, !- Water Supply Storage Tank Name
Secondary side OA inlet node; !- Secondary Air Inlet Node Name
The output variables that are available for the wet
indirect evaporative cooler are shown below:
HVAC,Average, Evaporative Cooler Total Stage Effectiveness
HVAC,Average, Evaporative Cooler Electric Power[W]
HVAC,Sum, Evaporative Cooler Electric Energy [J]
HVAC,Sum, Evaporative Cooler Water Volume[m3]
HVAC,Sum,Evaporative Cooler Mains Water Volume [m3]
HVAC,Sum,Evaporative Cooler Storage Tank Water Volume [m3]
HVAC,Sum,Evaporative Cooler Starved Water Volume [m3]
HVAC,Sum,Evaporative Cooler Starved Mains Water Volume [m3]
Evaporative
Cooler Total Stage Effectiveness [][LINK]
The Total Stage Efficiency is defined as the temperature
change of the supply air divided by the difference between the
outdoor dry-bulb and wet-bulb temperatures, including the
effect of the reduction in flow because of the secondary air
stream. In other words, it is a measure of the approach to the
outdoor wet-bulb temperature.
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when mains water is supplied to the
cooler.
This is the source of the water consumed. This output
variable appears when mains water is supplied to the
cooler.
Evaporative
Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when storage tank water is supplied to
the cooler.
Evaporative
Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that
could not accually be met by the storage tank. This output
variable appears when storage tank water is supplied to the
cooler.
Evaporative
Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the
evaporative cooler that could not accually be met by the
storage tank. This output variable appears when storage tank
water is supplied to the cooler.
This cooler is similar in principal to the EvaporativeCooler:Indirect:CelDekPad
and EvaporativeCooler:Indirect:WetCoil
(see Figure 147, Figure 148, and Figure 149). The model
differs in that it gives the user more flexibility to specify
the source of secondary air. The cooler effectiveness with
respect to wetbulb depression is allowed to go beyond 1.0.
Using the ResearchSpecial input object also allows the cooler
to control the amount of cooling based on node setpoints
(controlled by SetpointManagers). This avoid problems from
over cooling when conditions are such that loads are low and
cooling power is high. Fan power is assumed to vary linearly
when the cooler is operating at less than full capacity.
The name of a schedule that defines when the evaporative
cooler is available. A schedule value of 0 indicates that the
evaporative cooler is off for that time period. A schedule
value greater than 0 indicates that the evaporative cooler can
operate during the time period. If this field is blank, the
schedule has values of 1 for all time periods.
This field specifies the maximum effectiveness that is
applied to the wetbulb depression to determine the conditions
leaving the cooler. This effectiveness is a complicated
function of the efficiency with which heat and mass are
transferred on the secondary side and the efficiency of heat
exchange between the secondary and primary flows. The model
assumes that the effectiveness is constant.
Field:
Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the
water pump that circulates water in Watts. The pump power and
energy consumption is reduced by cycling when the amount of
cooling needs to be restricted for control purposes.
This field is used to specify the secondary fan flow rate
and is specified in m3/s. This flow rate would
typically be similar in magnitude to the flow through the
primary side. This field can be autosized. When it is
autosized, the program detects if the component is in the main
air loop or on an outdoor air path. If it is on the main air
loop, then the flow rate is set to the AirLoopHVAC
system’s design supply air flow rate (which is the maximum
required for heating and cooling). If it is on the outdoor air
path, then the flow rate is set to the larger of either the
design minimum outdoor air flow rate or one-half of the main
air loop design flow rate. The flow rate is used to determine
parasitic fan energy and does not impact the modeling of
cooler effectiveness. The flow rate (and fan power) is
effectively reduced by cycling when the amount of cooling
needs to be restricted for control purposes.
This value is the overall efficiency of the fan, i.e., the
ratio of the power delivered to the fluid to the electrical
input power. It is the product of the motor efficiency and the
impeller efficiency. The motor efficiency is the power
delivered to the shaft divided by the electrical power input
to the motor. The impeller efficiency is power delivered to
the fluid (air) divided by the shaft power. The power
delivered to the fluid is the mass flow rate of the air
multiplied by the pressure rise divided by the air density.
This input value must be between 0 and 1.
This field specifies an effectiveness that is applied to
the dewpoint depression to determine a bound for the
conditions leaving the cooler. The model uses the warmer of
the two temperatures determined from wetbulb depression and
dewpoint depression.
This field specifies the name of the node providing air to
the secondary/wet side of the cooler. Typically this node
could appear in an outdoor air node list or be part of an air
system loop.
This field specifies the name of a node that will provide
system air temperature setpoint information. A separate
SetpointManager object should be setup to update this
node.
This field is optional, but can be used to feed two sources
of secondary air into the wet side of the cooler. Typical use
is to run the air system relief air into the system. The model
first uses all of the air flow available from this node and
then adds the air flow from the secondary air inlet node to
make up the total defined by Secondary Fan Flow Rate.
This field is optional. It is used to describe where the
cooler obtains water used for evaporative cooling. If blank or
omitted, then the cooler will obtain water directly from the
mains. If the name of a WaterUse:Storage
object is used here, then the cooler will obtain its water
from that tank. If a tank is specified, the cooler will
attempt to obtain all the water it uses from the tank.
However, if the tank cannot provide all the water the cooler
needs, then the cooler will still operate and obtain the rest
of the water it needs from the mains.
This field is optional and can be used to model additional
water consumed by the cooler from drift. Drift is water that
leaves the cooling media as droplets and does not evaporate
into the process air stream. For example, water may get blown
off the evaporative media by winds and escape the air system.
The value entered here is a simple fraction of the water
consumed by the cooler for normal process evaporation. The
amount of drift is this fraction times the water evaporated
for the normal cooling process. This field can be left blank
and then there will be no added water consumption from
drift.
This field is optional and can be used to model additional
water consumed by the cooler from blowdown. Blowdown is water
that is intentionally drained from the cooler’s sump to offset
the build up of solids in the water that would otherwise occur
because of evaporation. The value entered here is
dimensionless. It can be characterized as the ratio of solids
in the blowdown water to solids in the make up water. Typical
values are 3 to 5. The default is 3.0.
An IDF example is shown below:
EvaporativeCooler:Indirect:ResearchSpecial,
Indirect Evap ZN1, !- Name
On_Except_Winter_Night, !- Availability Schedule Name
1.2, !- Cooler Maximum Effectiveness
, !- Cooler Flow Ratio
30, !- Recirculating Water Pump Power Consumption {W}
autosize, !- Secondary Fan Flow Rate {m3/s}
0.7, !- Secondary Fan Total Efficiency
300, !- Secondary Fan Delta Pressure {Pa}
Mixed Air Node ZN1, !- Primary Air Inlet Node Name
Evap Cooler Outlet Node ZN1, !- Primary Air Outlet Node Name
, !- Control Type
0.9, !- Dewpoint Effectiveness Factor
Purge Air Inlet ZN1, !- Secondary Air Inlet Node Name
Air Loop Outlet Node ZN1,!- Sensor Node Name
Relief Air Outlet Node ZN1; !- Relief Air Inlet Node Name
HVAC,Average,Evaporative Cooler Total Stage Effectiveness
HVAC,Average,Evaporative Cooler Part Load Ratio
HVAC,Average,Evaporative Cooler Dewpoint Bound Status
HVAC,Sum,Evaporative Cooler Electric Energy [J]
HVAC,Average,Evaporative Cooler Electric Power [W]
HVAC,Sum,Evaporative Cooler Storage Tank Water Volume [m3]
HVAC,Sum,Evaporative Cooler Starved Water Volume [m3]
HVAC,Sum,Evaporative Cooler Starved Mains Water Volume [m3]
Evaporative
Cooler Total Stage Effectiveness [][LINK]
The Total Stage Efficiency is defined as the temperature
change of the supply air divided by the difference between the
outdoor dry-bulb and wet-bulb temperatures, including the
effect of the reduction in flow because of the secondary air
stream. In other words, it is a measure of the approach to the
outdoor wet-bulb temperature.
This output variable provides the part load fraction of the
indirect cooler. The ResearchSpecial cooler model is able to
modulate to meet a temperature set point to avoid over
cooling. This output variable is the fraction formed by the
ratio of the capacity needed over the maximum cooling capacity
available. A value of 1.0 corresponds to full capacity
cooling.
This output variable is a flag that indicates if the
modeling was based on dewpoint effectivenss rather than
wetbulb effectiveness The ResearchSpecial model is usually
based on wet-bulb approach, but since values in excess of 1.0
are allowed, there is a secondary constraint imposed by
dewpoint. If the dewpoint effectiveness was applied, then this
flag variable will have the value 1.0, otherwise it is
0.0.
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when mains water is supplied to the
cooler.
This is the source of the water consumed. This output
variable appears when mains water is supplied to the
cooler.
Evaporative
Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad.
This water consumption is only from the direct thermodynamics
of water evaporation and does not include other sources of
consumption such as drift or concentration blow down. This
output variable appears when storage tank water is supplied to
the cooler.
Evaporative
Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that
could not accually be met by the storage tank. This output
variable appears when storage tank water is supplied to the
cooler.
Evaporative
Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the
evaporative cooler that could not accually be met by the
storage tank. This output variable appears when storage tank
water is supplied to the cooler.
Group - Evaporative Coolers[LINK]
This group of objects describes the properties and configuration for the evaporative coolers models for the HVAC section.
EvaporativeCooler:Direct:CelDekPad[LINK]
The direct stage, shown in the figure below, consists of a rigid media evaporative pad, with water recirculated from a reservoir. The water is pumped from the reservoir to a water distribution header, for water feed by gravity from above the media. The evaporative pad provides the area for the adiabatic saturation of the air. While the process provides a lower dry-bulb temperature, the moisture content of the leaving air is higher than the entering condition. The direct stage is used for comfort cooling in a building where adding humidity to the air can be tolerated.
The thermodynamic process is a simultaneous heat and mass transfer, or adiabatic cooling, and follows a constant enthalpy line on the psychrometric chart, it is shown in the figure below as a process from A to B. Since the deviation of the constant wet-bulb line and the constant enthalpy line is small, it is assumed that the wet-bulb temperature is constant across the direct evaporative stage.
If the direct evaporative process were 100% efficient, the leaving dry-bulb temperature would equal the entering wet-bulb temperature. The efficiency of the direct evaporative process is less than 100% and by defining saturation efficiency (\(\varepsilon\) se) for the direct stage or evaporative pad, the leaving dry-bulb temperature can be expressed by the following equation.
Inputs[LINK]
Field: Name[LINK]
A unique identifying name for each evaporative cooler.
Field: Availability Schedule Name[LINK]
The name of a schedule which defines when the evaporative cooler is available. A schedule value of 0 indicates that the evaporative cooler is off for that time period. A schedule value greater than 0 indicates that the evaporative cooler can operate during the time period. If this field is blank, the schedule has values of 1 for all time periods.
Field: Direct Pad Area[LINK]
The face area of the evaporative pad in m2. With the area and mass flow rate, the air velocity is calculated and is used to determine the saturation efficiency. This field is autosizable.
Field: Direct Pad Depth[LINK]
The depth of the evaporative pad in meters. The pad depth is used to determine the saturation efficiency. This field is autosizable.
Field: Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the evaporative cooler recirculating pump in Watts.
Field: Air Inlet Node Name[LINK]
The name of the evaporative cooler air inlet node from the Air Loop Simulation.
Field: Air Outlet Node Name[LINK]
The name of the evaporative cooler air outlet node from the Air Loop Simulation.
Field: Control Type[LINK]
This input field is currently unused and can be left blank.
Field: Water Supply Storage Tank Name[LINK]
This field is optional. It is used to describe where the cooler obtains water used for evaporative cooling. If blank or omitted, then the cooler will obtain water directly from the mains. If the name of a WaterUse:Storage object is used here, then the cooler will obtain its water from that tank. If a tank is specified, the cooler will attempt to obtain all the water it uses from the tank. However if the tank cannot provide all the water the cooler needs, then the cooler will still operate and obtain the rest of the water it needs from the mains.
An IDF example showing how this object is:
Outputs[LINK]
The output variables that are available for this direct evaporative cooler are shown below:
Evaporative Cooler Wet Bulb Effectiveness[LINK]
The effectivenss, or saturation efficiency, is the temperature change of the supply air divided by the difference between the inlet air dry-bulb and wet-bulb temperatures. In other words, it is a measure of the approach to the inlet air wet-bulb temperature.
Evaporative Cooler Electric Power[W][LINK]
Evaporative Cooler Electric Energy [J][LINK]
These output variables report the electric power and electric energy required to operate the water pump.
Evaporative Cooler Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Mains Water Volume [m3][LINK]
This is the source of the water consumed. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
EvaporativeCooler:Direct:ResearchSpecial[LINK]
This cooler is similar in principal to the EvaporativeCooler:Direct:CelDekPad. The model differs in that it gives the user a simple way of specify the cooler effectiveness. Using the ResearchSpecial input object also allows the cooler to control the amount of cooling based on node setpoints (controlled by SetpointManagers). This avoid problems from over cooling when conditions are such that loads are low and cooling power is high. Water pump power is assumed to vary linearly when the cooler is operating at less than full capacity.
Inputs[LINK]
Field: Name[LINK]
A unique identifying name for each cooler.
Field: Availability Schedule Name[LINK]
The name of a schedule that defines when the evaporative cooler is available. A schedule value of 0 indicates that the evaporative cooler is off for that time period. A schedule value greater than 0 indicates that the evaporative cooler can operate during the time period. If this field is blank, the schedule has values of 1 for all time periods.
Field: Cooler Effectiveness[LINK]
This field specifies the effectiveness that is applied to the wetbulb depression to determine the conditions leaving the cooler. This model assumes that the effectiveness is constant.
Field: Recirculationg Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the water pump that circulates water in Watts.
Field: Air Inlet Node Name[LINK]
The name of the air inlet node for the primary air flow path through the cooler.
Field: Air Outlet Node Name[LINK]
The name of the air outlet node for the primary air flow path through the cooler.
Field: Sensor Node Name[LINK]
This field specifies the name of a node that will provide system air temperature setpoint information. A separate SetpointManager object should be setup to update this node.
Field: Water Supply Storage Tank Name[LINK]
This field is optional. It is used to describe where the cooler obtains water used for evaporative cooling. If blank or omitted, then the cooler will obtain water directly from the mains. If the name of a WaterUse:Storage object is used here, then the cooler will obtain its water from that tank. If a tank is specified, the cooler will attempt to obtain all the water it uses from the tank. However, if the tank cannot provide all the water the cooler needs, then the cooler will still operate and obtain the rest of the water it needs from the mains.
Field: Drift Loss Fraction[LINK]
This field is optional and can be used to model additional water consumed by the cooler from drift. Drift is water that leaves the cooling media as droplets and does not evaporate into the process air stream. For example, water may get blown off the evaporative media by winds and escape the air system. The value entered here is a simple fraction of the water consumed by the cooler for normal process evaporation. The amount of drift is this fraction times the water evaporated for the normal cooling process. This field can be left blank and then there will be no added water consumption from drift.
Field: Blowdown Concentration Ratio[LINK]
This field is optional and can be used to model additional water consumed by the cooler from blowdown. Blowdown is water that is intentionally drained from the cooler’s sump to offset the build up of solids in the water that would otherwise occur because of evaporation. The value entered here is dimensionless. It can be characterized as the ratio of solids in the blowdown water to solids in the make up water. Typical values are 3 to 5. The default is 3.0.
An example IDF entry is
Outputs[LINK]
The output variables that are available for this direct evaporative cooler are shown below:
Evaporative Cooler Electric Power[W][LINK]
Evaporative Cooler Electric Energy [J][LINK]
These output variables report the electric power and electric energy required to operate the water pump.
Evaporative Cooler Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Mains Water Volume [m3][LINK]
This is the source of the water consumed. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
EvaporativeCooler:Indirect:CelDekPad[LINK]
The dry coil indirect evaporative cooler, shown in the figure below, has a rigid media pad, similar to the direct evaporative stage, where the adiabatic cooling takes place. The secondary air leaves the rigid media pad and enters an air to air heat exchanger where it cools the supply air flowing through the heat exchanger tubes. The moist secondary air is then exhausted to the environment. The secondary air stream has its own fan and consists of a rigid media evaporative pad, with water recirculated from a reservoir. The water is pumped from the reservoir to a water distribution header, for water feed by gravity from above the media. The evaporative pad provides the area for the adiabatic saturation of the air.
The process that the secondary air goes through, A to C to D, is shown by the dashed lines in the following figure. Process A to C is adiabatic cooling in the rigid media pad. Then the air enters the shell side of the heat exchanger and is sensibly heated from C to D by the warm supply air passing through the tube side. The secondary air inlet is modeled as a separate stream of outdoor air and the user has the option of defining the name of an outdoor air node.
The advantage of the dry coil heat exchanger is that the heat exchanger does not have the evaporation taking place on the outside of the tubes, thus no mineral deposits are left on the heat exchange surface to reduce the efficiency of the heat exchanger. The rigid media pads are designed to flush the mineral deposits to the sump, so the saturation efficiency of the pad stays relatively constant.
Inputs[LINK]
Field: Name[LINK]
A unique identifying name for each evaporative cooler.
Field: Availability Schedule Name[LINK]
The name of a schedule which defines when the evaporative cooler is available. A schedule value of 0 indicates that the evaporative cooler is off for that time period. A schedule value greater than 0 indicates that the evaporative cooler can operate during the time period. If this field is blank, the schedule has values of 1 for all time periods.
Field: Direct Pad Area[LINK]
The face area of the evaporative pad in m2. With the area and mass flow rate, the air velocity is calculated and is used to determine the saturation efficiency on the secondary side of the evaporative cooler. This field is autosizable.
Field: Direct Pad Depth[LINK]
The depth of the evaporative pad in meters. The pad depth is used to determine the saturation efficiency on the secondary side of the evaporative cooler. This field is autosizable.
Field: Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the evaporative cooler recirculating pump in Watts.
Field: Secondary Fan Flow Rate[LINK]
This field is used to specify the secondary fan flow rate and is specified in m3/sec.
Field: Secondary Fan Total Efficiency[LINK]
This value is the overall efficiency of the fan, i.e., the ratio of the power delivered to the fluid to the electrical input power. It is the product of the motor efficiency and the impeller efficiency. The motor efficiency is the power delivered to the shaft divided by the electrical power input to the motor. The impeller efficiency is power delivered to the fluid (air) divided by the shaft power. The power delivered to the fluid is the mass flow rate of the air multiplied by the pressure rise divided by the air density. This input value must be between 0 and 1.
Field: Secondary Fan Delta Pressure[LINK]
This field is used to specify the delta pressure across the secondary stage of the evaporative cooler in Pascals.
Field: Indirect Heat Exchanger Effectiveness[LINK]
This field is used to specify the effectiveness of the indirect heat exchanger between the primary and secondary air flow.
Field: Primary Air Inlet Node Name[LINK]
The name of the evaporative cooler’s primary air inlet node from the Air Loop Simulation. This is the air flow being cooled indirectly.
Field: Primary Air Outlet Node Name[LINK]
The name of the evaporative cooler’s primary air outlet node from the Air Loop Simulation.
Field: Control Type[LINK]
This input field is currently unused and can be left blank.
Field: Water Supply Storage Tank Name[LINK]
This field is optional. It is used to describe where the cooler obtains water used for evaporative cooling. If blank or omitted, then the cooler will obtain water directly from the mains. If the name of a WaterUse:Storage object is used here, then the cooler will obtain its water from that tank. If a tank is specified, the cooler will attempt to obtain all the water it uses from the tank. However if the tank cannot provide all the water the cooler needs, then the cooler will still operate and obtain the rest of the water it needs from the mains.
Field: Secondary Air Inlet Node Name[LINK]
This field is optional. It is used to explicitly define an outdoor air node for the inlet for secondary air stream. Defining an outdoor air node here allows using the height-dependent model for outdoor air conditions.
And an IDF example showing how this object is specified:
Outputs[LINK]
The output variables that are available for the indirect dry evaporative cooler are shown below:
Evaporative Cooler Wetbulb Effectiveness[LINK]
The dry evaporation saturation efficiency is the saturation efficiency of the secondary or wet side air stream defined as the temperature change of the supply air divided by the difference between the outdoor dry-bulb and wet-bulb temperatures. In other words, it is a measure of the approach to the outdoor wet-bulb temperature.
Evaporative Cooler Total Stage Effectiveness[LINK]
The total stage efficiency includes the sensible heat exchanger effectiveness of the heat exchanger in the supply air stream. It is the saturation efficiency multiplied by the heat exchanger effectiveness.
Evaporative Cooler Electric Power[W][LINK]
Evaporative Cooler Electric Energy [J][LINK]
These output variables report the electric power and energy consumed by the secondary air fan and the sump pump.
Evaporative Cooler Water Volume[m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Mains Water Volume [m3][LINK]
This is the source of the water consumed. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
EvaporativeCooler:Indirect:WetCoil[LINK]
The wetted coil evaporative cooler shown in the figure below, has water sprayed directly on the tubes of the heat exchanger where latent cooling takes place. The vaporization of the water on the outside of the heat exchanger tubes allows the simultaneous heat and mass transfer which removes heat from the supply air on the tube side. Then the moist secondary air is exhausted. The secondary air stream has its own fan.
The process that the secondary air goes through, A to C on the following figure, is a path of simultaneous heat and mass transfer, but it does not follow a line of constant enthalpy as in the direct stage. The process is not adiabatic due to the heat gain from the supply air flowing through the tubes of the heat exchanger.
The wet coil heat exchanger can have a higher stage efficiency than the dry coil due to a higher heat transfer rate on the outside of the heat exchanger tubes. Over the operating lifetime of the heat exchanger, the vaporization taking place on the heat exchange surface can leave mineral deposits which will decrease the effectiveness of the heat exchanger.
Inputs[LINK]
Field: Name[LINK]
A unique identifying name for each evaporative cooler.
Field: Availability Schedule Name[LINK]
The name of a schedule which defines when the evaporative cooler is available. A schedule value of 0 indicates that the evaporative cooler is off for that time period. A schedule value greater than 0 indicates that the evaporative cooler can operate during the time period. If this field is blank, the schedule has values of 1 for all time periods.
Field: Coil Maximum Efficiency[LINK]
The maximum efficiency of the stage is a combination of the efficiency due to the simultaneous heat and mass transfer on the outside of the tube and the efficiency of the heat exchanger. This value can be higher than the dry coil overall efficiency since the convective coefficients on the outside of the tube are larger.
Field: Coil Flow Ratio[LINK]
The Coil Flow Ratio is determined from performance data. The Coil Flow Ratio tells how quickly the efficiency of the stage would decrease with a mismatch of the supply and secondary flows.
Field: Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the evaporative cooler recirculating pump in Watts.
Field: Secondary Fan Flow Rate[LINK]
This field is used to specify the secondary fan flow rate and is specified in m3/sec.
Field: Secondary Fan Total Efficiency[LINK]
This value is the overall efficiency of the fan, i.e., the ratio of the power delivered to the fluid to the electrical input power. It is the product of the motor efficiency and the impeller efficiency. The motor efficiency is the power delivered to the shaft divided by the electrical power input to the motor. The impeller efficiency is power delivered to the fluid (air) divided by the shaft power. The power delivered to the fluid is the mass flow rate of the air multiplied by the pressure rise divided by the air density. This input value must be between 0 and 1..
Field: Secondary Fan Delta Pressure[LINK]
This field is used to specify the delta pressure across the secondary stage of the evaporative cooler in Pascals.
Field: Primary Air Inlet Node Name[LINK]
The name of the evaporative cooler air inlet from the Air Loop Simulation.
Field: Primary Air Outlet Node Name[LINK]
The name of the evaporative cooler air outlet from the Air Loop Simulation.
Field: Control Type[LINK]
This input field is currently unused and can be left blank.
Field: Water Supply Storage Tank Name[LINK]
This field is optional. It is used to describe where the cooler obtains water used for evaporative cooling. If blank or omitted, then the cooler will obtain water directly from the mains. If the name of a WaterUse:Storage object is used here, then the cooler will obtain its water from that tank. If a tank is specified, the cooler will attempt to obtain all the water it uses from the tank. However if the tank cannot provide all the water the cooler needs, then the cooler will still operate and obtain the rest of the water it needs from the mains.
Field: Secondary Air Inlet Node Name[LINK]
This field is optional. It is used to explicitly define an outdoor air node for the inlet for secondary air stream. Defining an outdoor air node here allows using the height-dependent model for outdoor air conditions.
Field: Drift Loss Fraction[LINK]
This field is optional and can be used to model additional water consumed by the cooler from drift. Drift is water that leaves the cooling media as droplets and does not evaporate into the process air stream. For example, water may get blown off the evaporative media by winds and escape the air system. The value entered here is a simple fraction of the water consumed by the cooler for normal process evaporation. The amount of drift is this fraction times the water evaporated for the normal cooling process. This field can be left blank and then there will be no added water consumption from drift.
Field: Blowdown Concentration Ratio[LINK]
This field is optional and can be used to model additional water consumed by the cooler from blowdown. Blowdown is water that is intentionally drained from the cooler’s sump to offset the build up of solids in the water that would otherwise occur because of evaporation. The value entered here is dimensionless. It can be characterized as the ratio of solids in the blowdown water to solids in the make up water. Typical values are 3 to 5. The default is 3.0.
And an IDF example showing how this object is specified:
Outputs[LINK]
The output variables that are available for the wet indirect evaporative cooler are shown below:
Evaporative Cooler Total Stage Effectiveness [][LINK]
The Total Stage Efficiency is defined as the temperature change of the supply air divided by the difference between the outdoor dry-bulb and wet-bulb temperatures, including the effect of the reduction in flow because of the secondary air stream. In other words, it is a measure of the approach to the outdoor wet-bulb temperature.
Evaporative Cooler Electric Power [W][LINK]
Evaporative Cooler Electric Energy [J][LINK]
These output variables report the electric power and energy that are consumed by the secondary air fan and the sump pump.
Evaporative Cooler Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Mains Water Volume [m3][LINK]
This is the source of the water consumed. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
EvaporativeCooler:Indirect:ResearchSpecial[LINK]
This cooler is similar in principal to the EvaporativeCooler:Indirect:CelDekPad and EvaporativeCooler:Indirect:WetCoil (see Figure 147, Figure 148, and Figure 149). The model differs in that it gives the user more flexibility to specify the source of secondary air. The cooler effectiveness with respect to wetbulb depression is allowed to go beyond 1.0. Using the ResearchSpecial input object also allows the cooler to control the amount of cooling based on node setpoints (controlled by SetpointManagers). This avoid problems from over cooling when conditions are such that loads are low and cooling power is high. Fan power is assumed to vary linearly when the cooler is operating at less than full capacity.
Inputs[LINK]
Field: Name[LINK]
A unique identifying name for each cooler.
Field: Availability Schedule Name[LINK]
The name of a schedule that defines when the evaporative cooler is available. A schedule value of 0 indicates that the evaporative cooler is off for that time period. A schedule value greater than 0 indicates that the evaporative cooler can operate during the time period. If this field is blank, the schedule has values of 1 for all time periods.
Field: Cooler Maximum Effectiveness[LINK]
This field specifies the maximum effectiveness that is applied to the wetbulb depression to determine the conditions leaving the cooler. This effectiveness is a complicated function of the efficiency with which heat and mass are transferred on the secondary side and the efficiency of heat exchange between the secondary and primary flows. The model assumes that the effectiveness is constant.
Field: Cooler Flow Ratio[LINK]
Not used in this model.
Field: Recirculating Water Pump Power Consumption[LINK]
This field is used to specify the power consumed by the water pump that circulates water in Watts. The pump power and energy consumption is reduced by cycling when the amount of cooling needs to be restricted for control purposes.
Field: Secondary Fan Flow Rate[LINK]
This field is used to specify the secondary fan flow rate and is specified in m3/s. This flow rate would typically be similar in magnitude to the flow through the primary side. This field can be autosized. When it is autosized, the program detects if the component is in the main air loop or on an outdoor air path. If it is on the main air loop, then the flow rate is set to the AirLoopHVAC system’s design supply air flow rate (which is the maximum required for heating and cooling). If it is on the outdoor air path, then the flow rate is set to the larger of either the design minimum outdoor air flow rate or one-half of the main air loop design flow rate. The flow rate is used to determine parasitic fan energy and does not impact the modeling of cooler effectiveness. The flow rate (and fan power) is effectively reduced by cycling when the amount of cooling needs to be restricted for control purposes.
Field: Secondary Fan Total Efficiency[LINK]
This value is the overall efficiency of the fan, i.e., the ratio of the power delivered to the fluid to the electrical input power. It is the product of the motor efficiency and the impeller efficiency. The motor efficiency is the power delivered to the shaft divided by the electrical power input to the motor. The impeller efficiency is power delivered to the fluid (air) divided by the shaft power. The power delivered to the fluid is the mass flow rate of the air multiplied by the pressure rise divided by the air density. This input value must be between 0 and 1.
Field: Secondary Fan Delta Pressure[LINK]
This field is used to specify the pressure difference in Pascals experienced by the secondary fan as it moves air through the wet side of the cooler.
Field: Primary Air Inlet Node Name[LINK]
The name of the air inlet node for the primary air flow path through the cooler.
Field: Primary Air Outlet Node Name[LINK]
The name of the air outlet node for the primary air flow path through the cooler.
Field: Control Type[LINK]
This input field is not used by this model. But using this model does implement controlling of the primary outlet temperature.
Field: Dewpoint Effectiveness Factor[LINK]
This field specifies an effectiveness that is applied to the dewpoint depression to determine a bound for the conditions leaving the cooler. The model uses the warmer of the two temperatures determined from wetbulb depression and dewpoint depression.
Field: Secondary Air Inlet Node Name[LINK]
This field specifies the name of the node providing air to the secondary/wet side of the cooler. Typically this node could appear in an outdoor air node list or be part of an air system loop.
Field: Sensor Node Name[LINK]
This field specifies the name of a node that will provide system air temperature setpoint information. A separate SetpointManager object should be setup to update this node.
Field: Relief Air Inlet Node Name[LINK]
This field is optional, but can be used to feed two sources of secondary air into the wet side of the cooler. Typical use is to run the air system relief air into the system. The model first uses all of the air flow available from this node and then adds the air flow from the secondary air inlet node to make up the total defined by Secondary Fan Flow Rate.
Field: Water Supply Storage Tank Name[LINK]
This field is optional. It is used to describe where the cooler obtains water used for evaporative cooling. If blank or omitted, then the cooler will obtain water directly from the mains. If the name of a WaterUse:Storage object is used here, then the cooler will obtain its water from that tank. If a tank is specified, the cooler will attempt to obtain all the water it uses from the tank. However, if the tank cannot provide all the water the cooler needs, then the cooler will still operate and obtain the rest of the water it needs from the mains.
Field: Drift Loss Fraction[LINK]
This field is optional and can be used to model additional water consumed by the cooler from drift. Drift is water that leaves the cooling media as droplets and does not evaporate into the process air stream. For example, water may get blown off the evaporative media by winds and escape the air system. The value entered here is a simple fraction of the water consumed by the cooler for normal process evaporation. The amount of drift is this fraction times the water evaporated for the normal cooling process. This field can be left blank and then there will be no added water consumption from drift.
Field: Blowdown Concentration Ratio[LINK]
This field is optional and can be used to model additional water consumed by the cooler from blowdown. Blowdown is water that is intentionally drained from the cooler’s sump to offset the build up of solids in the water that would otherwise occur because of evaporation. The value entered here is dimensionless. It can be characterized as the ratio of solids in the blowdown water to solids in the make up water. Typical values are 3 to 5. The default is 3.0.
An IDF example is shown below:
Outputs[LINK]
The output variables that are available for the EvaporativeCooler:Indirect:ResearchSpecial object are shown below:
Evaporative Cooler Total Stage Effectiveness [][LINK]
The Total Stage Efficiency is defined as the temperature change of the supply air divided by the difference between the outdoor dry-bulb and wet-bulb temperatures, including the effect of the reduction in flow because of the secondary air stream. In other words, it is a measure of the approach to the outdoor wet-bulb temperature.
Evaporative Cooler Part Load Ratio [][LINK]
This output variable provides the part load fraction of the indirect cooler. The ResearchSpecial cooler model is able to modulate to meet a temperature set point to avoid over cooling. This output variable is the fraction formed by the ratio of the capacity needed over the maximum cooling capacity available. A value of 1.0 corresponds to full capacity cooling.
Evaporative Cooler Dewpoint Bound Status [][LINK]
This output variable is a flag that indicates if the modeling was based on dewpoint effectivenss rather than wetbulb effectiveness The ResearchSpecial model is usually based on wet-bulb approach, but since values in excess of 1.0 are allowed, there is a secondary constraint imposed by dewpoint. If the dewpoint effectiveness was applied, then this flag variable will have the value 1.0, otherwise it is 0.0.
Evaporative Cooler Electric Power [W][LINK]
Evaporative Cooler Electric Energy [J][LINK]
These output variables report the electric power and energy that are consumed by the secondary air fan and the sump pump.
Evaporative Cooler Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Mains Water Volume [m3][LINK]
This is the source of the water consumed. This output variable appears when mains water is supplied to the cooler.
Evaporative Cooler Storage Tank Water Volume [m3][LINK]
The water consumption is the water evaporated from the pad. This water consumption is only from the direct thermodynamics of water evaporation and does not include other sources of consumption such as drift or concentration blow down. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Water Volume [m3][LINK]
This is the water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
Evaporative Cooler Starved Mains Water Volume [m3][LINK]
This is the source (mains) of water consumed by the evaporative cooler that could not accually be met by the storage tank. This output variable appears when storage tank water is supplied to the cooler.
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