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COOLING TOWERS
 Prepared by:-
ENG/ Mostafa Nassar
 Senior Mechanical Engineer
 Phone:- 00201065749313
 E-mail:- Mostafa.sadek.nassar73@gmail.com
COOLING TOWERS
 INTRODUCTION
 COOLING TOWER FUNDAMENTALS
 COOLING TOWER PERFORMANCE FACTORS
 COMPONENTS AND MAIN FEATURES OF COOLING TOWER
 TYPES OF COOLING TOWER
 ASSESSMENT OF COOLING TOWER PERFORMANCE APPLICATIONS
 REFERENCES
 INTRODUCTION
 Cooling tower is heat rejection
device, which extracts waste heat to
the atmosphere through the cooling
of a water stream to a lower
temperature.
 It is a device designed to reject heat
from the condenser water to the
ambient air.
 Every cooling tower, no matter how
configured or constructed, must have
the elements shown in Figure 1.
 Cooling tower fundamentals
 Every cooling tower, no matter how configured or constructed,
must have the elements shown in Figure 2.
 Fill: Heat transfer media in the cooling tower.
 Hot-water distribution (“wet deck”).
 Pans or basins with metering outlets or spray nozzles
designed to provide an even distribution of the return
condenser water entering the fill.
 Fan(s). All cooling towers used for HVAC applications are
mechanical draft towers that use one or more fans to provide
airflow through the tower.
 Inlet louvers and drift eliminators. Inlet louvers act to force the
air entering the tower into as straight and even flow pattern as
possible.
COOLING TOWER HEAT TRANSFER
 Heat is transferred from a water droplet to the
surrounding air by both sensible and latent heat
transfer processes. Figure 3 illustrates a typical
water droplet and the heat transfer mechanisms.
This heat transfer process can generally be
modeled using the Merkel equation:
 The amount of heat removed from the water must
be equal to the heat absorbed by the surrounding
air as shown by the following equation:
L/G =
(𝒉𝟐−𝒉𝟏)
(𝑻𝟏−𝑻𝟐)
 Cooling tower performance factors
 there are three factors that define the
requirements for a specific cooling tower
characteristic:
 1. Entering (ambient) air wet bulb temperature
 2. Condenser water flow rate
 3. Approach
 Once a tower is selected, that is, the cooling
tower characteristic is established, changes in
any of these three factors may necessitate a
change in the cooling tower.
 Cooling tower performance
factors
 Every HVAC cooling tower has six functional components: (1) fill,
(2) wet deck, (3) basin, (4) fan(s), (5) inlet louvers, and (6) drift
eliminators. To this list we must also add the two structural
elements: the structural frame and the casing.
 FILL
 Fills types:- a) splash fill b) film fill.
 STRUCTURAL FRAME
 CASING
 The wet deck
 BASINS
 INTAKE LOUVERS AND DRIFT ELIMINATORS
 FANS, MOTORS, AND DRIVES
 TYPES OF COOLING TOWERS
 Basic HVAC tower configurations are dictated by
 (1) the direction of the air versus water flow through the
tower fill
 (2) the location of the tower fan(s).
 Cooling towers can be classified in two types
1) Natural Draught Cooling Tower
Natural Draught
 TYPES OF COOLING TOWERS
 2) Mechanical or Forced Draught
Cooling Tower
Name?
Name?
 Assessment of Cooling Tower Performance
 There are several parameters to assess the performance of cooling towers. Note: CT = cooling tower; CW = cooling water
1) Range
 This is the difference between cooling tower inlet and outlet temperature. A high cooling tower range means that cooling tower has
been able to reduce temperature effectively.
CT range (oC) = CW inlet temperature (oC) – CW outlet temperature (oC)
2) Approach
 This is the difference between the cooling tower outlet cold water temperature and ambient wet bulb temperature. The lower the
approach the better the cooling tower performance. The ‘approach’ is a better indicator of cooling tower performance.
3) Effectiveness
 This is the ratio between the range and the ideal range (in percentage), i.e. difference between cooling water inlet temperature and
ambien wet bulb temperature. The higher this ratio, the higher the cooling tower effectiveness.
CT effectiveness (%) = 100 x (CW in temp – CW out temp) / (CW in temp – WB temp)
 Assessment of Cooling Tower Performance
4) Cooling Capacity
 This is the heat rejected in kCal/hr, given as product of mass flow rate of water, specific heat and temperature difference.
5) Evaporation Loss
 This is the water quantity evaporated for cooling duty. Theoretically the evaporation quantity works out to 1.8 m3 for
following formula can be used:
Evaporation loss (m3/hr)= 0.00085 x 1.8 x circulation rate (m3/hr) x (CW inlet temperature – CW outlet temperature)
6) Cycles of Concentration
 This is the ratio of dissolved solids in circulating water to the dissolved solids in make up water. Based on the vendor of
usually 5-7.
7) Blow down Losses
 It depends upon cycles of concentration and the evaporation losses and is given by formula:
Blow down = Evaporation loss /(Cycles of concentration -1)
 references
 HVAC water chillers and cooling towers fundamentals, application, and
operation by Stanford, Herbert W.
 Wikipedia (images).

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Cooling tower

  • 1. COOLING TOWERS  Prepared by:- ENG/ Mostafa Nassar  Senior Mechanical Engineer  Phone:- 00201065749313  E-mail:- Mostafa.sadek.nassar73@gmail.com
  • 2. COOLING TOWERS  INTRODUCTION  COOLING TOWER FUNDAMENTALS  COOLING TOWER PERFORMANCE FACTORS  COMPONENTS AND MAIN FEATURES OF COOLING TOWER  TYPES OF COOLING TOWER  ASSESSMENT OF COOLING TOWER PERFORMANCE APPLICATIONS  REFERENCES
  • 3.  INTRODUCTION  Cooling tower is heat rejection device, which extracts waste heat to the atmosphere through the cooling of a water stream to a lower temperature.  It is a device designed to reject heat from the condenser water to the ambient air.  Every cooling tower, no matter how configured or constructed, must have the elements shown in Figure 1.
  • 4.  Cooling tower fundamentals  Every cooling tower, no matter how configured or constructed, must have the elements shown in Figure 2.  Fill: Heat transfer media in the cooling tower.  Hot-water distribution (“wet deck”).  Pans or basins with metering outlets or spray nozzles designed to provide an even distribution of the return condenser water entering the fill.  Fan(s). All cooling towers used for HVAC applications are mechanical draft towers that use one or more fans to provide airflow through the tower.  Inlet louvers and drift eliminators. Inlet louvers act to force the air entering the tower into as straight and even flow pattern as possible.
  • 5. COOLING TOWER HEAT TRANSFER  Heat is transferred from a water droplet to the surrounding air by both sensible and latent heat transfer processes. Figure 3 illustrates a typical water droplet and the heat transfer mechanisms. This heat transfer process can generally be modeled using the Merkel equation:  The amount of heat removed from the water must be equal to the heat absorbed by the surrounding air as shown by the following equation: L/G = (𝒉𝟐−𝒉𝟏) (𝑻𝟏−𝑻𝟐)
  • 6.  Cooling tower performance factors  there are three factors that define the requirements for a specific cooling tower characteristic:  1. Entering (ambient) air wet bulb temperature  2. Condenser water flow rate  3. Approach  Once a tower is selected, that is, the cooling tower characteristic is established, changes in any of these three factors may necessitate a change in the cooling tower.
  • 7.  Cooling tower performance factors  Every HVAC cooling tower has six functional components: (1) fill, (2) wet deck, (3) basin, (4) fan(s), (5) inlet louvers, and (6) drift eliminators. To this list we must also add the two structural elements: the structural frame and the casing.  FILL  Fills types:- a) splash fill b) film fill.  STRUCTURAL FRAME  CASING  The wet deck  BASINS  INTAKE LOUVERS AND DRIFT ELIMINATORS  FANS, MOTORS, AND DRIVES
  • 8.  TYPES OF COOLING TOWERS  Basic HVAC tower configurations are dictated by  (1) the direction of the air versus water flow through the tower fill  (2) the location of the tower fan(s).  Cooling towers can be classified in two types 1) Natural Draught Cooling Tower Natural Draught
  • 9.  TYPES OF COOLING TOWERS  2) Mechanical or Forced Draught Cooling Tower Name? Name?
  • 10.  Assessment of Cooling Tower Performance  There are several parameters to assess the performance of cooling towers. Note: CT = cooling tower; CW = cooling water 1) Range  This is the difference between cooling tower inlet and outlet temperature. A high cooling tower range means that cooling tower has been able to reduce temperature effectively. CT range (oC) = CW inlet temperature (oC) – CW outlet temperature (oC) 2) Approach  This is the difference between the cooling tower outlet cold water temperature and ambient wet bulb temperature. The lower the approach the better the cooling tower performance. The ‘approach’ is a better indicator of cooling tower performance. 3) Effectiveness  This is the ratio between the range and the ideal range (in percentage), i.e. difference between cooling water inlet temperature and ambien wet bulb temperature. The higher this ratio, the higher the cooling tower effectiveness. CT effectiveness (%) = 100 x (CW in temp – CW out temp) / (CW in temp – WB temp)
  • 11.  Assessment of Cooling Tower Performance 4) Cooling Capacity  This is the heat rejected in kCal/hr, given as product of mass flow rate of water, specific heat and temperature difference. 5) Evaporation Loss  This is the water quantity evaporated for cooling duty. Theoretically the evaporation quantity works out to 1.8 m3 for following formula can be used: Evaporation loss (m3/hr)= 0.00085 x 1.8 x circulation rate (m3/hr) x (CW inlet temperature – CW outlet temperature) 6) Cycles of Concentration  This is the ratio of dissolved solids in circulating water to the dissolved solids in make up water. Based on the vendor of usually 5-7. 7) Blow down Losses  It depends upon cycles of concentration and the evaporation losses and is given by formula: Blow down = Evaporation loss /(Cycles of concentration -1)
  • 12.  references  HVAC water chillers and cooling towers fundamentals, application, and operation by Stanford, Herbert W.  Wikipedia (images).

Editor's Notes

  1. Fill is designed to maximize the “contact” between the return condenser water and the ambient air. The better the contact, obviously, the better the evaporation and heat transfer. Hot-water distribution (“wet deck”). Pans or basins with metering outlets or spray nozzles designed to provide an even distribution of the return condenser water entering the fill. Cold water basin. The basin, either as an integral part of the tower or as a separate sump, collects the water passing through the tower for supply to the system by the condenser water pump. The basin must also be sized to contain enough water to supply the condenser water system until the pump returns water to the tower. Fan(s). All cooling towers used for HVAC applications are mechanical draft towers that use one or more fans to provide airflow through the tower. Inlet louvers and drift eliminators. Inlet louvers act to force the air entering the tower into as straight and even flow pattern as possible, while the drift eliminators are designed to trap and remove any entrained water droplets that may be in the tower’s leaving air.
  2. Where KaV/L = cooling tower characteristic K = mass transfer coefficient (lb water/h ft2 ) a = contact area/tower volume (1/ft) V = active cooling volume/plan area (ft) L = water mass flow rate (lb/h ft2 ) T1 = entering (hot) water temperature (°F) T2 = leaving (cold) water temperature (°F) T = bulk water temperature (°F) hw = enthalpy of air–water vapor mixture at bulk water temperature (Btu/ lb of dry air) ha = enthalpy of air–water vapor mixture at wet bulb temperature (Btu/lb of dry air) L/G = water-to-air mass flow ratio (lb of water/lb of air) h1 = enthalpy of air–water vapor mixture at inlet wet bulb temperature (Btu/ lb of dry air) h2 = enthalpy of air–water vapor mixture at exhaust wet bulb temperature (Btu/lb of dry air)
  3. The selection of a cooling tower for a specific set of required performance parameters (condenser water flow rate, selected range, and ambient wet bulb temperature) results in establishing a required cooling tower characteristic. the performance parameters that are subject to change include the following: 1. Increase of entering wet bulb temperature. Too often, the wrong ambient wet bulb temperature is selected for tower sizing. 2. Increase of rejected heat load. This may dictate increasing the condenser water flow rate and/or increasing the range.
  4. fill:- The function of the tower fill is to provide a large “contact area” between the water flow and the airflow to promote evaporation and heat transfer. Splash and Film Fill Media: As the name indicates, splash fill media generates the required heat exchange area by splashing action of water over fill media and hence breaking into smaller water droplets. Thus, surface of heat exchange is the surface area of the water droplets, which is in contact with air. Choosing a Cooling Tower The counter-flow and cross flows are two basic designs of cooling towers based on the fundamentals of heat exchange. It is well known that counter flow heat exchange is more effective as compared to cross flow or parallel flow heat exchange. Cross-flow cooling towers are provided with splash fill of concrete, wood or perforated PVC. Counter-flow cooling towers are provided with both film fill and splash fill. STRUCTURAL FRAME:- A structural framing system is required to support the wet deck, fan(s), fill, intake louvers, and drift eliminators. Casing is required to enclose the fill and to create the tower air and water flow path. CASING:- A cooling tower’s casing performs two roles. First, it forms an enclosure around the fill to create a contained air path or plenum, forcing the airflow through the fill. Second, it simply helps to keep the water inside the tower. The wet deck:- is located at the top of the tower and its job is to distribute the incoming warm condenser water as evenly as possible over the fill to ensure uniform heat transfer. BASINS:- The basin is located at the bottom of the tower and its job is to collect the cold condenser water for supply to the condenser water pump. INTAKE LOUVERS AND DRIFT ELIMINATORS:- Intake louvers are provided on all crossflow cooling towers to help control the airflow over the fill. The louvers are spaced and slanted to direct air evenly into the fill pack. FANS, MOTORS, AND DRIVES:- One or more fans, connected to one or more motors via a drive assembly, provide the motive power for airflow through a mechanical draft HVAC cooling tower.
  5. Almost all HVAC cooling towers are film or splash fill, mechanical draft type. 1) Natural Draught Cooling Tower: In this type of cooling tower, fan is not used for circulating air but here, by enclosing the heated air in the chimney and it will create pressure difference between heated air and surrounding air. Because of this pressure difference air enters into the cooling tower. It requires large hyperbolic tower, so capital cost is high but operating cost is low because of absence of electrical fan. There are two types of natural draught cooling tower, rectangular timber tower and reinforced concrete hyperbolic tower.
  6. Mechanical or Forced Draught Cooling Tower: In this type of cooling tower, fan is used to circulate the air. When power plant runs on peak load, it requires a very high rate of cooling water. To rotate fan, it uses motor with speed around 1000 rpm. Working principle is same as natural draught cooling tower, only difference is that here fan is mounted on the cooling tower. If fan is mounted on the top of the tower is called as induced draught cooling tower which is most popular for very large capacity installation and requires large capacity of fan. So, forced draught cooling tower contains horizontal shaft for the fan and it is placed at bottom of the tower and induced draught cooling tower contains vertical shaft and it is placed at top of the cooling tower.
  7. 1) Range Example: Inlet and outlet cooling water temperature of my cooling tower is 31 and 41oC, respectively. Then CT range is 41-31 = 10oC 2) Approach Example: Wet bulb temperature = 27.4 oC, therefore CT approach is 31-27.4 = 3.6oC 3) Effectiveness Example: CT effectiveness of my cooling tower = 100 x (41-31) / (41-27.4) = 73.53%
  8. 4) Cooling Capacity Example: Flow rate of water = 1225 m3/hr Density = 1000 kg/m3 Specific heat =4.2 kJ/kgoC Temperature difference = 10 oC Heat rejected = 1225 x 1000 x 4.2 x 10 =  51,450,000 kJ/hr = 12,348,000 kCal/hr 5) Evaporation Loss Example: Evaporation loss =0.00085 x 1.8 x 1225 x (41-31) = 18.74 m3/hr 7) Blow down Losses Example: By using cycles of concentration = 7, Blow down = 18.74/(7-1) = 3.12 m3/hr