A well structured slideshow by Steve Lowe, PE for the Hampton Roads, VA Chapter of ASHRAE. Presentation explains how to apply cooling towers including the basic cooling tower principles, design considerations, and construction issues.
For more information on any cooling tower issue in Colorado, New Mexico, Wyoming, Montana, Utah, Nevada, Idaho, or the western Dakotas, contact:
Mountain States Engineering and Controls
1520 Iris Street
Lakewood, CO 80215
303.232.4100 Phone
303.232.4900 Fax
Email: info@mnteng.com
2. Stephen Lowe
ASHRAE Hampton Roads Chapter Past President
AECOM Design – Mechanical Engineering Discipline
Manager, Virginia Beach Division
Professional Engineer Commonwealth of Virginia Professional Engineer – Commonwealth of Virginia,
NCEES
BSME – University of Virginia, 2002
Sheet metal fabricator, equipment installer, refrigeration
service technician during high school and college
C l i E i f P Consulting Engineer from 2003 – Present
3. OverviewOverview
Introduction
Cooling Tower Basics
Principles of Operation
Types of Cooling Towers
Common Applications
Design Considerations
Selection CriteriaSelection Criteria
Open Piping and Pumping Systems
Water Quality
Tower Location
Ancillary Systems Ancillary Systems
Construction Issues
Constructability, Quality Control and Startup
Rating and Certification
L L d Lessons Learned
Conclusion
Resources
Questions and Discussion
4. Cooling Tower Basics
Principles of Operation
Cooling Via Evaporation – depends on Wet Bulb
TemperatureTemperature
Design Dry Bulb Temperatures commonly exceed 95 deg
F: poor delta T for cooling processes
D i W b lb h l d F Design Wet bulb much less: ~80 deg F
Use a process that depends on WB to take advantage of
greater delta Tg
Evaporative effect is a change of state and thus a large
transfer of energy occurs relative to the required mass
flowflow
5. Cl d Ci i
Open Cooling Tower
Closed Circuit
Cooling Tower
7. Cooling Tower Basics
Common Applications
Power Plant Steam Condensation
Process Cooling
HVAC Heat Rejection
Chiller Condenser Heat Chiller Condenser Heat
WSHP Loop Heat
*We will be focusing on open, cross flow cooling towers for
chiller condenser heat rejection for the remainder of the j
presentation.
10. Design Considerations
Selection Criteria
Process (Chiller Condenser) Temperature Requirements
Hot Water Temperature (HWT): Temperature of water entering the p ( ) p g
tower
Cold Water Temperature (CWT): Temperature of water leaving the
tower
Tower Range: HWT – CWT
Lower CWT generally results in higher Chiller Efficiency
Flow Rate or Capacity
Ambient Conditions
Evaporation (or Entering) Design Wet Bulb (EWB)
Approach: CWT ‐ EWB
Lower approach generally results in a larger tower
13. Design Conditions
Use Evaporation Design WB for selection of
evaporative equipment
U f % % % di i i h d i Use of 0.4%, 1%, or 2% condition is up to the designer
based on specific application and design firm practice
A 2 degree F margin of safety is recommended to A 2 degree F margin of safety is recommended to
account for recirculation (rule of thumb – further
analysis is required for the specific application)y q p pp
Condenser water delta T depends on many factors
such as the process that is cooled and optimization of
h i the pumping system
15. Design Considerations
Open Piping and Pumping Systems
Pump Head Estimation
l l f h h Determine actual static lift height
Determine impact of siphon draw: either break the siphon or
design to maintain it.
Determine friction head
Pipe
Equipment (condenser tower spray nozzle etc ) Equipment (condenser, tower spray nozzle, etc.)
Components (valves, strainers, etc.)
18. Design Considerations
Open Piping and Pumping Systems
Pump cavitation is the flashing (boiling) of the working
fluid (water) into a vapor due to excessively low suction
d i ft f d ith i i t d ti i t th pressure and is often confused with air introduction into the
pump suction.
Net Positive Suction Head (NPSH) is the measure of suction
pressure pressure.
The required suction pressure for a particular pump is
indicated NPSHR and is published as a curve on the pump
selection chart.
The suction pressure available to the pump in a particular
system is indicated NPSHA and must be calculated by the
engineer.
If NPSHA NPSHR it ti ill If NPSHA < NPSHR, cavitation will occur.
24. Design Considerations
Open Piping and Pumping Systems
Tower pan vortexing is caused by excessive velocity in
th t it i i d b t ll d bthe tower exit piping and can be controlled by:
Do not excessively oversize the pump
Maintaining tower exit pipe size for a minimum of 10 pipe g p p p p
diameters
Increase pan depth
Provide a vortex breaker in the tower pan Provide a vortex breaker in the tower pan
Install tower on the equator
25. Design Considerations
Open Piping and Pumping Systems
Tower pan drain down is caused by insufficient water
d th t fl d th t it i i d b id d depth to flood the tower exit piping and can be avoided
by:
Correctly sizing the makeup water liney g p
Evaporation Rate
Blowdown Rate
Providing a check valve to keep the piping system flooded on Providing a check valve to keep the piping system flooded on
pump shut down
Properly isolating tower cells in multiple cell installations
28. WRONG
Bypass connected to pump
i i i i suction piping can cause air
introduction to pump inlet and
unstable pump operation.
CORRECT
B di h i t b i ith Bypass discharging to basin with
balancing valve set equal to
discharge nozzle pressure drop
will result in constant pump
head and flooded pump suction.p p
31. Design Considerations
Water Quality
Removal of Solids
Chemical Treatment
Consult a chemical treatment professional for your specific
applicationpp
Biological Contamination
Minimize drift
Site towers away from air intakes
Avoid piping designs that result in stagnant water
Chemically treaty
36. Design Considerations
Ancillary Systems
Freeze Protection
Tower Sump Basin
Electric
Steam Injection
Recirculation
Piping Piping
Water Treatment Systems
Chemical Systems
Solids FiltrationSolids Filtration
Control Systems
Pneumatic operators – will require freeze protection in some
climates
Large valves require lots of torque – electric operators may need to
be industrial grade
39. Construction Issues
Lessons Learned
Tower Basin Freeze Protection
l d l d l l Direct steam injection is popular in industrial and large scale
HVAC applications.
Chemical used for boiler feedwater may react with condenser
water chemical treatment resulting in the release of noxious
gases.
A hot water circulator pump coupled to a heat source can be p p p
used instead.
40.
41. Construction Issues
Lessons Learned
Vertical Loop in Suction Piping
d d d h l Tower mounted on grade adjacent to mechanical room
Cold water pipe exits bottom of basin and passes through
mechanical room wall
Pipe is the run up the wall to the roof structure to get the pipe
across the room to the pump
Upon shutdown, the system equalizes and the piping at the Upon shutdown, the system equalizes and the piping at the
roof level becomes air locked
The pump will require manual priming in order to start
42.
43. Construction Issues
Lessons Learned
Flooding Tower on Pump Shutdown
Tower is mounted on grade adjacent to mechanical room Tower is mounted on grade adjacent to mechanical room.
There is a significant volume of water located above the tower
basin due to a long horizontal run of hot condenser water pipe
in the mechanical roomin the mechanical room.
The diverting valve is installed in the horizontal with the
bypass connection facing down.
Whenever the pump shuts down all of the water in the Whenever the pump shuts down, all of the water in the
horizontal pipe runs through the diverting valve and back to
the basin.
The basin overflows in the parking lot resulting in an p g g
unsightly puddle and wasted chemical treatment
50. Construction Issues
Lessons Learned
Multiple connected towers should have an equalization
liline.
When adding or replacing towers connected through an
equalization line, design the tower and framing to q , g g
ensure that the existing operating water level is
matched with the new tower.
If i i id ib i i l i f h If it is necessary to provide vibration isolation for the
tower, the piping system must be isolated from the
tower.