Abstract
In this paper, the optimal design of dry-type natural-draft cooling towers is investigated. Using physical laws and engineering design relations that govern the system, a rather detailed optimization model is developed. This model is then reformulated as a geometric programming problem. A primary consideration in this reformulation is how certain polynomial equations may be effectively replaced by inequalities. A numerical example follows.
This research was supported in part by the National Science Foundation, Grant No. MPS75-09443, and by the NATO Postdoctoral Fellowship Program in Science.
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Abbreviations
- A Fi :
-
total fin surface, sq ft
- A i :
-
total inside tube surface, sq ft
- A o :
-
total outside tube surface, sq ft
- \( \overline{A} \) o :
-
total outside bare tube surface (finned tubes), sq ft
- A To :
-
tot surface area of tower shell, sq ft
- a s :
-
free flow area, sq ft
- b :
-
fin thickness, ft
- C F,Fi :
-
fixed charges on air cooler fins, $/yr
- C F,To :
-
fixed charges on tower shell, $/yr
- C F,Tu :
-
fixed charges on air cooler tubes, $/yr
- C O,P :
-
operating cost of air cooler pump, $/yr
- c :
-
distance between two adjacent fins, ft
- c p,a :
-
cP a specific heat of air, Btu/lb °F
- D e :
-
equivalent diameter, ft
- D i :
-
inside tube diameter, ft
- D o :
-
outside tube diameter, ft
- D To :
-
tower diameter, ft
- D v :
-
equivalent volumetric diameter, ft
- d :
-
distance between centerlines of two adjacent banks of tubes in air cooler, ft
- e :
-
gap between fins of two adjacent banks of tubes, ft
- F:
-
cross-flow-temperature-difference correction factor
- f :
-
frictional surface, sq ft
- G :
-
greater terminal temperature difference, °F
- H To :
-
tower height above air entrance, ft
- h :
-
fin height, ft
- h i :
-
inside film coefficient, Btu/(sq ft) hr °F
- h o :
-
outside film coefficient, Btu/(sq ft) hr °F
- L :
-
tube length, ft
- l :
-
tube wall thickness, ft
- N :
-
number of tubes in bank of air cooler
- \( \overline{N} \) :
-
number of vertical banks in air cooler
- n :
-
number of fins per ft. of tube length
- q :
-
rate of heat transfer, Btu/hr
- S l :
-
center-to-center distance to the nearest tube in the next bank, ft
- S t :
-
pitch in a bank, ft
- t To :
-
tower shell thickness, ft
- T :
-
temperature, °R
- U :
-
lesser terminal temperature difference, °F
- W :
-
flow rate, lb/hr
- ΔP f :
-
tower friction loss, psi
- ΔP l :
-
tower leaving loss, psi
- ΔP o :
-
pressure drop across air cooler coils, psi
- ΔP t :
-
theoretical tower draft, psi
- ΔT a :
-
change in air temperature, °F
- ΔT m :
-
overall mean temperature drop between hot and cold fluid, °F
- ΔT mi :
-
mean temperature drop through inside tube film, °F
- ΔT mo :
-
mean temperature through outside tube film, °F
- Ω:
-
fin efficiency
- a :
-
air
- w :
-
water
- c :
-
cold
- h :
-
hot
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Ecker, J.G., Wiebking, R.D. (1980). Optimal Design of a Dry-Type Natural-Draft Cooling Tower by Geometric Programming. In: Avriel, M. (eds) Advances in Geometric Programming. Mathematical Concepts and Methods in Science and Engineering, vol 21. Springer, Boston, MA. https://doi.org/10.1007/978-1-4615-8285-4_22
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DOI: https://doi.org/10.1007/978-1-4615-8285-4_22
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