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Optimal Design of a Dry-Type Natural-Draft Cooling Tower by Geometric Programming

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Advances in Geometric Programming

Part of the book series: Mathematical Concepts and Methods in Science and Engineering ((MCSENG,volume 21))

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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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© 1980 Plenum Press, New York

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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

  • Publisher Name: Springer, Boston, MA

  • Print ISBN: 978-1-4615-8287-8

  • Online ISBN: 978-1-4615-8285-4

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