This work presents and discusses the results of a series of experiments inv
estigating effects from corona discharge in air on the heat transfer rate a
nd on the pressure drop in tube flows. Two electrode geometries were studie
d: a single wire electrode, concentric with the grounded tube wall and dual
equipotential wire electrodes which were offset 0.4 cm from center in the
horizontal plane. Both positive and negative discharge were examined for th
e single-wire geometry, at Reynolds numbers in the range 1,000 less than or
equal to Re-D less than or equal to 20, 000. The dual wire geometry was st
udied using positive polarity discharge only, over the range Re-D = 1,000 t
o Re-D = 10, 000. Heat transfer rates were determined at electrode potentia
ls from 6.00 kV (DC) to 7.75 kV (DC), depending on polarity and electrode c
onfiguration. Baseline data were also obtained with the electrode(s) at gro
und potential.
Results demonstrate increases in the Nusselt number of more than two hundre
d per cent over the values obtained in the absence of discharge. Relative i
ncreases in the friction coefficients were generally comparable to the corr
esponding Nusselt number enhancement. The extent of the increase in either
quantity was highly dependent on discharge current and on the Reynolds numb
er. The relative enhancements of both Nusselt number and friction loss coef
ficient were generally reduced at higher Reynolds numbers (Re-D greater tha
n or equal to 5000). However, the fall-off of enhancement with Reynolds num
ber was less pronounced in the offset, dual-electrode geometry.
Results suggest the enhancement mechanism may significantly depend on the e
lectrode geometry, independent of the geometry effects on discharge current
. The observed trends are discussed in the context of current theory.