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Experimental Heat Transfer
A Journal of Thermal Energy Generation, Transport, Storage, and Conversion
Volume 32, 2019 - Issue 1
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Articles

An experimental study on convective heat transfer performance of steam and air flow in V-shaped rib roughened channels

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Pages 51-68 | Received 18 Nov 2017, Accepted 25 Apr 2018, Published online: 01 Oct 2018
 

ABSTRACT

An experimental study on heat transfer characteristics of steam and air flows in a V-shaped ribbed channels was conducted. The effects of Reynolds numbers and rib angles on heat transfer of steam and air were obtained. The area-averaged Nusselt numbers of steam flow at a Reynolds number of 12,000 were 13.9%, 20.6%, 27.1%, and 27.9% higher than those of air flow for rib angles of 90°, 75°, 60°, and 45°, respectively. The correlations for Nusselt number in terms of Reynolds number and rib angle for steam and air in V-shaped ribbed channels were developed.

Highlights

  • The heat transfer distributions of V-shaped rib-roughness channel cooled by superheated steam and air flows were experimentally investigated.

  • Influences of rib angle on heat transfer enhancement of V-shaped ribbed channel under steam and air cooling were both studied.

  • Advantage of steam cooling to air cooling in V-shaped ribbed channel with different rib angle was compared and analyzed.

  • Correlations for Nusselt number in terms of Reynolds number and rib angle for steam and air cooling in V-shaped ribbed channels were developed.

Nomenclature

A=

area of the heat plate, m2

AR=

Aspect ratio of channel

Cp=

specific heat at constant pressure

Dh=

hydraulic diameter of the channel, mm

e=

rib width and rib height, mm

e/Dh=

relative rib height,

H=

channel height, mm

h=

heat transfer coefficient, W/m2/K

I=

current provided by DC, A

L=

length of the heat transfer surface, mm

Nu=

Nusselt number

Nulocal=

local Nusselt number

Nuave=

area-averaged Nusselt number

P=

rib pitch, mm

P/e=

rib pitch-to-height ratio

Pr=

Prandtl number

Qloss=

heat loss dissipating to the environment, W

Qnet=

heat flux provided by heat plate, W

QT=

total heating power, W

Re=

Reynolds number, based on hydraulic diameter of the channel

Tw=

temperature on target plate, °K

Ts=

temperature of the coolant in the channel, °K

Tin=

temperature of the coolant at the inlet, °K

Tout=

temperature of the coolant at the outlet, °K

U=

voltage provided by DC, V

V=

the flow velocity in the channel, m/s

W=

channel width, mm

Greek symbols

α=

rib angle, °

λ=

thermal conductivity, W/(m.K)

μ=

dynamic viscocity, kg/(m.s)

ρ=

density, kg/m3

Additional information

Funding

This work was supported by the National Natural Science Foundation of China [51206109].

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