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Numerical and Experimental Investigation of the Effect of Geometrical Parameters on the Performance of a Contraction-Expansion Helical Mixer

  • Liang Dong and Zhang Shufen EMAIL logo
Published/Copyright: July 15, 2014

Abstract

In this study, the mixing efficiency of a passive contraction-expansion helical mixer, which combines several features, such as helical pipes for induction of secondary flows and sudden expansion and contraction array for expansion vortices, was numerically and experimentally studied. We employed the method of Box–Behnken to select the appropriate design points. Then, various configurations were investigated via computational fluid dynamics (CFD) simulations. The extent of mixing was evaluated by monitoring the residence time distribution (RTD) and observing the shape of the RTD curves. A fast competitive-consecutive diazo coupling reaction is carried out to validate the RTD results. The influences of radius of curvature of the helical mixer, ratio of the length of the contraction part to expansion part, pitch of helical mixer, and the Reynolds number (Re) on mixing efficiency, and pressure drop were also investigated. As expected, the radius of curvature of the helical mixer, ratio of the length of the contraction part to expansion part, and the Reynolds number affected significantly the mixing efficiency, while the pitch of helical mixer had little influence on mixing efficiency. Quadratic models for mixing efficiency and pressure drop were then proposed and could be used for designing the optimal contraction-expansion helical mixer for the required pumping power.

Nomenclature

b [m]

pitch of helical mixer

C(t) [s−1]

tracer concentration as a function of time

dc [m]

inner diameter of the contraction part

de [m]

inner diameter of the expansion part

E(t) [s−1]

RTD function

E(θ) [–]

normalized RTD function

Ep [–]

peak value of the normalized RTD function

k [mol m−3 s−1]

reaction rate constants,

Lc [m]

length of the contraction part

Le [m]

length of the expansion part

o–R [–]

2-[(4-sulfophenyl)azo]-1-naphthol

p–R [–]

4-[(4-sulfophenyl]azo]-1-naphthol

R [m]

radius of curvature

Re [–]

Reynolds number

S [–]

2,4-bis[(4-sulfophenyl)azo]-1-naphthol

t [s]

mixing time

tm [s]

mean residence time

ΔP [kg m−1 s−2]

pressure drop along the conduit

XS

product distribution

Y

response function

Greek letters

aj, βj [–]

coefficients of the quadratic model

θ [–]

dimensionless time

Acknowledgements

The authors are grateful to the financial supports of the National Key Technology R&D Program (2011BAE07B01) and Major Program of the National Natural Science Foundation of China (20836001).

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Published Online: 2014-7-15
Published in Print: 2014-1-1

©2014 by De Gruyter

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