Article
Research for a Non-Standard Kenics Static Mixer with an
Eccentricity Factor
Chenfeng Wang , Hanyang Liu, Xiaoxia Yang and Rijie Wang *
Citation: Wang, C.; Liu, H.; Yang, X.;
Wang, R. Research for a Non-Standard
Kenics Static Mixer with an
Eccentricity Factor. Processes 2021, 9,
1353. https://doi.org/10.3390/
pr9081353
Received: 6 July 2021
Accepted: 29 July 2021
Published: 1 August 2021
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4.0/).
School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China;
chenfeng_wang@tju.edu.cn (C.W.); liuhanyang@tju.edu.cn (H.L.); xxy@tju.edu.cn (X.Y.)
* Correspondence: rjwang@tju.edu.cn
Abstract:
The Kenics static mixer is one of the most widely studied static mixers, whose structure–
function relationship has been studied by varying its aspect ratio and modifying the surface. However,
the effect of the symmetric structure of the Kenics static mixer itself on twisting the fluid has been
neglected. In order to study how the symmetrical structure of the Kenics static mixer impacts the fluid
flow, we changed the center position of elements at twist angle 90
◦
and introduced the eccentricity
factor
γ
. We applied LHS-PLS to study this non-standard Kenics static mixer and obtained the
statistical correlations of the aspect ratio, Reynolds number, and eccentricity factor on relative Nusselt
number and relative friction factor. We analyzed the results by comparing the PLS model with the
univariate analysis, and it was found that the underlying logic of the Kenics static mixer with an
asymmetric structure became different. In addition, a non-standard Kenics static mixer with an
asymmetric structure was investigated using vortex generation and dissipation through fluid flow
simulation. The results demonstrated that the classical symmetric structure has a minor pressure
drop, but the backward eccentric one has a higher thermal-hydraulic performance factor. It was
found that the nature of the eccentric structure is that two elements with different aspect ratios are
being combined at
θ =
90
◦
, and this articulation leads to non-standard Kenics static mixers with
different underlying logic, which finally result in the differences between the PLS model and the
univariate analysis.
Keywords:
Kenics static mixer; heat transfer; structure-function relationship; non-standard static
mixer; eccentricity factor
1. Introduction
Fluid mixing schemes can be divided into either “active”, where external forces drive
fluid movement, like electric field perturbations [
1
,
2
] and mechanical agitation [
3
], or
“passive”, where the contact area and contact time of the species samples are increased
through specially designed inserts, like a static mixer [
4
] and modified wall [
5
,
6
]. A static
mixer is an efficient mixing device that incorporates continuously repeating elements in the
pipeline and influences the fluid flow during the process, intensifying the mass and heat
transfer [
7
]. In recent years, it has been widely used in the processing of fine chemicals,
such as pharmaceuticals [8–10].
Kenics static mixers, as one of the classic types of static mixers, have the advantages
of their unique structure and easy manufacturing. Its structure–function relationship has
been extensively studied for many years [
11
–
14
]. The element of the Kenics static mixer
is obtained by 180
◦
reversing two ends of a metal blade. As shown in Figure 1, when
placed in a circular tube, two elements with different rotational directions need to be placed
one by one, intersecting. Mixing the fluid in the Kenics static mixer is accomplished by
continuously being split and reorganized by the crossover in the axial flow [
15
–
17
]. The
effectiveness of mixing and the resulting pressure drop depends on the specific geometric
parameters of the Kenics static mixer, including the pitch, thickness, and twist angle for
each mass transfer element [18–20].
Processes 2021, 9, 1353. https://doi.org/10.3390/pr9081353 https://www.mdpi.com/journal/processes
