(285e) CFD Simulations of Rotating Zigzag Bed Hydrodynamics

The
concept of process intensification was first proposed in the late 1970s. High
gravity technology (abbreviated to HIGEE), which substitutes terrestrial
acceleration for higher centrifugal acceleration (up to 1000 g) achieved by
rotating a specially shaped bed, is a promising alternative to enhancing heat
and mass transfer in the process intensification field. Compared to
conventional distillation columns, the HIGEE can make dramatic reductions in
equipment volume, and reduces the capital and operation costs accordingly.

Generally,
an HIGEE device mainly consists of a rotor housed in a stationary casing and
driven by a motor. The structure of rotor determines the characteristics of
different HIGEE devices. There are several types of rotors, such as packing
bed, wave form disk, helical bed, multi-staged spraying bed and split packing
bed. Another type of HIGEE device, referred to as rotating zigzag bed (RZB),
was invented by Ji et al. and patented in China and
the United States. It has been successfully applied in continuous distillation
service after unremitting improvements and tests. The simplified sketch of the
RZB is shown in Figure 1. Tow series of concentric circular sheets are
alternately fixed on the rotational (lower) and stationary (upper) disk,
respectively; one series as rotational baffles and the other as stationary
baffles. The clearance between rotational baffles and the stationary disk as
well as between the stationary baffles and rotational disk offers zigzag flow
channels for fluids. The gas is introduced into the casing and flows inward
radially driven by pressure difference. The liquid is fed at the center of the
rotational disk flowing outward countercurrent to gas by virtue of centrifugal
force. In the interior of the rotor, the gas flows as continuous phase along a
zigzag path and the liquid undergoes multiple dispersion-accumulation recycles.
The liquid is dispersed in fine droplets by rotational baffles. These droplets
are intercepted by stationary baffles and then accumulate to form liquid film
which falls onto the rotational disk again. Then the liquid flows radially
outward to the next rotational baffle and is dispersed, and so on. During this
process, impingement and spray of the liquid in the rotor results in
fast-renewed gas-liquid interface with very large specific surface area
available for mass transfer.

Figure 1.
Simplified sketch of the rotor of the RZB.

1-Rotational disk, 2-Rotational baffles,
3-Gas inlet, 4-Stationary baffles, 5-Stationary disk, 6-Gas outlet, 7-Liquid
inlet, 8-Intermediate feed, 9-casing, 10-Liquid outlet, 11-Rotating axle

Mass
transfer performances of RZB and other HIGEE devices have been experimentally
studied in the literature, but few studies on the hydrodynamics have been
reported. The understanding of the two-phase hydrodynamic phenomenon in the
rotor is helpful for the fine tuning and optimization of HIGEE device design.

Figure
2. 3D physical model of RZB.

Due
to progresses in computer hardware and software and consequent increase of the
calculation speed, the computational fluid dynamics (CFD) modeling technique
becomes a powerful and effective tool for understanding the complex
hydrodynamics in chemical engineering processes. In this study, a
three-dimensional CFD model was developed to predict the hydrodynamics of RZB
as shown in Figure 2. The model considered gas- and liquid-flow within the
Eulerian-Eulerian framework in which both phase were treated as
interpenetrating continuum having separate transport equations. With the model
focusing on the interphase contacting region, the liquid phase has been taken
as the disperse phase, while the gas phase has formed the continuous phase.
Interphase momentum transfer term was employed for describing the interfacial
forces between the two phases. Since the focus is on the hydrodynamics behavior
of RZB, energy and mass transfers have not been considered in this study.