AM Technology are pleased to share news of a publication in "Chemical Engineering and Processing - Process Intensification" describing work performed collaboratively between the University of Leeds and AM Technology as part of an IbD project, entitled: Physical and numerical characterisation of an agitated tubular reactor (ATR) for intensification of chemical processes.
Please find a link to the publication here: https://doi.org/10.1016/j.cep.2022.109067
The abstract of the paper states:
"This study investigates the dynamics of a novel, oscillatory, intensified plug-flow reactor – an agitated tubular reactor (ATR) – designed for efficient flow processing of solid-liquid mixtures. The relative movement of the reactor and agitator bar, and associated effects on fluid mixing were characterised physically with a suite of experimental instruments – utilising laser-based, video-based and acoustic techniques – and numerically via a Lattice Boltzmann method (LBM) computational fluid dynamic simulation. The reactor volume consisted of a cylindrical outer tube containing a free-moving, perforated agitator tube. The position, velocity and angular velocity of the inner agitator relative to the outer tube were measured experimentally and computationally under a range of realistic operating conditions, in terms of applied agitation frequency and displacement distance, along with their effect on the associated fluid velocity and turbulence levels. Additionally, simulations were used to validate a model for the reactor power input. The agreement between experimental and simulation data were very good in all cases, leading to clear recommendations for optimal operating conditions, while an experimentally derived regime map of the types and magnitudes of ATR motion is also presented."
Active mixing is a vital component of Coflore flow reactors and is key to offering a viable continuous alternative to traditional batch reactors with regard to versatility and simplicity of operation. The unique mixing characteristics of the Coflore ATR stem from the use of radial mechanical stirring rather than passive or diffusive mixing. This approach decouples plug flow and mixing from residence time, to give very low dispersion numbers, fast blending, and high shear across a large range of residence times from seconds to hours.
Figure 1, reprinted from the publication, shows an example of the agitator motion within an ATR reactor tube at an agitation frequency of 3 Hz, with the three 2D slices displaying the velocity field at different relative positions of the agitator. The researchers concluded that the process fluid is well coupled to the ATR agitator and that the agitator motion generates fluid wakes within the perforated holes located along the length of the agitator, creating small regions of high fluctuating velocities where shear mixing will be enhanced. The researchers went on to state that the regions "are expected to cause higher levels of micro-mixing, despite relatively low peak Reynolds numbers."