Packed beds with gaseous flows are part of many industrial processes which, in their majority, come with an immense energy consumption. Packed beds are, for example, used in the food industry, for instance for coffee roasting, for drying processes in several fields, and for catalytic processes in chemical engineering. For yield and product quality optimization and the reduction of resource and energy consumption, a thorough understanding of the processes inside the packed bed, such as heat and mass transfer, is indispensable. The heat and mass transfer are thereby dependent on the characteristics of the gaseous flow in the bed. The measurement of flow fields in the complex geometry is, however, very challenging.
To measure gas velocities in packed beds, intrusive measurement techniques like hot-wire anemometry or endoscopic PIV can be applied. Different authors (Cairns and Prausnitz 1959; Morales et al. 1951; Moran and Glicksman 2003; Schwartz and Smith 1953) worked with hot-wire anemometry to obtain the velocity distribution for different bed heights. However, only pointwise measurements are obtained with this approach, so that numerous anemometers have to be applied at the same time to obtain velocity information at several points, or the measurement position has to be varied in a stationary flow. Both lead to an impact of the inserted measurement device on the gas flow. 2D-velocity fields in the interstices of packed beds can also be obtained by endoscopic PIV measurements (Blois et al. 2012; Shaffer et al. 2013). Unfortunately, the macroscopic endoscopes also modify the flow field.
Non-intrusive measurement techniques avoid influencing the flow. Tomographic techniques can be used, like magnetic resonance imaging (Baldwin et al. 1996; Kuniyasu Ogawa et al. 2001; Lovreglio et al. 2018; Ogawa et al. 2000; Ogawa et al. 2001; Ren et al. 2005; Sankey et al. 2009; Sederman et al. 1998; Suekane et al. 2003) or particle emission tomography (Khalili et al. 1998). These approaches do not require transparent geometries but suffer from low spatial and temporal resolutions and materials incompatibilities (Gladden et al. 2006; Poelma 2020).
Optical measurement techniques allow for high resolution in space and time. These, however, require optical access. Therefore, PIV measurements were primarily performed in near wall regions of packed beds (Wu and Mirbod 2018) or on the surface of beds (Pokrajac and Manes 2009) where one has direct optical access. By the use of transparent materials, e.g. glass balls with a refractive index in the range of n = 1.45 to n = 1.96 (Budwig 1994), optical access to the packed bed can also be generated. Unfortunately, transparent packing materials introduce distortions in the PIV images, since the material and the flow have different refractive indices. In general, the distortions can be avoided with refractive index matching (RIM) using different index matched fluids (Borrero-Echeverry and Morrison 2016; Budwig 1994; Wiederseiner et al. 2011). RIM has also been applied to Particle Tracking Velocimetry (PTV) and PIV techniques in porous media or packed beds (Huang et al. 2008; Monica et al. 2009; Moroni and Cushman 2001). In this way, turbulence quantities of the interstitial flow have been determined (Khayamyan et al. 2017a; Khayamyan et al. 2017b; Patil and Liburdy 2013, 2015) and first attempts to measure 3D velocity fields have been done via tomographic PIV (Larsson et al. 2018). This approach is, however, limited to liquids as working fluid because of the significant discrepancy in the refractive indices between gases and solids so that no matching is possible. For gaseous flows, similarity approaches have therefore been applied for data evaluation and interpretation (Hassan and Dominguez-Ontiveros 2008; Nguyen et al. 2019).
To the best of our knowledge, velocity data of gaseous flows in packed beds, measured by PIV, has not been obtained systematically up to now. First approaches have been done by our group (Kováts et al. 2015) and the fundamentals of the technique proposed in this paper have been published in (Martins et al. 2018a, b). Besides RT-PIV, all aforementioned measurement techniques have to accept compromises between influencing the flow, use of liquids instead of gases, and temporal and/or spatial resolution.
Therefore, RT-PIV is proposed here for the measurement of instantaneous 2D gas velocity fields inside transparent packed beds. RT-PIV is a non-intrusive optical measurement technique and allows for temporally as well as spatially highly resolved measurements of gaseous flows in packed beds.
The ray tracing correction takes as input a 3D computer model of the experimental setup as well as the raw PIV images. Based on it, two optical light transport simulations are performed. In the first one, the captured PIV image is used as source and an inverse simulation from the camera into the experimental setup recovers an approximation of the light field. The second step simulates the image formation in the experimental setup but with the transparent geometry removed, yielding an undistorted image.
Very few experimental realisations of RT-PIV exist up to now. They are mostly in the field of surface reconstruction or correcting distortions in PIV measurements caused by liquid-gas boundaries (Kang et al. 2004; Minor et al. 2007; Wu et al. 2019). Some applications of ray tracing in PIV measurements can also be found in the field of in-cylinder flows (Daher et al. 2019; Zha et al. 2016) where curvature effects due to transparent cylindrical walls require correction.
In the present work, we discuss the application of RT-PIV in gaseous flows through a packed bed, with particular emphasis on the challenges and difficulties the approach implies. Furthermore, the step-wise validation of the ray tracing based correction method is presented. As setup we consider 2D RT-PIV gas velocity measurements in a regular body-centred-cubic packing of glass balls.