Zobrazeno 1 - 10
of 62
pro vyhledávání: '"Vivek V. Buwa"'
Publikováno v:
Particuology. 75:50-68
Publikováno v:
Industrial & Engineering Chemistry Research. 60:17677-17693
Eulerian computational fluid dynamics (CFD) models that can predict bubbling behavior accurately are important to predict solids mixing, transport processes, and reactions in fluidized beds. In the...
Publikováno v:
Journal of Fluid Mechanics. 948
Liquid spreading through a randomly packed particle-resolved bed influenced by capillary or inertial ( $AB_s \sim 1$ ), and gravitational force (moderately ( $AB_s \sim 0.1$ ) and strongly ( $AB_s \sim 0.01$ )) is investigated using the volume-of-flu
Publikováno v:
AIChE Journal. 68
Autor:
Vivek V. Buwa, Sirisha Parvathaneni
Publikováno v:
Powder Technology. 372:178-191
Dynamics of segregation and mixing phenomena of binary gas-solids flow in fluidized beds is predominantly influenced by the bubbling behaviour. In the present work, we have investigated experimentally the effect of the local bubbling behaviour on the
Publikováno v:
Powder Technology. 361:474-489
Particle-resolved CFD simulations are widely used for the predictions of particle-scale flow, transport processes and chemical reactions. However, the effect of turbulence models used in such simulations is not quantitatively established. In the pres
Publikováno v:
AIChE Journal. 69
Autor:
G.M. Karthik, Vivek V. Buwa
Publikováno v:
Reaction Chemistry & Engineering. 5:163-182
Particle-resolved CFD simulations are performed for four industrially important solid-catalysed gas-phase reactions (methane steam reforming (MSR), water–gas shift (WGS), and methanol (MeOH) and DME synthesis) in a fixed-bed reactor. The effect of
Autor:
Vivek V. Buwa, Karthik Gopal Manoharan
Publikováno v:
Industrial & Engineering Chemistry Research. 58:22363-22375
Structure-resolved simulations of fluid flow, heat transfer, and chemical reactions were performed to understand the effect of different catalytic structures on reactor performance using methane st...
Publikováno v:
Chemical Engineering Journal. 374:189-200
A comparison of the particle-scale PIV measurements with the corresponding particle-resolved CFD simulations in the turbulent flow regime using SST k - ω model is performed. A cylindrical packed bed containing spherical particles with the tube-to-pa