Zobrazeno 1 - 10
of 42
pro vyhledávání: '"K. Ekambara"'
Publikováno v:
International Journal of Chemical Engineering, Vol 2012 (2012)
Modelling of gas-liquid bubbly flows is achieved by coupling a population balance equation with the three-dimensional, two-fluid, hydrodynamic model. For gas-liquid bubbly flows, an average bubble number density transport equation has been incorporat
Externí odkaz:
https://doaj.org/article/4b278e4c0e764380af3c8d40acc453eb
Publikováno v:
AIChE Journal. 60:3596-3613
Crystallization processes in a 500 mL stirred tank crystallizer with computational fluid dynamics (CFD) and population balances toward estimating how crystal size distributions (CSDs) are influenced by flow inhomogeneities was explored. The flow patt
Autor:
Jyeshtharaj B. Joshi, Sagar S. Deshpande, Mayur J. Sathe, K. Ekambara, Zoheb Khan, Channamallikarjun S. Mathpati
Publikováno v:
Chemical Engineering Science. 66:3087-3107
The bubble column reactors are usually operated in a heterogeneous regime where the liquid phase turbulence is generated by the bubble motion and the velocity gradients in the mean motion. The turbulent flow comprises of fluid elements moving in a ra
Autor:
M.T. Dhotre, K. Ekambara
Publikováno v:
Nuclear Engineering and Design. 240:963-969
Three-dimensional simulations of gas–liquid flow in the bubble column using the Euler–Euler approach is presented. The attempt is made to assess the performance and applicability of different turbulence models namely, k – ɛ , k – ɛ RNG, k
Publikováno v:
Industrial & Engineering Chemistry Research. 48:8159-8171
The behavior of horizontal solid−liquid (slurry) pipeline flows was predicted using a transient three-dimensional (3D) hydrodynamic model based on the kinetic theory of granular flows. Computationa...
Publikováno v:
Chemical Engineering Journal. 144:277-288
The internal phase distribution of co-current, air-water bubbly flow in a 50.3 mm i.d. horizontal pipeline has been modeled using the volume averaged multiphase flow equations. Liquid and gas volumetric superficial velocities varied in the range from
Publikováno v:
Industrial & Engineering Chemistry Research. 47:8505-8516
In this paper, we have presented a comprehensive analysis of the development of flow pattern in a bubble column reactor by the introduction of a population balance equation combined with the three-dimensional two-fluid model (Reynolds stress model).
Autor:
K. Ekambara, Jyeshtharaj B. Joshi
Publikováno v:
Scopus-Elsevier
A three-dimensional CFD model has been developed to predict liquid phase velocities in bubble columns. An agreement was observed between the predicted and the experimental data available in the published literature. The validated CFD model has been e
Autor:
M.T. Dhotre, K. Ekambara
Publikováno v:
Chemical Engineering Science. 62:7205-7213
In the present work, an attempt has been made to combine population balance and a CFD approach for simulating the flow in oscillatory baffled column (OBC). Three-dimensional Euler–Euler two-fluid simulations are carried out for the experimental dat
Publikováno v:
Chemical Engineering Science. 62:1049-1072
A comprehensive analysis of the development of flow pattern in a bubble column reactor is presented here through extensive LDA measurements and CFD predictions. In the LDA measurements, the simultaneous measurements of 2D velocity-time data were carr