| 000 | 01687nam a2200253Ia 4500 | ||
|---|---|---|---|
| 003 | MX-MdCICY | ||
| 005 | 20250626080926.0 | ||
| 040 | _cCICY | ||
| 090 | _aB-20567 | ||
| 245 | 1 | 0 | _aConsiderations about the gas fraction in two-phase electrochemical reactors by using a rigorous hydrodynamic model |
| 490 | 0 | _aChemical Engineering Science, 276, 118699, 2023 | |
| 500 | _aArtÃculo | ||
| 520 | 3 | _aThe experimental evidence that a limiting value of gas fraction is achieved in a gas-liquid dispersion as the gas volumetric flow rate is increased is explained by means of a rigorous hydrodynamic model. The mathematical treatment, based on the Eulerian concept applied to each phase, considers a population balance with a range of bubble sizes allowing the coalescence and breakup between them; and it is implemented in the OpenFOAM framework. It is concluded that the limiting gas fraction is a consequence of the increase of the gas velocity and the constancy of the drag term of the interfacial exchange moment as the volumetric gas flow is enlarged. A simplified hydrodynamic model is also reported that closely matches both the rigorous one and the experimental results under limiting operating conditions. | |
| 650 | 1 | 4 | _aELECTROCHEMICAL REACTORS |
| 650 | 1 | 4 | _aGAS-EVOLVING ELECTRODES |
| 650 | 1 | 4 | _aGAS-LIQUID FLOW |
| 650 | 1 | 4 | _aOPENFOAM |
| 650 | 1 | 4 | _aTWO-PHASE HYDRODYNAMICS |
| 700 | 1 | 2 | _aColli, A. N. |
| 700 | 1 | 2 | _aBisang, J. M. |
| 856 | 4 | 0 |
_uhttps://drive.google.com/file/d/1y3t7_qEX69B4YhQK0nbuG3ijAOQqZE2V/view?usp=drive_link _zPara ver el documento ingresa a Google con tu cuenta: @cicy.edu.mx |
| 942 |
_2Loc _cREF1 |
||
| 008 | 250602s9999 xx |||||s2 |||| ||und|d | ||
| 999 |
_c55593 _d55593 |
||