2009
DOI: 10.1016/j.compchemeng.2008.12.011
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Modeling and simulation of a pseudo-three-phase slurry bubble column reactor applied to the process of petroleum hydrodesulfurization

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Cited by 13 publications
(10 citation statements)
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“…The Reynolds-averaged Navier–Stokes (RANS) turbulence model 19 and multi-fluid model 20 were adopted to simulate the motion of the gas and the multiphase flow in the tower, respectively. For each phase, based on the conservation of mass, momentum and energy, the control equations can be derived out.…”
Section: Modeling and Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…The Reynolds-averaged Navier–Stokes (RANS) turbulence model 19 and multi-fluid model 20 were adopted to simulate the motion of the gas and the multiphase flow in the tower, respectively. For each phase, based on the conservation of mass, momentum and energy, the control equations can be derived out.…”
Section: Modeling and Methodsmentioning
confidence: 99%
“…the relationship between C Ai , gas-liquid interfacial concentration of SO 2 and P Ai can be calculated out. By solving equations (14)- (20), and substituting the value of parameters, the mass transfer rate of SO 2 , N A , can be derived finally.…”
Section: The Mass Conservation Equationmentioning
confidence: 99%
“…On the basis of using the DGD technique, various authors ,,, observed that the large gas bubbles move quickly upward through the slurry in a plug-flow manner, whereas, the small gas bubbles move slowly and are often entrained within the slurry-phase. This finding led to the development of the “two-bubble” or “bimodal” class model, which has been widely used to represent the gas bubbles in the convective and dispersive flow schemes within SBCRs , in one-dimensional (1-D) and two-dimensional (2-D) modeling of multiphase reactors. ,, …”
Section: Introductionmentioning
confidence: 99%
“…This finding led to the development of the "two-bubble" or "bimodal" class model, which has been widely used to represent the gas bubbles in the convective and dispersive flow schemes within SBCRs 31,32 in one-dimensional (1-D) and two-dimensional (2-D) modeling of multiphase reactors. 6,33,34 Critiques of the Conventional DGD Technique. It should be mentioned that despite the popularity of the bimodal class model, lumping gas bubbles into only two classes is a gross oversimplification of the complex hydrodynamics in SBCRs.…”
Section: Introductionmentioning
confidence: 99%
“…9,10 With the development of computer technology and chemical engineering, the chemical reaction calculation model of environmental engineering becomes gradually mature. Matos et al 11 developed a pseudo three-phase reactor model to simulate the process of petroleum hydrodesulfurization. Wang et al 12 and Darake et al 13 used a mathematical model to calculate the desulfurization efficiency of the pilot-scale desulfurization project, and the results meet the practical requirements.…”
Section: Introductionmentioning
confidence: 99%