2009
DOI: 10.1016/s1003-6326(08)60301-5
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Computational simulation of fluid dynamics in a tubular stirred reactor

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Cited by 19 publications
(8 citation statements)
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“…Moreover, stability problems were experienced during tracer introduction when using the RNG model [ 10 ]. For simulating the flows generated by the impeller, the multiple reference frame (MRF) method was adopted [ 7 ]. This method allows for efficient steady state flow simulation in a mixer with a rotating impeller.…”
Section: Methodsmentioning
confidence: 99%
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“…Moreover, stability problems were experienced during tracer introduction when using the RNG model [ 10 ]. For simulating the flows generated by the impeller, the multiple reference frame (MRF) method was adopted [ 7 ]. This method allows for efficient steady state flow simulation in a mixer with a rotating impeller.…”
Section: Methodsmentioning
confidence: 99%
“…By adopting this approach, the effects of the blade rotations were recorded per the reference frame. The convection term in the governing equation was modeled by a first-order scheme, and the SIMPLE algorithm was used to resolve the coupling between the velocity and the pressure parameters [ 7 ]. A 10 −4 convergence limit was set for the solution.…”
Section: Methodsmentioning
confidence: 99%
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“…This situation indicates that the tracer is not representing the fluid in the system or under estimated the calculation of theoretical MRT. Besides, study by Choi et al [ 17 ] showed that by using single Rushton in 1.3l unbaffled vessel, the optimum percentage of dead volume achieved was 7% with respective parameters, whereas no specific values of important parameters have been stated for MRT estimation by IAEA [ 13 ]; Cao et al [ 18 ]; and Furman et al [ 19 ].…”
Section: Resultsmentioning
confidence: 99%
“…However, as the inlet flow rate increases, a change in the rotational speed does not affect the mean residence time. Cao et al [ 43 ] explained that, to quantitatively understand the RTD, the experimental data have to be fitted to an adequate model, as described in Section 3 , to describe the nonideal reactor flow pattern, which will provide a better understanding of the quality of mixing, especially for reactions that are not first order. Moreover, the placement of a stirrer at the bottom of an annular reactor with an optimal speed of 150–250 rpm could narrow the RTD curve and improve the mass transfer for surface reactions.…”
Section: Computational Simulations Using Cfdmentioning
confidence: 99%