2015
DOI: 10.1016/j.cep.2015.02.003
|View full text |Cite|
|
Sign up to set email alerts
|

Liquid backmixing in an inclined rotating tubular fixed bed reactor – Augmenting liquid residence time via flow regime adjustment

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
2
1

Citation Types

0
12
0
1

Year Published

2015
2015
2020
2020

Publication Types

Select...
5
1

Relationship

3
3

Authors

Journals

citations
Cited by 13 publications
(13 citation statements)
references
References 29 publications
0
12
0
1
Order By: Relevance
“…Apart from these works, some researchers paid more attention to comprehensively study the effect of different tilt angles on the hydrodynamics prevailing inside stationary packed beds in three gas–liquid contacting modes, namely, cocurrent downward, cocurrent upward, and countercurrent or when cocurrent downflow slanted packed beds are subjected to axial vessel rotations …”
Section: Introductionmentioning
confidence: 99%
“…Apart from these works, some researchers paid more attention to comprehensively study the effect of different tilt angles on the hydrodynamics prevailing inside stationary packed beds in three gas–liquid contacting modes, namely, cocurrent downward, cocurrent upward, and countercurrent or when cocurrent downflow slanted packed beds are subjected to axial vessel rotations …”
Section: Introductionmentioning
confidence: 99%
“…The liquid back mixing in the inclined rotating tubular fixed bed reactor was investigated in another study [41]. Due to increasing transverse forces, an increase in axial dispersion with rotational velocity was observed.…”
Section: Analysis Of the Reaction Under Rotationmentioning
confidence: 98%
“…Härting et al [34][35][36] reported that the superimposed rotation of previously inclined packed beds leads to cyclic wetting/dewetting mode of operation at the expense of gas-liquid segregation and emergence of stratified flow pattern in the bed (Fig. 9 a).…”
Section: Potential Methods For Process Intensificationmentioning
confidence: 99%
“…Recently, two new reactor concepts have been introduced for process intensification of conventional cocurrent two-phase flow packed-bed reactors: (i) inclined rotating reactor [34][35][36] and (ii) low-shear rotation of the vertical reactor [37]. Härting et al [34][35][36] reported that the superimposed rotation of previously inclined packed beds leads to cyclic wetting/dewetting mode of operation at the expense of gas-liquid segregation and emergence of stratified flow pattern in the bed (Fig.…”
Section: Potential Methods For Process Intensificationmentioning
confidence: 99%