Michele Marigo

Dr. Michele Marigo


Research Focus & Metrics

Academic Career Length

14Years (2013-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 April 2017 in Powder Technology
Verified
Journal Article
Closed access
SPStefan Pantaleev
Stefan Pantaleev
SYSlavina Yordanova
Slavina Yordanova
AJAlvaro Janda
Alvaro Janda
MMMichele Marigo
Michele Marigo
JOJin Y. Ooi
Jin Y. Ooi

1 November 2016 in International Journal of Pharmaceutics
Verified
Journal Article
Closed access
Zilin YanZilin Yan
Zilin Yan
SWSam K. Wilkinson
Sam K. Wilkinson
ESEdmund H. Stitt
Edmund H. Stitt
MMMichele Marigo
Michele Marigo

1 March 2013 in International Journal of Pharmaceutics
Verified
Journal Article
Closed access
MMMichele Marigo
Michele Marigo
MDM. Davies
M. Davies
TLTom Leadbeater
Tom Leadbeater
DCD.L. Cairns
D.L. Cairns
AIA. Ingram
A. Ingram
ESE.H. Stitt
E.H. Stitt

1 August 2020 in Minerals Engineering
Verified
Journal Article
Closed access
DDDomenico Daraio
Domenico Daraio
JVJose Villoria
Jose Villoria
AIAndrew Ingram
Andrew Ingram
AAAlessio Alexiadis
Alessio Alexiadis
ESE. Hugh Stitt
E. Hugh Stitt
MMMichele Marigo
Michele Marigo

11 November 2019 in Applied Sciences
Verified
Journal Article
Open access
PDF file
DDDomenico Daraio
Domenico Daraio
JVJose Villoria
Jose Villoria
AIAndy Ingram
Andy Ingram
Alessio AlexiadisAlessio Alexiadis
Alessio Alexiadis
ESEdmund Hugh Stitt
Edmund Hugh Stitt
MMMichele Marigo
Michele Marigo
Positron emission particle tracking (PEPT) was used to investigate the grinding media dynamics in a laboratory-scale attritor mill in the absence of powder. The grinding media motion was analysed as a function of the equipment’s typical operating parameters: impeller speed, impeller clearance and bead fill level. It was observed that the impeller speed had the strongest influence on the media motion. An increase of the impeller speed from 300 rpm to 600 rpm led to a change in the bead recirculation patterns with the increasing formation of well segregated upper and lower recirculation loops that fully developed at the maximum speed of 600 rpm. For a constant impeller speed, an increase of the bead loading did not majorly affect the bead velocity as remarked by minor changes on the flow field. For all the impeller clearance values, the occupancy plots revealed an inefficient dead region at the bottom of the attritor where the beads were moving at very low velocity. In this region the beads were tightly packed under their own weight and, furthermore, there was an absence of direct contact with the impeller arms. The depth of this region increased proportionally to the distance between the bottom of the impeller and the vessel base indicating that a minimum value of clearance should be set to optimise the lower recirculation pattern. For two experimental conditions, the data generated by PEPT measurements were utilised to set-up a friction-adjusted discrete element method (DEM) model. Here, the simulation results were qualitatively and quantitatively compared against the PEPT data by assessing the averaged velocity flow fields and the average velocity profiles at different radial locations inside the vessel. Given the intrinsic uncertainty of the PEPT measurements, the DEM model results were in considerably good agreement with the experimental results. The major discrepancy was observed close to the vessel wall where the simulations overpredicted the velocity by about 10%.

1 February 2020 in Chemical Engineering Science
Verified
Journal Article
Closed access
MMMichele Marigo
Michele Marigo
JXJiansheng Xiang
Jiansheng Xiang
JLJohn-Paul Latham
John-Paul Latham
MCM. Carlsson
M. Carlsson
ESE.H. Stitt
E.H. Stitt
MMM. Marigo
M. Marigo