Highly Viscous Systems Maria C. Quaresima, Markus Schmidt, Andreas - - PowerPoint PPT Presentation

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Highly Viscous Systems Maria C. Quaresima, Markus Schmidt, Andreas - - PowerPoint PPT Presentation

Solvent Extraction Design for Highly Viscous Systems Maria C. Quaresima, Markus Schmidt, Andreas Pfennig mariachiara.quaresima@uliege.be Products, Environment, and Processes (PEPs) Department of Chemical Engineering Universit de Lige,


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Solvent Extraction Design for Highly Viscous Systems

Maria C. Quaresima, Markus Schmidt, Andreas Pfennig mariachiara.quaresima@uliege.be Products, Environment, and Processes (PEPs) Department of Chemical Engineering Université de Liège, Belgium www.chemeng.uliege.be

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agenda

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 motivation  extraction column design  single-drop behavior

 sedimentation  mass transfer

 conclusions and perspectives

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motivation

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 sources: fossil-based

bio-based

higher oxygen content lower vapor pressure higher viscosity  pilot-plant based design is time consuming,

expensive

 design based on lab-scale experiments

and simulations

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the ReDrop concept

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ReDrop simulation

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single-drop sedimentation

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2800 100 100 50 DN 200 camera nozzle for producing droplets rising droplet 1350 50 50 50 100 100 100

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sedimentation EFCE system

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  • M. Henschke, A.Pfennig, AIChE J., 45, 10 (1999).

1 2 3 4 5 6 7 20 40 60 80 100 120 140

rigid interface ideally mobile interface

T = 20 °C, n-butylacetate (d) + water (c) without mass transfer, Hoting (1996)

  • ur experiments

terminal velocity in mm/s drop diameter in mm

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single-drop sedimentation

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rigid drop circulating drop

  • scillating drop

deformed drop

dSW αSW a16 a15

  • M. Henschke, A.Pfennig, AIChE J., 45, 10 (1999).

1 2 3 4 5 6 7 20 40 60 80 100 120 140

terminal velocity in mm/s drop diameter in mm

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single-drop sedimentation

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4 adjustable parameters: dSW a15 a16 αSW

system αSW Henschke d: n-butyl acetate c: water 10 Kalem et al. d: isododecane + D2EHPA c: water + Zn + H2SO4 2 Adinata d: toluene + paraffin c: water + PEG 5

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increasing viscosity of EFCE system

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continuous phase dispersed phase water n-butyl acetate + polyethylene glycol (PEG) + paraffin oil acetone

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sedimentation velocity

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αSW dSW

low viscous system

10 2.39

this system

5.44 4.28

d: n-butyl acetate, viscosity 0.797 mPas c: water + PEG, viscosity 7.928 mPas

T=20°C

Henschke model

2 4 6 15 30 45 60 75 90

sedimentation velocity in mm/s drop diameter in mm

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single-drop mass transfer

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ATPS mass transfer

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  • F. Buchbender, M. Schmidt, T. Steinmetz, A. Pfennig,
  • Chem. Ing. Tech., 84, (4) 540-546 (2012)

10 20 30 40 50 60 70 0.9 1

dimensionless driving concentration difference y + residence time in s

exp calc diameter 1.24 mm 1.42 mm 1.56 mm c: phosphate buffer, viscosity 2.145 mPas d: PEG, viscosity 9.250 mPas mass-transfer component: protein albumin

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conclusions and perspectives

 viscosity influence on mass transfer  fitting of models parameter  further investigation of viscosity

dependency

 implementing adapted models in

simulation

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Solvent Extraction Design for Highly Viscous Systems

Maria C. Quaresima, Markus Schmidt, Andreas Pfennig mariachiara.quaresima@uliege.be Products, Environment, and Processes (PEPs) Department of Chemical Engineering Université de Liège, Belgium www.chemeng.uliege.be