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Ultrafiltration of protein based solution: Study of membrane - - PowerPoint PPT Presentation

6 th International Conference on Sustainable Solid Waste Management NAXOS 2018 Ultrafiltration of protein based solution: Study of membrane fouling Simona M.Miron, Patrick Dutourni, Arnaud Ponche Institut de Science des Matriaux de


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Simona M.Miron, Patrick Dutournié, Arnaud Ponche

21/06/2018 1 Institut de Science des Matériaux de Mulhouse (IS2M), UMR 7361 CNRS, Université de Strasbourg, Université de Haute Alsace, 3 bis rue A. Werner, 68098 Mulhouse Cedex, France

Ultrafiltration of protein based solution: Study of membrane fouling

NAXOS 2018

6th International Conference

  • n

Sustainable Solid Waste Management

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Outline

  • Introduction
  • Study cases
  • 1. Study of interactions between biomolecules and material

through cross‐flow filtration ‐ Study of fouling behavior

  • 2. Study of biological activity of the filtrated solutions
  • Conclusions

Introduction Materials and methods Results and discussion Conclusions and future work

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Water and wastewater treatment

Ultrafiltration

Membrane process Food and diary industry

Introduction Materials and methods Results and discussion Conclusions and future work

Separate, concentrate, rectify and purify Biopharmaceutical industry

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Part 1. Study of interactions between biomolecules and material through cross‐flow filtration Study of fouling behavior

Introduction Materials and methods Results and discussion Conclusions and future work

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Ribbon diagram of HEWL

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Hen egg white lysozyme ‐ enzyme with 129 amino acids ‐ antimicrobial activity against Gram‐positive bacteria

Introduction Materials and methods Results and discussion Conclusions and future work

Amino acid L-tyrosine  Elementary constituent of Lysozyme Neutral solution Vitamin B12  Used for membrane performances investigation (Mean pore radius calculation using Nernst-Plank model)

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Introduction Materials and methods Results and discussion Conclusions and future work

Membrane Membrane Permeate Retentate Feed Membrane characteristics: ‐ ultrafiltration membrane ‐ bilayer membrane of TiO2 ‐ asymmetrical pore structure ‐ cut‐off 1 kDa Membrane performances:

  • 1. Selectivity performances:

rejection rate (R)

  • 2. Hydraulic performances:

permeability (Lp)

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N° Test Solution R max (%) Calculated Pore radius (nm) Lp (10‐14m3.m‐2

memb)

Pure water after conditioning step 6.2 1 L‐tyrosine 5 4.7 2 VB12 57 1.61 4.1 3 Lysozyme 85 3.6 4 Lysozyme 93 3.3 5 VB12 75 1.27 3.2 6 Lysozyme 98 3.1 7 VB12 86 1.09 2.4 8 L‐tyrosine 6.5 2.3

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Introduction Materials and methods Results and discussion Conclusions and future work

Decrease in lysozyme transmission and in hydraulic permeability  adsorption ? Pore clogging ?

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30 40 50 60 70 80 90 0,0E+00 2,0E‐05 4,0E‐05 6,0E‐05 8,0E‐05

Rejection rate (%) Permeation flux (m3.m‐2 .s‐1 )

test 3 test 6 test 10

rp = 1.61 nm rp = 1.27 nm rp = 1.09 nm

Membrane selectivity increases, hydraulic performances decreases calculated pore radius decreases

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Introduction Materials and methods Results and discussion Conclusions and future work

Test 2 Test 5 Test 7

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Introduction Materials and methods Results and discussion Conclusions and future work

  • membrane hydraulic performances
  • selectivity properties
  • lysozyme transmission and hydraulic permeability

Adsorption of protein pore clogging

  • Tyrosine filtration after Lysozyme – no variation
  • Tyrosine filtration before lysozyme (clean membrane) - significant effect

 Adsorption

  • f

lysozyme in pores increases selectivity and decreases hydraulic performances. Conclusions from filtration tests

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No modification of the lysozyme molecule (no time/ shear stress effect)

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Introduction Materials and methods Results and discussion Conclusions and future work

7 8 9 10 11 12 13 14 15 20 40 60 80 100

9.81 Response[mAU]

Retention time (min)

Lysozyme reference sample Lysozyme II Membrane M2 pressure 4 bar Lysozyme II Membrane M2 pressure 6 bar Lysozyme II Membrane M2 pressure 8 bar Lysozyme II Membrane M2 pressure 10 bar Lysozyme II Membrane M2 pressure 12 bar

HPLC analysis of lysozyme Retentate

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7 8 9 10 11 12 13 14 15 0,0 0,2 0,4 0,6 0,8 1,0

10.22 9.81

Normalized response Retention time (min)

Lysozyme reference sample Lysozyme II Membrane M2 pressure 4 bar Lysozyme II Membrane M2 pressure 6 bar Lysozyme II Membrane M2 pressure 8 bar Lysozyme II Membrane M2 pressure 10 bar Lysozyme II Membrane M2 pressure 12 bar

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Introduction Materials and methods Results and discussion Conclusions and future work

HPLC analysis of lysozyme Permeate Modification

  • f

the lysozyme molecule after permeation (denaturated)

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  • f denatured population of molecules after filtration

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Introduction Materials and methods Results and discussion Conclusions and future work

HPLC analysis of lysozyme

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Part 2. Study of biological activity of the filtrated solutions

Introduction Materials and methods Results and discussion Conclusions and future work

Lysozyme Micrococcus lysodeikticus

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Retentate shows slightly higher activity than permeate

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Sample Unit/mg Loss of activity Native 83 926 ‐ Retentate 85 528 ‐ Permeate 68 929 20 %

Introduction Materials and methods Results and discussion Conclusions and future work

100 200 300 400 0,20 0,25 0,30 0,35 0,40

Abs (450nm) Time [s]

Retentate Native Permeate

Lysozyme assay

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Conclusions/observations

  • Protein

adsorption in larger pores (modification

  • f

membrane performances‐> Partial fouling)

  • HPLC

: 2 populations

  • f

lysozyme with different hydrodynamic radii in retentate and permeate (denaturation)

  • Loss of conformation not correlated to a huge diminution of

bacterial activity

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Introduction Materials and methods Results and discussion Conclusions and future work

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W

Σας ευχαριστώ για την προσοχή σας Thank you for your attention Vă mulţumesc pentru atenţie

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Simona M.Miron, Patrick Dutournié, Arnaud Ponche

21/06/2018 17 Institut de Science des Matériaux de Mulhouse (IS2M), UMR 7361 CNRS, Université de Strasbourg, Université de Haute Alsace, 3 bis rue A. Werner, 68098 Mulhouse Cedex, France

Ultrafiltration of protein based solution: Study of membrane fouling

NAXOS 2018

6th International Conference

  • n

Sustainable Solid Waste Management