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EVALUATION OF FINE SAND FILTRATION FOR 
LARGE SCALE ALGINATE PURIFICATION FOR CLINICAL USE 
T. GREGO,1 A. GANDER,2 DR C. SELDEN,2 PROF H. J. F. HODGSON,2 DR L. C. CAMPOS1 
1 Civil, Environmental & Geomatic Engineering Department, University College London 
2 Centre for Hepatology, Royal Free Campus, Royal Free & University College Medical School 
INTRODUCTION 
Alginate is a natural biopolymer extracted from brown seaweed, in this project, alginate was 
used to microencapsulate HepG2 cells (a human hepatocyte immortal cell line) for use in a 
Bioartificial Liver device (Figure 1.). 
Alginate may contain “unknown” (e.g. micron particulates) and “known” (e.g. heavy metals, 
endotoxins, proteins, pyrogens, and polyphones') contaminants [1-2]. Therefore, 
biocompatibility of alginates for immobilising hepatocytes is crucial. Other purification methods 
achieved a suitable biocompatibility of the polymer by removing the known impurities, but were 
not appropriate for our application. 
Figure 1. The three stages of the BAL system [3] 
Stage 1 HepG2 cells are encapsulated in alginate beads achieving a 3D state, which provides better cell growth and function [4]. 
Stage 2 Encapsulated cells are proliferated in a Fluidised Bed Bioreactor (FBB) over 8-10 days; 
Stage 3 patient plasma is passed over beads by fluidisation. 
“(i.) FDA stained HepG2 cells after encapsulation. (ii.) FDA stained HepG2 cells after 8 days of proliferation. (iii.) A phase contrast alginate beads 8 days after initial 
immobilisation. (iv.) Fluidised Bed Bioreactor (FBB) competence culture setup. (v.) FBB containing alginate” [3]. 
HYPOTHESIS AND AIMS 
Hypothesis: For clinical application and regulatory authority approval, particulates 
must be removed to prevent transit to the patient. Therefore, we seek to purify raw 
sodium alginate solution removing micron particulate impurities by fine sand filtration 
without altering the viscosity of the resulting solution. 
The specific aims of the research project were: 
•To remove micro particulates between 1μm and 10μm in size. 
•To evaluate the effect of fine sand filtration on the sodium alginate properties. 
•To determine and measure any changes in the physical properties of the non-Newtonian fluid 
by rheology. 
•Encapsulate empty alginate beads to assess morphology of beads after filtration. 
•To immobilise encapsulated HepG2 cells in filtered alginate solution comparing cell growth, 
viability and function. 
METHODOLOGY 
RESULTS 
Figure 6. Proliferation of encapsulated HepG2 
cells in 1.875% alginate beads over 14 days 
20 
15 
10 
5 
CONCLUSION 
(B) 
(C) 
10 
8 
6 
4 
2 
0.350 
0.300 
0.250 
0.200 
0.150 
0.100 
0.050 
0.35 
0.30 
0.25 
0.20 
0.15 
0.10 
0.05 
• Filtering sodium alginate solution through a dual media filter could eliminate micron 
particulates between 10 to 20μm, and reduced by 94% 2μm particulates compared to non 
filtered Na-alginate solution. 
• The filtration process had a major impact on the dynamic viscosity of the solution, even 
though the micron particulates were removed to some extent. As a consequence of this, the 
stability and the morphology of the beads were adversely affected. 
• Immobilisation of HepG2 cells in fine sand filtered, aqueous sodium alginate did not provide 
a coherent gel matrix to support cell growth. 
RECOMMENDATIONS 
The experimental works were evaluated not only by engineering and medical science aspects 
but also the efficiency of the currently publish purification processes were taken into 
consideration [2]. Therefore, a key question was addressed: 
“Is the liquid-solid based purification method the most appropriate for the purification of “micron 
particulates free” alginate biopolymer suitable for cell encapsulation?” 
The research outcomes highlighted the need for an alternative approach for alginate 
purification. One possibility would be utilising dry alginate powder in a cyclonic separation from 
gas stream and possible production of “micron particulate free” alginate for cell encapsulation 
[5]. 
REFERENCES 
Figure 2. Life cycle of the experimental work 
Phase I. Fine sand filtration (single and dual media filter): to remove macro particulates 
from raw Na-alginate. 
Phase II. Lyophilisation 0.2% filtered alginate solution was shell frozen in a dry ice 
acetone bath, to be lyophilised to sublimate water, leaving dry alginic acid salt. 
Phase III. Reconstitution of alginate to final concentration of 1.0%, 1.25%, 1.5%, 1.75%, 
1.875% and 2%, and autoclaving for 10 mins at 121°C. 
Phase III-B. Physical analysis: to determine the particle size distribution and to measure 
the viscosity of the filtered 2% NaAlg solutions. 
Phase IV. Biological analysis: HepG2 cell encapsulation in 1.875% alginate beads using 
Inotech® encapsulator. 
Figure 3. Particle Size and Number distributions of 
alginate powder with Different Filtration Methods 
Figure 4. Effects of fine sand filtration on the viscosity of 
0.2% Na-alginate solutions 
Figure 5. Effects of fine sand and dual (fine and coarse sands) 
media filtration on the viscosity of 0.2% Na-alginate solutions 
(A) 
(A) Encapsulated HepG2 cells in fine sand (RH110) filtered 
1.875% sodium alginate solution, phase contrast on day 9; 
(B) Viability of cells on day 9, estimated by vital dye staining 
(C) Dead cells as estimated by propidium iodide 
(cell permeability). 
Green shows live cells, and red represent dead cells. 
0.000 
0.00 0.09 0.17 0.25 0.34 0.44 0.51 0.70 0.68 
Shear stress (Pa) 
Dinamic viscosity (Pa s) 
0.2% Control NaAlg solution (non filtered, 
freeze-dried, and autoclaved) 
0.2% NaAlg filtered (RH-70) solution, 
freeze-dried and autoclaved 
0.2% NaAlg filtered (RH-110) solution, 
freeze-dried and autoclaved 
0.00 
1 29 59 89 118 148 177 207 237 
Shear rate (1/s) 
Dinamic viscosity (Pa s) 
0.2% Unfiltered NaAlg (control) solution 
0.2% Filtered (fine sand RH-110) NaAlg 
solution 
0.2% Filtered (fine and coarse sands) 
NaAlg solution 
1. Dusseault, J., et. al. ‘Evaluation of alginate purification methods: Effect on polyphenols, endotoxin, and protein contamination’ (2005) DOI: 10.1002/jbm.a.30541 
2. van de Ven, W. J. C., et. al. ‘Hollow fibre dead-end ultrafiltration: Influence of ionic environment on filtration of alginates. (2008) 
Journal of Membrane Science pp 218-229 
3. Jones, J. The removal of toxic lactate levels using Immobilised lactate oxidase within a Bioartificial Liver. Research Department of Structural and Molecular Biology, 
Division of Bioscience (unpublished work) 
0 
2 5 10 15 
Particle size (μm) 
Particle Number in 1g Dry Alginate (x 10 6) 
non filtered non autoclaved 
non filtered autoclaved 
Dual Media Filter-I. 
Mono Media Filter-III 
RH110/VI Sand 
RH70/VII Sand 
0 
0 2 4 6 8 10 12 14 
Days 
Cell number (x 10 6) 
Dual Sand Media 
Filter 
Mono Layer Media 
Non-Filtered Alginate 
4. Damelin, L. H., et. al. (2007) ‘Fat-Loaded HepG2 Spheroids Exhibit Enhanced Protection From Pro-Oxidant and Cytokine Induced Damage’. Journal of Cellular 
Biochemistry. 101:723-734. 
5. Hoffmann, A. C. and Stein, L. E. (2007) ‘Gas Cyclones and Swirl Tubes: Principles, Design, and Operation’. Springer.

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Timea Grego's Poster_ MSc ESE Dissertation2009

  • 1. EVALUATION OF FINE SAND FILTRATION FOR LARGE SCALE ALGINATE PURIFICATION FOR CLINICAL USE T. GREGO,1 A. GANDER,2 DR C. SELDEN,2 PROF H. J. F. HODGSON,2 DR L. C. CAMPOS1 1 Civil, Environmental & Geomatic Engineering Department, University College London 2 Centre for Hepatology, Royal Free Campus, Royal Free & University College Medical School INTRODUCTION Alginate is a natural biopolymer extracted from brown seaweed, in this project, alginate was used to microencapsulate HepG2 cells (a human hepatocyte immortal cell line) for use in a Bioartificial Liver device (Figure 1.). Alginate may contain “unknown” (e.g. micron particulates) and “known” (e.g. heavy metals, endotoxins, proteins, pyrogens, and polyphones') contaminants [1-2]. Therefore, biocompatibility of alginates for immobilising hepatocytes is crucial. Other purification methods achieved a suitable biocompatibility of the polymer by removing the known impurities, but were not appropriate for our application. Figure 1. The three stages of the BAL system [3] Stage 1 HepG2 cells are encapsulated in alginate beads achieving a 3D state, which provides better cell growth and function [4]. Stage 2 Encapsulated cells are proliferated in a Fluidised Bed Bioreactor (FBB) over 8-10 days; Stage 3 patient plasma is passed over beads by fluidisation. “(i.) FDA stained HepG2 cells after encapsulation. (ii.) FDA stained HepG2 cells after 8 days of proliferation. (iii.) A phase contrast alginate beads 8 days after initial immobilisation. (iv.) Fluidised Bed Bioreactor (FBB) competence culture setup. (v.) FBB containing alginate” [3]. HYPOTHESIS AND AIMS Hypothesis: For clinical application and regulatory authority approval, particulates must be removed to prevent transit to the patient. Therefore, we seek to purify raw sodium alginate solution removing micron particulate impurities by fine sand filtration without altering the viscosity of the resulting solution. The specific aims of the research project were: •To remove micro particulates between 1μm and 10μm in size. •To evaluate the effect of fine sand filtration on the sodium alginate properties. •To determine and measure any changes in the physical properties of the non-Newtonian fluid by rheology. •Encapsulate empty alginate beads to assess morphology of beads after filtration. •To immobilise encapsulated HepG2 cells in filtered alginate solution comparing cell growth, viability and function. METHODOLOGY RESULTS Figure 6. Proliferation of encapsulated HepG2 cells in 1.875% alginate beads over 14 days 20 15 10 5 CONCLUSION (B) (C) 10 8 6 4 2 0.350 0.300 0.250 0.200 0.150 0.100 0.050 0.35 0.30 0.25 0.20 0.15 0.10 0.05 • Filtering sodium alginate solution through a dual media filter could eliminate micron particulates between 10 to 20μm, and reduced by 94% 2μm particulates compared to non filtered Na-alginate solution. • The filtration process had a major impact on the dynamic viscosity of the solution, even though the micron particulates were removed to some extent. As a consequence of this, the stability and the morphology of the beads were adversely affected. • Immobilisation of HepG2 cells in fine sand filtered, aqueous sodium alginate did not provide a coherent gel matrix to support cell growth. RECOMMENDATIONS The experimental works were evaluated not only by engineering and medical science aspects but also the efficiency of the currently publish purification processes were taken into consideration [2]. Therefore, a key question was addressed: “Is the liquid-solid based purification method the most appropriate for the purification of “micron particulates free” alginate biopolymer suitable for cell encapsulation?” The research outcomes highlighted the need for an alternative approach for alginate purification. One possibility would be utilising dry alginate powder in a cyclonic separation from gas stream and possible production of “micron particulate free” alginate for cell encapsulation [5]. REFERENCES Figure 2. Life cycle of the experimental work Phase I. Fine sand filtration (single and dual media filter): to remove macro particulates from raw Na-alginate. Phase II. Lyophilisation 0.2% filtered alginate solution was shell frozen in a dry ice acetone bath, to be lyophilised to sublimate water, leaving dry alginic acid salt. Phase III. Reconstitution of alginate to final concentration of 1.0%, 1.25%, 1.5%, 1.75%, 1.875% and 2%, and autoclaving for 10 mins at 121°C. Phase III-B. Physical analysis: to determine the particle size distribution and to measure the viscosity of the filtered 2% NaAlg solutions. Phase IV. Biological analysis: HepG2 cell encapsulation in 1.875% alginate beads using Inotech® encapsulator. Figure 3. Particle Size and Number distributions of alginate powder with Different Filtration Methods Figure 4. Effects of fine sand filtration on the viscosity of 0.2% Na-alginate solutions Figure 5. Effects of fine sand and dual (fine and coarse sands) media filtration on the viscosity of 0.2% Na-alginate solutions (A) (A) Encapsulated HepG2 cells in fine sand (RH110) filtered 1.875% sodium alginate solution, phase contrast on day 9; (B) Viability of cells on day 9, estimated by vital dye staining (C) Dead cells as estimated by propidium iodide (cell permeability). Green shows live cells, and red represent dead cells. 0.000 0.00 0.09 0.17 0.25 0.34 0.44 0.51 0.70 0.68 Shear stress (Pa) Dinamic viscosity (Pa s) 0.2% Control NaAlg solution (non filtered, freeze-dried, and autoclaved) 0.2% NaAlg filtered (RH-70) solution, freeze-dried and autoclaved 0.2% NaAlg filtered (RH-110) solution, freeze-dried and autoclaved 0.00 1 29 59 89 118 148 177 207 237 Shear rate (1/s) Dinamic viscosity (Pa s) 0.2% Unfiltered NaAlg (control) solution 0.2% Filtered (fine sand RH-110) NaAlg solution 0.2% Filtered (fine and coarse sands) NaAlg solution 1. Dusseault, J., et. al. ‘Evaluation of alginate purification methods: Effect on polyphenols, endotoxin, and protein contamination’ (2005) DOI: 10.1002/jbm.a.30541 2. van de Ven, W. J. C., et. al. ‘Hollow fibre dead-end ultrafiltration: Influence of ionic environment on filtration of alginates. (2008) Journal of Membrane Science pp 218-229 3. Jones, J. The removal of toxic lactate levels using Immobilised lactate oxidase within a Bioartificial Liver. Research Department of Structural and Molecular Biology, Division of Bioscience (unpublished work) 0 2 5 10 15 Particle size (μm) Particle Number in 1g Dry Alginate (x 10 6) non filtered non autoclaved non filtered autoclaved Dual Media Filter-I. Mono Media Filter-III RH110/VI Sand RH70/VII Sand 0 0 2 4 6 8 10 12 14 Days Cell number (x 10 6) Dual Sand Media Filter Mono Layer Media Non-Filtered Alginate 4. Damelin, L. H., et. al. (2007) ‘Fat-Loaded HepG2 Spheroids Exhibit Enhanced Protection From Pro-Oxidant and Cytokine Induced Damage’. Journal of Cellular Biochemistry. 101:723-734. 5. Hoffmann, A. C. and Stein, L. E. (2007) ‘Gas Cyclones and Swirl Tubes: Principles, Design, and Operation’. Springer.