Spinning around: from molecules to particles and …...partition Chromatography Facilities: 4 Labs...

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Spinning around: from molecules to particles and beyond Dr Svetlana Ignatova Advanced Bioprocessing Centre (ABC) Chemical Engineering Department, CEDPS Brunel University London [email protected]

Transcript of Spinning around: from molecules to particles and …...partition Chromatography Facilities: 4 Labs...

Page 1: Spinning around: from molecules to particles and …...partition Chromatography Facilities: 4 Labs (Analytical, Applications’ , Biological, Hazards’ Labs) Dynamic Extractions Ltd

Spinning around:

from molecules to particles and

beyond

Dr Svetlana Ignatova

Advanced Bioprocessing Centre (ABC)

Chemical Engineering Department, CEDPS

Brunel University London

[email protected]

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Brunel University London

Advanced Bioprocessing Centre (ABC)

separation technologies based centre Formally opened on April 25th 2006

Aim:

“To act as a focus for Brunel’s research on bioprocessing,

establishing it as an international centre of excellence and

the first point of contact for both academia and industry when

facing challenging separation problems”

Core technology:

Liquid-liquid dynamic extraction in fluctuating g-field known as Counter-current Chromatography & Centrifugal

partition Chromatography

Facilities: 4 Labs

(Analytical, Applications’ , Biological, Hazards’ Labs)

Dynamic Extractions Ltd (Wales, UK) since 2003

www.dynamicextractions.com 2

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Brunel University London

Engineering

Fluid dynamics

& Modelling

Materials

Biology & Chemistry

Multidisciplinary Research @ ABC

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Identification

Analysis

Bioassay

Pharmaceutical studies

Clinical studies

New medicine

Separation/ purification of target

compound(s)/bioparticles

From Bioactive Compounds to a Medicine

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Brunel University London

Target purification & impurities removal

Pharmaceuticals

Target concentration is high

Stable in Organic solvents

Easy recovery from fractions

Bioactivity is not affected

Natural product

Target concentration is low/medium/high

Crude Stable in Organic solvents

Extract is well balanced buffer system

Easy recovery from fractions

Bioactivity might be affected

Biopharmaceuticals

Target concentration is low

Stability has to be carefully guided

Recovery can be complicated

Bioactivity can be compromised

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Brunel University London

Biopharmaceutical manufacturing technology

flowchart (upstream and downstream bioprocesses)

A. Faustino Jozala, et al. Brazilian Journal of Microbiology, 47S, 2016, 51–63

Chromatography

Chromatography

Final

product

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Brunel University London

CCC/CPC Instrument schematics

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Multilayer column

CPC rotor

&

chambers

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Brunel University London

ABC facilities:

Dynamic Extractions CCC instruments

Mini Spectrum Midi Maxi

Coil volume (mL) 20 22 and 132 1000 4600 or 18000

Flow rate (mL/min) 0.5-2 0.5 - 12 10-80 500 - 1500

Loading (g/run) Up to 200mg Up to 2 5 to 40 20 to 700

Rotational speed

@240g (RPM)*

2100 1600 1400 600*

Elution time for D=1

component (min)

20 20 20 20

*Maxi currently runs at 120g

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Brunel University London

ABC facilities: from analytical to pilot scale,

4.6 & 18L MAXI-centrifuges

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Brunel University London

ABC:

Contract Research & Academic Investigations

• Natural product purifications

• Continuous processing & Scale up

• Small molecules

• Screening for novel metabolites

• Pharmaceutical waste stream purification

• Cell, Virus & other Bioparticles separations

• Biopharmaceuticals (incl Antibody-based products)

• Bioreactor/separator for enantiomer conversion

• Biofuels from non-food resources

• Nanomaterials

• Biorefinery (monosaccharides separation from SBP)

• Technology development for novel applications

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Brunel University London

Liquid nature of stationary phase:

removal of bulk impurities

Fractionation of Brazilian red propolis crude

extracts

with

Dr Begoña Gimenez-Cassina &

Prof Alexandra C H F Sawaya at the University of

Campinas (UNICAMP, Brazil)

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Brunel University London

Combination of CCC capacity &

HPLC resolution power

• Difficulties with HPLC separations at preparative scale

(presence of waxes, emulsification, very low loading).

• Removal of bulk impurities with CCC for further purification

with HPLC.

• Further UPLC-MS analysis and preparative HPLC separation

• Bioassays and Toxicology studies

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Combination of CCC capacity &

HPLC resolution power

• CCC step gradient in normal phase:

1-25min with hexane-methanol-water (5:4:1)

25-60min with hexane-ethyl acetate-methanol-water (1:1:1:1).

• Sample dissolved in methanol (higher loading, 2.5g/1L column)

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Brunel University London

Bio-applications using CCC as extraction

technology

Capture and fractionation of Antibody-based product using Counter Current Extraction and ATPS

with

Will Lewis, Peter Kampalume (GSK)

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Purification of e-mAb using CCC (analogy to capture (bind/elute) chromatography)

Crude material is a part

of the mobile phase

Pure mobile

phase

1) Sample loading

2) Washing the impurities from the column

3) Liquid stationary phase (SP) extrusion

Impurities that partition

into the mobile phase

Impurities that partition

into both phases

Product (e-mAb) in SP

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Brunel University London 16

Selection of ATPS parameters

Partitioning of e-mAb and impurities were tested in a range of

aqueous two-phase systems (ATPS) to identify those which

provided differential partitioning.

Used Protein A to quantify e-mAb partitioning and SEC and

SDS-PAGE to check selectivity.

The ATPS variables were:

A) PEG molecular weight (400, 1000 and 3350Da)

B) PEG and salt concentration (14/14 and 20/20% w/w)

C) Presence of an additional salt (none, 5% NaCl and 5% NaClO4)

D) Salt type (ammonium sulphate, di-potassium phosphate and sodium citrate)

Although pH was not tested as a separate factor, each of the three

salts had different pH (potassium phosphate (pH 9.0-9.5), sodium

citrate (pH 8.6-10.1) and ammonium sulphate (pH 5.5-6).

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Optimisation of the CCE conditions with 14/14/5% w/w/w/ PEG1000/ sodium citrate /NaCl

To maximise the product yield and purity by testing:

• Sample loading (volume and concentration fermentation crude)

• Volume of the mobile phase to wash the impurities from the column

• Mobile phase flow rate & type of mixing

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Protein A analysis

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Purification of e-mAb on Midi

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e-mAb e-mAb

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PLA & PCL nanoparticles manufacture in CCC

Flow rate 0.5 ml/min

Pumping direction – from Head (Centre) to Tail (Periphery)

Sample concentration:10mg/ml PLA in DCM; 5mg/ml PCL-HPG(Na) in Acetone

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Brunel University London

Agarose crude fractionation by

centrifugation - workflow

S: supernatant

P: pellet

8.1_30.1 50xg

S 2000xg

S

P 70xg

S 1800xg

S

P 90xg

S 1500xg

P P P

1500xg S

P 150xg S 250xg

S 350xg S 400xg

S 6000xg

P P

P P

xg : centrifugation g-force 20 min 8 °C

most of small particles < 1µm are removed

centrifugation of crude lot8.1 with stepwise and alternating g-forces

aim: removing big particles by low g-force and small particles by high g-force

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Fractionation by CCC (ABC)

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Particles counted

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Brunel University London

Collaborative research with Biosciences…

Dr Michael Themis

Dr Evgeny Makarov & Dr Terry Roberts

Dr Joanna Bridger (Interdisciplinary award)

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Our research is a team work!

Prof Svetlana Ignatova

Dr Peter Hewitson

Dr Ian Garrard

Dr Jonathan Huddleston

Prof Ian Sutherland

Prof Derek Fisher