next generation zirconia-based antibody purification media · used protein a and protein g antibody...

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Next Generation Zirconia-Based Antibody Purification Media Dr. Clayton McNeff , Dwight Stoll, Danielle Hawker (ZirChrom), Dr. Andy Clausen (Merck) Dr. Peter W. Carr and Dr. Anuradha Subramanian (U of MN) 2003 ZirChrom Separations, Inc. ® 1-866-STABLE-1 www.zirchrom.com

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Page 1: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Next Generation Zirconia-Based Antibody Purification Media

Dr. Clayton McNeff, Dwight Stoll, Danielle Hawker (ZirChrom), Dr. Andy Clausen (Merck)Dr. Peter W. Carr and Dr. Anuradha Subramanian (U of MN)

2003 ZirChrom Separations, Inc.

®

1-866-STABLE-1www.zirchrom.com

Page 2: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Outline

Supports for Bio-ChromatographyModification of zirconia for bio-chromatographySmall scale Mab purification Fast Mab purifcationComparison to Protein GBinding Capacity StudiesConclusions

Page 3: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Current Supports forBio-Chromatography

Soft-Gels: Hard-Gels:1. Cellulose 7. Silica2. Agarose 8. Hydroxy-apatite3. Sepharose 9. Zirconia4. Polyacrylamide5. Polyamide6. Polystyrene

Page 4: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Particle Sizes Available Data for Rhinophase®-AB

Both nonporous and porous analytical (3, 5 micron) and preparative (10, 25 micron) particles are available.

25 micron3 micron1.7 micron NPZ

Page 5: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Modification: Chelating Ligand

Reflux particles in EDTPA solutionForms multiple bondsBlocks Lewis acid/base interactions

NCH2CH2

N

CH2

CH2

CH2

CH2

H2O3P

H2O3P

PO3H2

PO3H2

Ethylenediamine-N,N’-tetra(methylenephosphonic) acid = “EDTPA”

Page 6: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Nitrogen Porosimetry of P-EDTA Modified ZrO2

No pore blockageNo loss of surface area

10 100 1000

0.0

0.2

0.4

0.6

0.8

1.0

1.2Bare Unmodified ZrO2

Reflux 4 hrs in P-EDTA

Reflux 8 hrs in P-EDTA

Reflux 16 hrs in P-EDTA

dV/dlogD

(cm3/g)

Pore Diameter (A)

Page 7: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Gradient Chromatography on Rhinophase®-AB

0 5 10 15 20Time (min)

1

2

3

4

5

6

7

Protein mixture. Mobile phase: 4 mM P-EDTA, 20 mM MES, pH 5.5; linear gradient from 0 to 1 M Na2SO4 in 30 min. Flow Rate 1 mL/min. UV detection at 280 nm.

1 BSA2 Myoglobin3 Ribonuclease B4 Ribonuclease A5 Chymotrypsin6 Lysozyme7 Cytochrome c

Page 8: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Small-Scale Purification of Mab IgG2a Contaminated with BSA

min0 5 10 15 20 25 30 35

mAU

-20

0

20

40

60

80

100

120

140

VWD1 A, Wavelength=280 nm (NIH22399\IGGBSA01.D)

Area: 5329.822.

682

Area: 2602.62

12.6

78

0.5 M NaCl0.05 M NaCl 1.0 M NaCl

BSA

MAB

LC Conditions: 100 ul injection of BSA (6.0 mg/ml) contaminated MAB (1.0 mg/ml) eluted by salt step gradient. Mobile phase: 20 mM MES, 4 mM EDTPA, 0.05 M-to-1.0 M NaCl pH=5.5. Flow rate: 2.0 ml/min. Temperature: 30oC. Detection: 280 nm.

Note: BSA is not retained undersample loading conditions.

Page 9: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

A New Ultrafast Preparative Purification Method Using Rhinophase®-AB

Due to zirconia’s very high mechanical strength,Mab purifications can beperformed at high mobile phase linear velocities. A simple vacuum filtration apparatus can be use to achieve very high flow rates through a packed bed (90 mL/min). This approach is not possible using soft affinity gels such as Protein A and Protein G media.

Page 10: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Ultrafast Preparative Purification of IgG1Using Rhinophase®-AB

Fraction Number

Total Analysis Time= 15 minutes

This is 100 times faster than a

Protein G purification of the

same scale!

Step A = 20 mM MES buffer, 4 mM EDTPA, 50 mM NaCl @ pH 4.0, Step B = 20 mM MES buffer, 4 mM EDTPA, 50 mM NaCl @ pH 4.0, Step C = 20 mM MES buffer, 4 mM EDTPA, 2.0 M NaCl @ pH 4.0.Flow Rate = 60 mL/min, Injection size = 31.6 mL serum-free cell culture supernatant diluted 4-times withloading buffer, (3.98 mg of Mab), Amount of Rhinophase®-AB in tube = 10 grams.

0

0.5

1

1.5

2

2.5

1 2 3 4 5 6 7 8 9 10 11

UV

Abs

orba

nce

at 2

80nm Step A

(Load)Step B(Wash)

Step C(Elution)

Fraction 5

Page 11: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

ELISA Plate Comparison of Protein G and the Ultrafast Purification on

Rhinophase®-AB

Protein Protein G Rhinophase®-ABOffered Purified IgG Fraction 5 Fraction 5

15.6 0.0531 0.0502 94.5%31.3 0.0946 0.0992 104.9%62.5 0.1676 0.1892 112.9%125 0.3176 0.3632 114.4%250 0.5596 0.6362 113.7%500 1.0166 1.1507 113.2%

1000 1.8151 1.8632 102.6%Average % 108.0%

OD 280 nm

An ELISA plate analysis using the same amount of Mab from Protein Gand Rhinophase®-AB purifications showed an increased signal for the Rhinophase®-AB purified Mab.

Page 12: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Mab Purity Comparison from Semi-Preparative Run

Silver-stained, SDS-PAGE gel Comparing IgG1 purified by Protein G (row 1 from right) and Rhinophase®-AB (row 3 from right). Electrophoresis was run under reducing conditions. Sample loading at 1 ug per lane. All other lanes are standards.

Rhinophase®-ABPurified

Protein G Purified

Purified Mabwas equally pure

using Protein G and Rhinophase®-AB.

Page 13: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

0

2

4

6

8

10

12

0.0 5.0 10.0 15.0

C, mg/ml

Qa,

mg/

ml b

eads

Linear Velocity: 12 cm/min

Effect of Mab (hIgG) Concentration on DynamicBead Capacity (Qa) of ZirChrom Mab Media

Conditions: Pure hIgG in Loading Buffer (20mM MES, 4mM EDTPA, 50mM NaCl, pH5.5) was loaded on a 5x4.6mm i.d. ZirChrom Mab Media column at a linear velocity of 12.0cm/min and detected at280nm. The injection was continued until the absorbance of the effluent reached 80% of the inletconcentration. The column was then washed with Loading Buffer until it had reached baseline. The Adsorbed hIgG was then eluted with Elution Buffer (20mM MES, 4mM EDTPA, 1.0M NaCl, pH5.5).

The DynamicCapacity of

ZirChrom Mab Media was Determined as the Amount

of hIgG captured per

mL of Media.

Isotherm shapeIndicates

Langmuir-typeAdsorption

Page 14: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

Effect of Linear Velocity on the Dynamic Qmax of ZirChrom Mab Media

Qmax = 20.0mg/cc

13.9mg/cc11.5 mg/cc

0

5

10

15

20

25

0 5 10 15Linear Velocity, cm/min

Qm

ax, m

gH

IgG

/ ml

med

ia

Conditions: Pure hIgG in Loading Buffer (20mM MES, 4mM EDTPA, 50mM NaCl, pH5.5) was loaded on a 5x4.6mm i.d. ZirChrom Mab Media column at a linear velocities of 3.0, 6.0, and 12.0 cc/min and detected at 280nm. The injection was continued until the absorbance of the effluent reached 80% ofthe inlet concentration. The column was then washed with Loading Buffer until it had reached baseline.

The adsorbed hIgG was then eluted with Elution Buffer (20mM MES, 4mM EDTPA, 1.0M NaCl, pH5.5).

Typical value onProtein A = 2-4 mg/mL

Page 15: Next Generation Zirconia-Based Antibody Purification Media · used Protein A and Protein G antibody purification media. ¾ Typical yields of Mab purifications greater than 95%, with

ConclusionsRhinophase®-AB provides a widely applicable alternative to currently used Protein A and Protein G antibody purification media.Typical yields of Mab purifications greater than 95%, with purity levels equal to or greater than affinity gel-type media.Due to Rhinophase®-AB’s excellent mechanical stability, purifications can be performed 100-fold faster with equivalent results.Rhinophase®-AB is chemically durable over the entire pH range, which allows for cleaning and depyrogenation.Rhinophase®-AB has affinity for a wide range of immunoprotein classes and subclasses including monoclonal and polyclonal IgG, IgA, and IgM.Rhinophase®-AB can be packed into large preparative scale columns and operated at high mobile phase linear velocities for fast large scale purifications of immunoproteins.Acknowledgement: National Institutes of Health