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Science with Passion

Application No.: VBS0064 
Version 1  06/2017

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Comparison of IgG purification with two different protein A media

Michaela Schulze, Kate Monks; applications@knauer.net

KNAUER Wissenschaftliche Geräte GmbH, Hegauer Weg 38, 14163 Berlin

Comparison of IgG purification with two different protein A media

Summary

The purification of antibodies is generally performed with protein A column materials. Two prepacked protein A columns from two different suppliers were compared in their ability to purify immunoglobulin antibodies (IgG) from human plasma. Capacity and yield were compared and revealed no significant differences in the performances of the two investigated columns.

Introduction

Today, the most widely used affinity chromatography purification procedure in industry is the capture of antibodies using protein A ligand. Affinity chromatography is used to isolate and enrich proteins or nucleic acids from complicated mixtures like human plasma. The principle is based on biospecific interactions between two reaction partners. The column matrix contains a covalently bound ligand to which the substance of interest specifically binds. A certain buffer is needed to elute the antibodies bound to the matrix. This type of chromatography is very efficient and delivers a highly clean protein. An AZURA® Bio purification system was used for comparison of two affinity materials. Here, an automated method to purify IgG from human plasma was used. Two protein A media were compared. The capacity of the columns to bind IgG was determined for both materials.

Results

The IgG were purified from 500 µL human plasma by affinity chromatography using protein A columns. The eluted antibodies were then automatically collected with a fraction collector. The chromatogram of the whole purification process is divided in three steps (Fig 1 A&B). During the first step, the protein A column was equilibrated with buffer A followed by feed injection. The proteins that did not bind to the protein A columns went to waste and were visible as large flow through peak in step one. Thereafter, the column was washed with buffer A until no further peaks were detected. During step two, the antibodies were eluted from the column with buffer B and collected in 1 mL fractions. In the last step, the protein A columns were equilibrated with the buffer A in preparation for the next sample injection. Three runs were performed for each column material. The amount of purified protein was with 6 mg IgG originating from 500 µL human plasma are similar (Tab 1). Moreover, a SDS PAGE analysis was performed with the IgG samples to check the purity of the individual fractions. The protein bands of IgG heavy chains (HC) and IgG light chains (LC) are visible at 48 kDa and 25 kDa in the SDS-PAGE (Fig A1, suppl. material).

(A)

Fig. 1 Chromatogram of antibody purification with Protein A HP column from vendor x (A) and Sepapure Protein A FF (B) columns; Step 1: injection peak of human plasma and column washing; Step 2: elution peak of IgG from protein A column with buffer B; Step 3: column equilibration with buffer A

(B)

Fig. 1 Chromatogram of antibody purification with Protein A HP column from vendor x (A) and Sepapure Protein A FF (B) columns; Step 1: injection peak of human plasma and column washing; Step 2: elution peak of IgG from protein A column with buffer B; Step 3: column equilibration with buffer A

Fig. 1 Chromatogram of antibody purification with Protein A HP column from vendor x (A) and Sepapure Protein A FF (B) columns; Step 1: injection peak of human plasma and column washing; Step 2: elution peak of IgG from protein A column with buffer B; Step 3: column equilibration with buffer A

Tab. 1 Total and fraction concentrations of IgG purified with Sepapure Protein A FF or Protein A HP column from vendor x for three runs

Run

Column

IgG concentration in fraction (mg/mL)

Fraction size (mL)

Total IgG amount in fractions (mg)

1

Sepapure Protein A FF

0.82

7

5.74

2

Sepapure Protein A FF

0.83

7

5.81

3

Sepapure Protein A FF

0.87

7

6.09

4

Protein A HP vendor x

0.95

6

5.70

5

Protein A HP vendor x

1.00

6

6.00

6

Protein A HP vendor x

1.04

6

6.24

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Materials and Methods

In this application an AZURA Bio purification system was used. It consisted of an AZURA P 6.1L LPG metal-free pump, AZURA ASM 2.1L assistant module with feed pump and two 6 port/3 channel injection valves, an AZURA DAD 2.1L diode array detector with 10 mm, 10 µL flow cell cartridge; AZURA CM 2.1 conductivity monitor and a fraction collector.

The two 5 mL protein A columns were equilibrated with 20 mL buffer A (20 mM phosphate Buffer pH 7.0) at 2 mL/min. Then 500 µL human plasma were injected and the column washed with 20 mL buffer A at 2 mL/min.

The antibodies were then eluted with 20 mL elution buffer B (0.1 M Glycin-HCL, pH 2.7) and collected with the fraction collector. The concentrations of the IgG fractions from each individual run were determined with a NANODROP 2000 Tab 1). The UV signal was measured at 280 nm and conductivity signal was recorded.

Conclusion

Human immunoglobulin antibodies (IgG) were successfully purified with both protein A materials via affinity chromatography with the AZURA Bio purification system. An average of 6 mg IgG was purified from 500  µL of human plasma with both columns. When compared via SDS PAGE, in both cases eluted proteins are identical in purity. All in all, it can be concluded that the purification is quantitatively and qualitatively identical for both tested column materials.

References

[1] Janeway CA Jr, Travers P, Walport M, et al.; Immunology: The Immune System in Health and Disease. 5th Edition, New York; Garland Science, 2001

Additional Materials and Methods

Fig. A1 SDS Page of the eluted IgG from human plasma; Lanes 1 – 3 IgG (4 µg) purified from three runs with the Sepapure Protein A FF column; Marker (10 µL) in kDa; Lanes 4-6 IgG (4 µg) puri-fied from three runs with the vendor x column

Fig. A1 SDS Page of the eluted IgG from human plasma; Lanes 1 – 3 IgG (4 µg) purified from three runs with the Sepapure Protein A FF column; Marker (10 µL) in kDa; Lanes 4-6 IgG (4 µg) puri-fied from three runs with the vendor x column

Tab. A1 Method parameters

Buffer A

20 mM phosphate buffer pH 7.0

Buffer B

100 mM Glycin – HCl pH 2.7

Gradient

Time [min]

% A

% B

0-10

100

0

10-20

0

100

20-30

100

0

Flow rate

2 mL/min

System pressure

0 bar

Column temperature

25°C

Run time

30 min

Injection volume

0.5 mL

Injection mode

Full loop

Detection wavelength

280 nm

Data rate

10 Hz

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Tab. A2 System configuration

Instrument

Description

Article No.

Pump

AZURA P 6.1L LPG, metal-free

APH64EB

Detector

AZURA DAD 2.1L

ADC01

Flow cell

10mm, 10µL, Ti, 300bar

AMC38

Assistant

AZURA ASM 2.1L

Left: Pump with pressure sensor, 50 mL pump head, SSt

Middle: 6 port 2 position injection valve, 1/16" connectors

Right: 6 port 2 position injection valve, 1/16" connectors

AYBHECEC

Fraction collector

Foxy R1

A59100

Conductivity monitor

CM 2.1S

ADG30

Column 1

Protein A HP 5 mL from vendor x

-

Column 2

Sepapure Protein A FF, 5 mL Column

020X39FSPZ

Software

PurityChrom 3D Option

A2654

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KNAUER System Configuration

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Application details

Method

FPLC

Mode

Affinity

Substances

IgG in human plasma

CAS number

n/a

Version

Application No.: VBS0064 | Version 06/2017 | ©KNAUER Wissenschaftliche Geräte GmbH

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