Shop in your local currency and language

Choose another country or region to see specific content for your location and shop online.

United Kingdom
Downstream bioprocessing, Process development, Affinity chromatography

Evaluating antibody fragment purification using MabSelect™ VH3 resin

Mar 2, 2026

Conventional protein A resins primarily target the fragment crystallizable (Fc) region of antibodies, limiting their effectiveness in capturing antibody fragments. We developed our MabSelect™ VH3 protein A resin to uniquely bind to the variable heavy (VH) domain of VH3 class antibodies, to selectively capture antibody fragments and bispecific antibodies (bsAbs). In this study, we’ll show you purification results of the single variable domain of heavy chain antibodies from both camelid (VHH) and human fragmented antibody (Fab), demonstrating high binding capacities and yields for these targets. Additionally, we will investigate the impact on HCP clearance using different buffers in the intermediate wash for Fab purification.

Introduction

Our MabSelect™ VH3 affinity protein A resin uniquely binds the VH domain of VH3 class antibodies, thereby selectively targeting the antibody fragments and bispecific antibodies (bsAbs). The protein A-derived affinity ligand has a strengthened VH3 interaction and knocked-out Fc interaction, enabling stable and high-capacity binding of antibody fragments belonging to the VH3 sequence family of both human antibodies and camelid heavy-chain antibodies.

Due to the electrostatic character of the interaction between protein A and VH3 domain, the binding has different tolerance to pH and ionic strength compared to the Fc interaction (1). Additionally, the binding affinity can vary with minor amino acid (aa) sequence variations of the target VH region, and the purification protocol may need adjustments to optimize purity and yield.

In a conventional protein A protocol, an intermediate wash step at high-salt concentration is recommended to help improve purity, for example by removing host cell proteins (HCPs). In this article, we demonstrate good recoveries for fragment targets, even with high-conductivity wash buffers using the MabSelect™ VH3 resin. We also discuss how using alternative wash buffers to NaCl can affect purity.

Purification of single variable domain of heavy chain antibodies from camelid (VHH)

Experimental methods

We packed MabSelect™ VH3 resin in a Tricorn™ 5/50 column and tested the dynamic binding capacity (DBC) at a 6 min residence time with purified VHH in triplicate runs. We used clarified Pichia pastoris supernatant with VHH at 4.9 g/L titer for purification runs on MabSelect™ VH3 resin in Tricorn™ 5/50 columns, according to the method in Table 1. We also performed purification runs using 0.5 M NaCl and 1 M NaCl in 20 mM phosphate pH 7.0 as wash buffer, with each run conducted in triplicate using a sample load of 21.6 mg (CV = 0.96 mL), which corresponded to 70% of QB10%, We used the ANOVA test to statistically analyze results, for DBC and purification, considering yield and purity.

Table 1. Method for purification of VHH

Phase Buffer Volume (CV) Residence time (min)
Equilibration PBS* 5 4
Load 0.2 µm filtered Pichia pastoris VHH cell culture supernatant 4.4 mL (70% of QB10%) 6
PBS wash PBS 2 6
Intermediate wash 0.5 M NaCl or 1.0 M NaCl in 20 mM phosphate, pH 7.0 5 6
Low-salt wash 25 mM phosphate, pH 6.5 1 6
Elution 50 mM acetate, pH 3.5 5 6
Strip 100 mM acetic acid 2 6
Cleaning in place (CIP) 0.5 M NaOH 3 5 (up-flow)
Reequilibration PBS 5 5 (up-flow)

*20 mM sodium phosphate,150 mM NaCl, pH 7.4

Results

The QB10% (DBC at 10% breakthrough) for VHH on MabSelect™ VH3 resin was determined by frontal analyses to be 32.1 mg/mL resin (Table 2).

Table 2. QB10% results from DBC runs with VHH

Number of repeats (n) Mean QB10% SD* QB10%
MabSelect™ VH3 QB10% 3 32.1 0.4

*SD = Standard deviation


We carried out purification runs at load corresponding to 70% of QB10%, with intermediate wash buffer containing either 0.5 M NaCl or 1.0 M NaCl. Overlay chromatograms are shown in Figure 1. We observed no product loss during washing─even using 1.0 M NaCl in the wash buffer.

Table 3 presents our yield, HCP, and aggregate (analyzed using size exclusion chromatography, SEC) results for elution samples. We found that a higher salt concentration of 1 M NaCl in the wash buffer gave better purity in terms of HCP clearance, when compared to 0.5 M NaCl (p = 0.015, at 95% CI by statistical analysis using t-test). The aggregate level is 2.0 ± 0.1% with 0.5 M NaCl wash, and 1.8% with 1.0 M NaCl wash. We obtained a higher yield using 1.0 M NaCl in the wash buffer than 0.5 M NaCl; however, this deviation is likely coincidental, and the yields are most likely the same.

Table 3. Summary of results from purification runs with VHH

NaCl concentration (M) n Mean yield (%) SD* yield (%) Mean aggregate (%) SD* aggregate (%) p-value at 95% CI Mean HCP (ppm) SD* HCP (ppm) p-value at 95% CI
0.5 3 93 3.6 2.0 0.1 < 0.01 100 13.4 0.015
1.0 3 104 0.6 1.8 0 47 3.2

*SD = Standard deviation
CI = confidence interval


Fig 1. Chromatogram overlay from purification runs with VHH using wash buffer containing 0.5 M NaCl (blue) and 1.0 M NaCl (orange), respectively. UV280 (solid lines) and conductivity (dotted lines) traces are shown.


Purification of Fab fragment

Experimental materials and methods

We packed MabSelect™ VH3 resin in Tricorn™ 5/50 and Tricorn™ 10/100 columns and tested the DBC at a 6 min residence time with purified Fab. We used clarified CHO supernatant with Fab at a titer of 1.24 g/L for purification runs, according to the method in Table 4. Additionally, we performed a wash-buffer screening study on the Tricorn™ 5/50 column. We used a load amount of 33.1 mg/mL, which corresponded to 70% of QB10%. See Table 5 for a list of the wash buffers we used. Based on the outcome of the wash buffer screening, we carried out verification runs on the Tricorn™ 10/100 column with a subset of wash buffers. Following this, we analyzed the elution samples for yield, HCP, aggregate content, and ligand leakage.

Table 4. Method for purification runs with Fab

Phase Buffer Volume (CV) Residence time (min)
Equilibration PBS* 5 4
Load 0.2 µm filtered CHO Fab cell culture supernatant 33.1 mg/mL resin (70% of QB10%) 6
PBS wash PBS 2 6
Intermediate wash See Table 5 5 6
Low-salt wash 25 mM phosphate, pH 6.5 1 6
Elution 50 mM acetate, pH 3.5 3 (buffer screening)
5 (verification runs)
6
Strip 100 mM acetic acid 2 6
CIP 0.5 M NaOH 3 5 (up-flow)
Reequilibration PBS 5 5 (up-flow)

*20 mM sodium phosphate,150 mM NaCl, pH 7.4


Table 5. Intermediate wash buffers tested in buffer screening study with Fab

Intermediate wash buffers*
PBS
0.5 M NaCl in 20 mM phosphate, pH 7.0
10% glycerol in 25 mM sodium phosphate, pH 7.0
0.5% Triton CG-110 in 25 mM sodium phosphate, pH 7.0
0.2 M L-Arg in 25 mM sodium phosphate, pH set to 7.0 with HCl
1% Polysorbate 20 in 25 mM sodium phosphate, pH 7.0
0.5 M urea in 25 mM sodium phosphate, pH 7.0
0.5 M Tris, pH 7.5
0.1 M Tris, pH 7.5
0.5 M Tris, pH 8.5
0.25 M Tris, pH 8.5
20 mM citrate, pH 4.6 in 2 M ammonium sulfate
5% 1,2-propanediol in 25 mM sodium phosphate, pH 7.0
25 mM phosphate, 50 mM caprylic acid, pH 7.25
1% polyethylene glycol (PEG) 200 in 25 mM sodium phosphate, pH 7.0

*End users must always ensure freedom to operate for the specific processes used for purifying their specific molecules

Results

The QB10% for Fab on MabSelect™ VH3 resin was determined to be 47.3 mg/mL resin. To test impact on purity and yield, we carried out purification runs at loads corresponding to 70% of QB10%, screening different intermediate wash buffers (see Table 5).

Using standard high-salt intermediate wash buffer (0.5 M NaCl in 20 mM phosphate, pH 7.0), we observed some minor product loss in the wash step. High-conductivity Tris buffer and L-Arg containing buffer caused significant product loss (Fig 2). Other tested wash buffers did not cause product loss (Fig 3).

We determined the purity in terms of HCP reduction using different wash buffers, and plotted relative to HCP reduction using PBS as wash buffer (Fig 4). We found that

  • Wash buffers with 0.5% Triton CG-110 or 1% Polysorbate-20 most effectively reduce HCP.
  • Wash buffers using 50 mM caprylic acid give a similar level of HCP reduction to the 0.5 M NaCl wash buffer.

Fig 2. Overlay chromatogram from wash buffer screening study of buffers causing target loss. Least target loss is from standard wash buffer with 0.5 M NaCl.

Fig 3. Overlay chromatogram from wash buffer screening study of buffers not causing target loss.

Fig 4. HCP in Fab eluates from experiments screening different wash buffers relative to HCP amount obtained using PBS as wash buffer. Optimal reduction in HCP was obtained with 0.5% Triton CG-110 or 1% Polysorbate in the wash buffer.


We performed verification runs with Fab using five different wash buffers on Tricorn™ 10/100 columns:

  • Three concentrations of NaCl: 150 (PBS), 250 and 500 mM in phosphate pH 7.0
  • Two detergent additives: 0.5% Triton CG-110 or 1% Polysorbate 20 in phosphate pH 7.0

We analyzed these elution samples for yield, purity, and ligand leakage. Results from verification runs are presented in Table 6 and overlay chromatograms in Figure 5. We observed a minor UV peak early in the wash phase in the run using a 0.5 M NaCl wash buffer. SEC fraction analysis shows this peak mostly includes aggregated species, and it does not decrease the monomer yield compared to PBS (Table 6).

Using a 0.25 M NaCl wash buffer achieves comparable HCP clearance to 0.5 M NaCl, with no product loss during wash. The wash buffers containing detergent additives, as opposed to NaCl, give superior HCP clearance.

Table 6. Fab verification runs on Tricorn™ 10/100 result summary

Wash buffer additive Monomer yield (%) HCP (ppm) Aggregate (%) Ligand leakage (ppm)
PBS (150 mM NaCl in 20 mM phosphate, pH 7.4) 95 405 4.8 3
0.5 M NaCl* 95 292 4.8 19
0.25 M NaCl* 102 302 4.7 7
0.5% Triton CG-110* 93 234 4.6 12
1% Polysorbate 20* 95 206 4.7 16

*In phosphate buffer, pH 7.0.


Fig 5. Chromatograms from purification runs with Fab using wash buffer containing 0.15 M NaCl (blue), 0.25 M NaCl (orange), 0.5 M NaCl (red), 0.5% Triton CG-110 (green), and 1% Polysorbate 20 (purple). UV280 (solid lines) and conductivity (dotted lines) traces are shown. A different column with lower CV was used for the run with 0.5 M NaCl wash buffer, hence the lower load volume.


Conclusions

Our MabSelect™ VH3 resin emerges as a powerful and reliable solution for capturing antibody fragments of the VH3 sequence family. Although initially developed for binding the human VH region, it performs equally well in purification of single variable domain of heavy chain antibodies from camelids.

Our study demonstrates its ability to effectively purify antibody fragments from the VH3 sequence family in both species, delivering a strong binding capacity, excellent purity, and yield—even when high-conductivity wash buffers are used.

Furthermore, incorporating low concentration of Polysorbate-20 or Triton CG-110 in wash buffers can enhance purity when target binding is salt-sensitive, offering a versatile approach to balance efficiency and product quality.

Note: End users must always ensure freedom to operate for the specific processes used for purifying their specific molecules.

References

  • Graille et al, PNAS (2000), vol. 97, no. 10, pp 5399-5404
Capture of asymmetric bispecific antibody purification
In this video, we show a systematic approach that can be used to achieve high purity of the correctly paired antibody already in the capture step.

Did you find what you were looking for?