MONOCLONAL ANTIBODIES

CaptureSMBยฎ โ€” Continuous Capture Chromatography for mAbs

Twin-column Protein A capture for mAb manufacturing.

 

Load Protein A to its true capacity โ€” and keep it there, cycle after cycle. Validated from lab to GMP production scale by Bristol Myers Squibb at 100ร— scale-up: 2.5ร— Productivity | 92% Resin utilisation (vs. 67% batch) | 50% less buffer | โ‰ฅ94% Yield (equivalent to batch)

 

Source: Angelo et al., BioProcess International 2018; Mรผller-Spรคth et al., Biotechnol. Bioeng. 2019 (Bristol Myers Squibb)

The Protein A Capture Bottleneck

Monoclonal antibodies dominate the biopharmaceutical market โ€” with 100+ approved products, a rapidly growing biosimilar wave, and expanding next-generation formats (bispecifics, ADCs, Fc-fusion proteins). Downstream purification must keep pace.

The Protein A affinity capture step is the cornerstone of mAb downstream processing โ€” but conventional batch chromatography is inherently inefficient. Columns are loaded conservatively to only 50โ€“70% of the resin’s dynamic binding capacity, leaving expensive Protein A resin underutilized. Long sequential cycle times (load โ†’ wash โ†’ elute โ†’ regenerate โ†’ re-equilibrate) create idle column time, limiting throughput and inflating facility footprint.

With cell culture titers now routinely exceeding 5โ€“15 g/L and perfusion bioreactors demanding continuous feed processing, the batch capture step is the rate-limiting bottleneck in modern mAb manufacturing.

The Solution: CaptureSMBยฎ with AutomAbยฎ for mAb Capture

CaptureSMBยฎ is an optimized twin-column periodic countercurrent (PCC) process for continuous Protein A capture of monoclonal antibodies and antibody variants. Two identical columns operate in coordinated interconnected and parallel phases โ€” maximizing resin utilization by safely loading well beyond the breakthrough point, while the second column captures any product that breaks through. The result: 2.5ร— higher productivity (BMS-demonstrated), 92% resin utilization (vs. 67% batch), and 50% buffer savings compared to batch.

AutomAbยฎ dynamic process control uses in-line UV sensors at each column outlet to monitor the breakthrough curve in real-time, automatically adjusting the interconnected loading duration to compensate for feed titer variability, column aging, and batch-to-batch variation โ€” ensuring robust, unattended 24/7 continuous capture.

Same resin. Same buffers. Superior performance. CaptureSMB works with all major Protein A resins โ€” MabSelect SuRe, MabSelect PrismA, Amsphere, and others โ€” and uses your existing wash, elution, regeneration, and CIP buffers unchanged. Your current batch conditions are the starting point; CaptureSMBยฎ is developed from there. Only two columns required โ€” the simplest PCC configuration available.

Learn About CaptureSMBยฎ with AutomAbยฎ
CaptureSMB Continuous chromatography โ€” illustration

Proven Results: CaptureSMBยฎ vs. Batch – Protein A Capture – mAb

01 Productivity Increase

2.5 ร—

Productivity Increase
8.4 โ†’ 26.5 g/L/h

02 Resin

92 %

Resin Utilization
vs. 67% batch

03 Buffer Reduction

50 %

Buffer Reduction
0.73 โ†’ 0.34 L/g

04 Yield

โ‰ฅ94 %

Yield Maintained
Consistent at both scales

05 Operation

24/7

Continuous Operation
Perfusion-ready

06 Scale-Up

100 ร—

Scale-Up Validated
CUBE โ†’ TWIN (BMS)

mAb Purification Comparison Table:

Parameter Batch Protein A Capture CaptureSMBยฎ with AutomAbยฎ
Resin Utilization (DBC) 67% โ€” conservative loading to avoid breakthrough 92% โ€” safe overloading with second column capture
Productivity 8.4 g/L/h โ€” limited by sequential cycle times and idle time 26.5 g/L/h โ€” 2.5ร— higher, continuous loading eliminates idle time
Buffer Consumption 0.73 L/g โ€” large column volumes drive buffer needs 0.34 L/g โ€” 50% reduction from smaller columns
Product Yield โ‰ฅ94% typical โ‰ฅ94% โ€” equivalent to batch
Product Quality (HCP, Agg, DNA) HCP 447 ppm, HMW 3.0% Comparable โ€” HCP 500 ppm, HMW 2.9%
Feed Titer Sensitivity Conservative timing โ€” requires fixed load volumes AutomAbยฎ dynamically adjusts to titer variability
Column Aging Fixed load parameters, performance degrades over lifetime AutomAbยฎ compensates for capacity loss in real-time
Perfusion Compatibility Batch cadence mismatched with continuous feed Ideal โ€” continuous loading matches perfusion output directly
Hardware Complexity Single column, simple Two columns โ€” simplest PCC configuration
Process Control Manual monitoring or timer-based Automated UV-based PAT (AutomAbยฎ)
Stationary Phase / Buffers Standard Protein A Same โ€” no change required

The Contichromยฎ Platform: From mAb Development to Production

All Contichrom systems support twin-column continuous chromatography with the Protein A, CEX, AEX, HIC, and mixed-mode resins used in mAb purification. Methods scale predictably from CUBE โ†’ TWIN LPLC.

mAb & Antibody Variant Applications

Monoclonal Antibodies (IgG1, IgG2, IgG4)

CaptureSMBยฎ delivers 2.5ร— higher Protein A capture productivity for all IgG subtypes while maintaining โ‰ฅ94% yield and comparable product quality (HCP, aggregates, DNA). Validated at 100ร— scale by Bristol Myers Squibb across multiple molecules.


Biosimilar mAbs

Biosimilar manufacturers face intense cost pressure. CaptureSMB’s 2.5ร— higher productivity and 50% buffer savings directly lower Cost of Goods โ€” a critical competitive advantage in the biosimilar market where product differentiation occurs through manufacturing efficiency.


Bispecific Antibodies

Bispecific formats present unique downstream challenges (homodimer removal, charge variants). CaptureSMBยฎ maximizes capture step efficiency, freeing capacity for the more complex polishing steps required. MCSGP continuous polishing on the same Contichrom platform can further resolve closely related bispecific variants.


Antibody Fragments (Fab, F(ab’)โ‚‚, scFv, VHH/Nanobodies)

Antibody fragments can be captured using Protein L, Protein A (for Fc-containing fragments), or custom affinity resins. CaptureSMBยฎ has been demonstrated for F(ab’)โ‚‚ fragment capture using Protein L (KappaSelect) in twin-column countercurrent mode (Ulmer et al. 2015), delivering the same productivity and resin utilization gains as for full-length mAbs.

mAb & Antibody Variant Applications Continued….

Fc-Fusion Proteins

Fc-fusion proteins (e.g., etanercept, abatacept) are captured via Protein A affinity. CaptureSMBยฎ continuous capture applies directly โ€” maximizing resin utilization and throughput for this growing therapeutic class.


Perfusion-Coupled Continuous Manufacturing

CaptureSMB’s continuous loading mode is ideally matched to perfusion bioreactor output. By coupling CaptureSMBยฎ directly to the bioreactor harvest, manufacturers achieve true end-to-end continuous biomanufacturing โ€” reducing facility footprint, eliminating large harvest hold tanks, and shortening manufacturing cadence.


mAb Polishing with MCSGP

For charge variant, aggregate, or fragment separations that require gradient polishing (CEX, HIC), MCSGP continuous polishing on the same Contichrom platform eliminates the purity-yield trade-off โ€” increasing polishing yield while maintaining target CQA specifications (Mรผller-Spรคth et al. 2008, 2010).

Learn About MCSGPยฎ with AutoPeakยฎ
Continuous chromatography - MCSGP โ€” illustration

Getting Started with mAb CaptureSMBยฎ

See the Contichromยฎ platform in action before you commit, assess CaptureSMBยฎ suitability from your existing batch Protein A data โ€” computationally or experimentally โ€” develop your continuous capture process at lab scale on a Contichromยฎ CUBE, then transfer to the TWIN LPLC for GMP production. BMS have validated 100ร— scale-up with 2.5ร— productivity and 50% buffer savings.

See It First โ€” Free Demo or Webinar

Not yet familiar with the Contichromยฎ platform? Start here. YMC ChromaCon offers no-charge demonstrations and introductory webinars tailored to your team.

  • On-site in Zurich (half day, 2โ€“4 hours): see the CUBE in person, run ChromIQยฎ live, discuss your mAb capture process with YMC ChromaCon application scientists
  • Remote webinar (1โ€“3 hours): interactive live session covering CaptureSMBยฎ, MCSGP, N-Richยฎ, ChromIQยฎ software, and the full Contichromยฎ ecosystem
  • Sessions cover CaptureSMBยฎ process design, the AutomAbยฎ control concept, and scale-up to TWIN LPLC manufacturing

โ†’ Request a free demo or introductory webinar

Modeling Assessment for mAbs

Predict CaptureSMBยฎ performance on your Protein A step before running any new experiments. YMC ChromaCon builds a calibrated mechanistic model from your existing batch data.

  • Submit your batch Protein A method (column dimensions, resin, buffers, flow rate) and breakthrough curve data โ€” from any HPLC or FPLC system, no Contichromยฎ required
  • YMC ChromaCon builds the model, simulates CaptureSMBยฎ operating points, and delivers a predicted batch vs. continuous performance comparison: productivity gain, resin utilization, and buffer savings โ€” with scale-up parameters
  • AutomAbยฎ dynamic control impact is included in the simulation
  • Typical timeline: 3โ€“5 weeks from receipt of data; no material shipment required

โ†’ CaptureSMBยฎ Process Modeling Service

Experimental Feasibility Study โ€” Your mAb, Your Resin

Your molecule is run on YMC ChromaCon’s Contichromยฎ platform at our facility in Zurich. We reproduce your batch Protein A method as a benchmark and run โ‰ฅ 3 CaptureSMBยฎ experiments side-by-side.

  • Ship starting material to Zurich โ€” typically โ‰ฅ 20ร— a single preparative batch run, scaled to 1 cm i.D. columns
  • We reproduce your analytical HPLC method, establish the batch benchmark, and run CaptureSMB experiments using your Protein A resin and buffers
  • Deliverable: side-by-side batch vs. CaptureSMBยฎ comparison with real chromatographic data from your molecule, plus purified fractions for your independent verification
  • Typical timeline: 4โ€“6 weeks after receipt of starting material and purchase order

โ†’ YMC ChromaCon Feasibility Studies

Develop at Lab Scale โ€” Rent or Purchase a CUBE

CaptureSMBยฎ method development is performed on the Contichrom CUBE using your existing Protein A resin and buffer system. Available for rental or purchase.

  • ChromIQยฎ CaptureSMBยฎ Wizard converts your breakthrough curve data into an initial CaptureSMBยฎ operating point โ€” the first continuous capture run is typically achievable within a day
  • Your current batch Protein A conditions are the starting point โ€” no new resin or buffer development required
  • AutomAbยฎ dynamic process control is configured to compensate for feed titer variability, column aging, and batch-to-batch variation โ€” enabling robust, unattended 24/7 continuous capture
  • MCSGP polishing for downstream charge variant or size variant separation can also be developed on the same CUBE

โ†’ Contichromยฎ CUBE Rental Program

โ†’ Purchase a Contichromยฎ CUBE

Scale to GMP Production โ€” Contichromยฎ TWIN LPLC

The CaptureSMBยฎ process transfers directly from the CUBE to the TWIN LPLC for pilot and manufacturing-scale production. YMC ChromaCon provides scale-up consulting and GMP documentation support.

  • TWIN LPLC Capture for continuous Protein A capture with AutomAbยฎ at pilot and production scale
  • TWIN LPLC Polishing (optional) adds downstream MCSGP for charge variant or size variant purification on the same platform family
  • Four TWIN LPLC system sizes (300โ€“2000) cover 0.03โ€“3.33 L/min up to 0.5โ€“36 L/min โ€” pilot through full GMP production
  • BMS validated 100ร— scale-up from CUBE to TWIN: 2.5ร— productivity, 92% resin utilization, 50% buffer savings, yield maintained โ‰ฅ 94%
  • GMP documentation support (IQ/OQ/PQ) and scale-up consulting available

โ†’ Scale-Up Consulting and Training

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Frequently Asked Questions