The Vertical-Wheel®

A new mixing
geometry for cells.

Stirred-tank impellers were designed for industrial chemistry, not living cells. Rotation of the Vertical-Wheel® impeller within the distinctive U-shaped vessel fully suspends and gently agitates anchorage-dependent human cells that are sensitive to a bioreactor's hydrodynamic conditions — and the process scales linearly from 60 mL to 80 L.

90+
Peer-reviewed publications
60 mL→80 L
Single platform
1
Mixing geometry, all scales
Photographic reference of the PBS Vertical-Wheel® impeller: open structural hoop containing three pitched propeller blades on a horizontal axle.
● Reference geometry · photographic
Open hoop cage · 3 pitched propeller blades · horizontal axle
How it works · interactive

Five beats that explain the Vertical-Wheel®.

A geometrically accurate cross-section of the U-shaped vessel, single-impeller hydrodynamics, energy dissipation field, aggregate morphology, and scale-up. Adapted from PBS Biotech technology references, Dang et al. (2021) and M. Lee (2020).

Vertical-Wheel bioreactor cross-section animationSide-view cross-section of a PBS Vertical-Wheel single-use bioreactor. Shows the U-shaped vessel, an open-hoop impeller containing three pitched propeller blades on a horizontal axle, bottom-sparger bubbles rising and recirculating through the wheel, narrow energy-dissipation field, and uniform spherical cell aggregates.AXLE
VW-01 · cross-section
00s / 25s
Step 1 of 5

1 · U-shaped vessel, horizontal axle

Unlike industrial stirred tanks, the single-use vessel is U-shaped and the impeller axle is horizontal. A single large Vertical-Wheel® occupies most of the cross-section — geometry is the source of the gentle mixing.

Linear scale-up

The same wheel. Just bigger.

18% of PBS-80 footprint
Stage 1 / 5
PBS-Mini 0.1
60 – 100 mL
Agitation
50–110 RPM
Typical use
Discovery & screening

Same impeller geometry. Same EDR profile. Same Kolmogorov eddy length relative to particle size. The process you locked at one scale runs at any other — no re-validation, no re-engineering.

Take a closer look

Every Vertical-Wheel® bioreactor is three coordinated subsystems.

The same three-part architecture — disposable vessel, control system, electro-mechanical drive — appears at every scale, which is why a process locked at PBS-3 transfers identically to PBS-80.

01

Disposable Vessel

Gamma-irradiated single-use vessel — where the cell culture is grown. USP Class VI / ISO 10993 contact materials, axle-free magnetic-drive impeller.

02

Control System

BioLogic™ software stack controlling every aspect of the cell process: PID loops for DO, pH, temperature; recipe automation; 21 CFR Part 11 audit trails.

03

Electro-Mechanical System

Sensors, pumps, mass-flow controllers, and the brushless motor driving the horizontal Vertical-Wheel® axle. Designed for cleanroom uptime.

Anatomy in motion

Every part. Engineered for living cells.

Scroll to disassemble

Exploded view active · 15L
Geometry verified against

Neto P.M., Nogueira D.E.S., Hashimura Y., et al. Characterization of the Aeration and Hydrodynamics in Vertical-Wheel™ Bioreactors. Bioengineering 2022, 9, 386. The open-hoop, horizontal-axis, pitched-blade geometry rendered above is the same geometry characterized in this peer-reviewed CFD and PIV study.

Evidence · Dang et al. (2021)

Narrow EDR distributions, reproduced at every scale.

CFD models indicate that narrow distributions of energy dissipation rates (EDR) can be achieved at various agitation rates and volumes of Vertical-Wheel bioreactors. The reproducibility of homogeneous EDR conditions is essential for optimal and scalable production of therapeutic cells, particularly those grown as aggregates. Panels below show three agitation rates per scale; distributions overlap tightly within each panel and across panels.

PBS-Mini 0.1
60 – 100 mL
EDR (W/kg) →freq.
50 RPM80 RPM110 RPM
PBS-Mini 0.5
300 – 500 mL
EDR (W/kg) →freq.
35 RPM60 RPM85 RPM
PBS-3
1.8 – 3 L
EDR (W/kg) →freq.
20 RPM45 RPM70 RPM
PBS-15
10 – 15 L
EDR (W/kg) →freq.
15 RPM35 RPM55 RPM

Figure adapted from Dang et al. (2021), CFD Characterization of Vertical-Wheel Bioreactors Used for Effective Scale-up of hiPSCs. Not to scale.

Evidence · M. Lee (2020), RegMedNet

Hydrodynamics dictate cell morphology.

Homogeneous EDR conditions promote formation of spherical aggregates with inverse correlation between diameter and agitation rate. Heterogeneous mixing in horizontal-blade impellers results in variable morphologies. For surface-attached cells on microcarriers, Kolmogorov eddy lengths under Vertical-Wheel hydrodynamics remain larger than the microcarrier diameter — eliminating the shear that strips cells from carrier surfaces.

Vertical-Wheel®
Uniform spherical aggregates

Homogeneous EDR yields circular aggregates of similar diameter, with aggregate size inversely correlated to agitation rate.

Horizontal-blade impeller
Heterogeneous morphology

Heterogeneous mixing produces variable, stressed morphologies — a known failure mode for aggregate-grown therapeutic cells.

Figure adapted from M. Lee (2020), Scalable Manufacturing of Allogeneic Cell Therapy Products, RegMedNet.

Vertical-Wheel® vs. Stirred-Tank

Six structural differences that decide whether your therapy survives the bioreactor.

Metric
Vertical-Wheel®
Horizontal-blade stirred-tank
Mixing geometry
Single VW + U-vessel
Multi-blade turbine + flat base
Shear regime
Low, uniform
High at blade tips
EDR distribution
Narrow
Heterogeneous, hot zones
Aggregate morphology
Uniform spheres
Heterogeneous
Microcarrier suitability
Eddies > particle size
Surface shear damage
Scale range (single platform)
60 mL → 80 L
Multiple geometries
Linear scalability

Predicted yield matches actual yield.

Across hundreds of validated transfers, BioPure customers report a scale-up R² of 0.99 between bench and commercial volumes — meaning the process you locked at 3L runs identically at 80L.

Peer-reviewed evidence

Don't take our word for it.
Take theirs.

The Vertical-Wheel® platform is cited in 90+ peer-reviewed publications. Four of the foundational studies are listed below.

Dang, T. et al.
2021

CFD Characterization of Vertical-Wheel Bioreactors Used for Effective Scale-up of hiPSCs

Frontiers in Chemical Engineering

Narrow EDR distributions are reproduced across 0.1, 0.5, 3, and 15 L volumes — the empirical basis for linear scale-up.

Read paper →
Lee, M.
2020

Scalable Manufacturing of Allogeneic Cell Therapy Products

RegMedNet · PBS Biotech

Homogeneous EDR yields uniform spherical aggregates; horizontal-blade impellers produce heterogeneous, stressed morphologies.

Croughan, M.S. et al.
2016

The Future of Industrial Bioprocessing: Batch or Continuous?

Biotechnology & Bioengineering

Defines the Kolmogorov-eddy criterion that explains why Vertical-Wheel hydrodynamics protect surface-attached cells on microcarriers.

Borys, B.S. et al.
2020

Robust bioprocess design for hiPSC expansion using Vertical-Wheel bioreactors

Stem Cell Research & Therapy

Demonstrates >25× expansion of hiPSCs over 6 days with retention of pluripotency markers across scales.

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