Differences between microbial culture and cell culture

Microbial culture vs. cell culture: key differences

When people talk about fermentation in biopharma, they usually mean one of two things: microbial culture or cell culture in bioreactors. Both use the same basic controls (pH, temperature and dissolved oxygen), but they behave very differently in practice. Microbial processes tend to run fast and tolerate aggressive aeration and mixing, while cell culture needs a much gentler hydrodynamic environment and tighter control to keep cells healthy and product quality consistent. Below, we compare microbial vs. cell culture in bioreactors with a biopharmaceutical focus.

Organism types: prokaryotes vs. eukaryotes

Microbial culture typically uses prokaryotes or relatively simple unicellular eukaryotes, mainly bacteria and yeasts. Bacteria (e.g., Escherichia coli, Corynebacterium glutamicum) are prokaryotic cells with no nucleus, usually around 1-5 µm, and they can grow very quickly in relatively simple media. Yeasts are unicellular eukaryotes (e.g., Saccharomyces cerevisiae), but they are still treated as microorganisms in most industrial processes.

By contrast, cell culture involves more complex eukaryotic cells, most commonly animal cells (mammalian lines such as CHO or HEK293) or insect cells (e.g., Sf9), and sometimes plant cells or primary cells. These cells are larger (typically ~10-30 µm) and contain a nucleus and internal organelles. Many cell types are adherent, meaning they require a surface to attach to (often via microcarriers) and do not naturally proliferate freely in suspension without support.

Culture media and nutritional requirements

Microbial culture media are usually less complex and more cost-effective. They typically include a carbon source (glucose, lactose, or other sugars), nitrogen (ammonium salts or nitrates), phosphorus, sulfur, mineral salts, and sometimes yeast extract or peptones to provide trace nutrients. Depending on the process, these media can be defined/minimal (mainly salts plus a carbon source) or complex (including extracts).

In contrast, animal cell culture requires highly nutrient-rich media containing amino acids, vitamins, lipids, peptides, growth factors, and in some cases fetal bovine serum (FBS). These additional components make cell-culture media significantly more expensive than microbial media. Cell-culture media also demand stricter sterilization and handling, and they often rely on the bicarbonate/CO₂ buffering system to keep pH within a narrow operating window.

These tighter nutritional and sterility requirements explain why cell-culture media are more costly and more sensitive. In practical terms, microbes can grow in relatively simple formulations, while eukaryotic cells typically need premium supplements to achieve optimal growth and productivity.

Operating parameters: pH, temperature, oxygen and agitation

Both microbial and cell-based processes are commonly run in stirred-tank bioreactors (STRs), but the operating window is very different:

  • pH: Many bacteria perform best close to neutral pH (roughly 6,0-8.0), while yeasts often tolerate slightly acidic conditions (pH 4.0-6.5). Mammalian cells typically need pH ~7.0-7.4 and within a tight range. In all cases, pH is controlled using probes and automated acid/base addition.
  • Temperature: Most mesophilic bacteria are cultivated around 30-37°C. Yeasts often run at ~28-30°C (some strains can tolerate 37°C). Standard mammalian cell lines are usually operated at 37°C (insect cells around ~27-30°C, plant cells around ~25°C). For mammalian systems, even small temperature shifts can affect cell health and productivity.
  • Oxygen: Aerobic microbial cultures typically require high oxygen transfer rates due to fast metabolism, so processes often use air or oxygen enrichment combined with strong agitation. Some bacteria can grow anaerobically, but many industrial fermentations are aerobic. In cell culture, oxygen is also critical, but it is usually delivered more gently (careful sparging and mixing) to avoid stressing or damaging cells.
  • Agitation: Microbial fermentations often use high-power mixing (e.g., Rushton turbines or other robust impellers) because bacteria and many fungi tolerate shear relatively well. Cell culture generally uses lower-shear agitation (for example marine-style impellers, or low-shear configurations) because eukaryotic cells can be damaged by intense mechanical forces. For adherent cells, microcarriers or other low-shear approaches are used to provide a growth surface while maintaining acceptable mixing.
TECNIC elab advanced laboratory-scale bioreactor with its control unit and culture vessel.

Shear and culture sensitivity

Shear stress is the mechanical force generated by agitation and sparging. Microorganisms (bacteria and yeasts) are generally much more robust: their rigid cell wall and small size allow them to tolerate high agitation and high gas flow rates without a major loss of viability. That is why microbial fermentation often runs at higher RPMs with aggressive aeration when oxygen demand is high.

Eukaryotic cells, especially mammalian cells, are far more shear-sensitive. They lack a rigid cell wall and their structure can be damaged by turbulence. Harsh mixing or vigorous bubbling can disrupt the cell membrane and reduce viability. To reduce this risk, cell culture typically uses low-shear impellers and sparging strategies, and for adherent cultures, microcarriers (small beads) are often used so cells can grow with gentler agitation.

Shear, mixing and oxygen transfer in bioreactor flow patterns

In general terms, axial-flow impellers, such as pitched-blade and hydrofoil designs, achieve more effective bulk mixing than radial impellers. This results in faster homogenisation at the same power input and a reduction of zones with extreme local shear. In contrast, the Rushton turbine generates strong, highly localised turbulence that favours gas dispersion rather than overall circulation. Most experimental and CFD studies agree that axial impellers outperform radial ones in terms of mixing intensity and volume turnover.

With respect to dissolved oxygen, Rushton turbines typically deliver the highest kLa values due to their aggressive bubble breakup. Axial impellers generally reach slightly lower kLa at equivalent power, but they can compensate through improved fluid circulation and more uniform gas distribution. In practice, at similar power inputs, the Rushton turbine often has an advantage in absolute kLa, while hydrofoil impellers achieve effective oxygenation with lower energy consumption by maintaining high recirculation rates throughout the vessel.

Doubling time and culture productivity

A major difference is growth rate. Bacteria can double in minutes (for example, E. coli is often cited at roughly 20-30 minutes under optimal conditions). Yeasts typically double in ~60-90 minutes. Mammalian cells are much slower, often requiring many hours to a day or more (commonly ~18-24 hours or longer) to double. As a result, cell-culture runs are usually much longer than microbial runs.

This has a direct impact on productivity. Microbial fermentations can quickly reach very high cell densities (for example 10⁸-10⁹ cells/mL) in a matter of hours, producing large amounts of biomass or product in a short time. Fed-batch bacterial processes can generate tens of grams per litre of certain proteins or metabolites within a day (depending on the product and process). By contrast, mammalian cell cultures typically reach ~10⁶-10⁷ cells/mL, and recombinant protein titres (such as monoclonal antibodies) are often in the mg/L to g/L range after several days. Cell-based production is slower, but it enables complex proteins (including antibodies and glycosylated products) that bacteria cannot process in the same way.

Scale-up considerations

When moving from lab scale to industrial manufacturing, the main challenges differ depending on the type of culture:

  • Microbial culture: Scale-up commonly reaches very large working volumes (10³-10⁵ L) in stainless steel tanks. High metabolic rates generate significant heat, so efficient cooling systems (jackets and internal coils) are essential. Strong agitation is also needed to maintain oxygen transfer and prevent dead zones. Because bacteria are shear-tolerant, operations can be relatively flexible (batch, fed-batch, continuous), and feeding strategies can be adjusted to optimise productivity.
  • Cell culture: Scale-up is often smaller (typically up to ~10⁴-10⁵ L) and more sensitive. The priority is keeping the vessel homogeneous without harming the cells. This usually means gentler aeration (fine spargers, controlled oxygen addition) and low-shear agitation. Single-use bioreactors (SUBs) are widely used in mammalian processes because they simplify sterility and changeover. For adherent cells, scale-up also introduces extra complexity, often requiring microcarriers or 3D scaffolds to provide enough growth surface.

Overall, microbial processes are typically simpler to scale from a hydrodynamics point of view because the culture is more robust, while cell culture scale-up requires tighter equipment and design choices to protect viability.

Range of all TECNIC bioreactors, to see the full scalability

Monitoring and control strategies

In both cases, critical parameters are monitored and controlled in real time:

  • Sensors and automated control: pH, temperature, dissolved oxygen (pO₂/DO) and agitation are controlled using in-line sensors integrated into the bioreactor. Automation systems adjust acid/base addition, nutrient feeds (via pumps) and aeration according to predefined recipes. In cell culture, additional monitoring is common, such as CO₂ control and biomass/viability indicators (for example, turbidity or capacitance-based measurements).
  • Off-line analytics: Periodic sampling is used to measure viable cell concentration (manual counts, automated counters or flow cytometry), key metabolites (glucose, lactate, ammonia) and product concentration (for example, recombinant protein titre).
  • Advanced PAT tools: Industrial facilities increasingly use optical sensors, dielectric spectroscopy (capacitance) and other in-process analytical technologies (PAT) to estimate biomass and culture state without interrupting the run. These tools help optimise parameters in real time and support consistent product quality.

While the fundamentals of monitoring are similar, eukaryotic cell cultures typically need tighter control. A rapid shift in pH, temperature or oxygen can trigger alarms or compromise a mammalian culture quickly, whereas microbial cultures often tolerate wider fluctuations before performance is seriously affected.

Costs, productivity, and regulatory requirements

From an economic and compliance perspective, microbial and cell culture processes differ in clear ways:

  • Production costs: Microbial processes usually have lower operating costs per litre (cheaper media and faster runs). That said, if the end product is a drug substance, significant resources still go into downstream purification and validation. Cell culture relies on much more expensive media and high-grade sterile infrastructure (filters, controlled environments, cleanrooms), which increases both operating and capital costs.
  • Productivity: Microorganisms can produce large amounts of product quickly, but the molecules are often simpler and typically lack complex post-translational modifications. Cell culture is used to produce more complex proteins (for example, glycosylated human antibodies), although the process is slower. Recent improvements have increased mammalian titres (often reaching several g/L for monoclonal antibodies), but cultures still usually run for multiple days.
  • Regulatory focus: Both approaches must comply with strict GMP requirements, but the risk profile differs. In cell culture, regulators place strong emphasis on viral safety and genetic stability of the production cell line, with step-by-step controls to demonstrate the absence of adventitious agents. In microbial processes, endotoxin control (especially with Gram-negative bacteria) and product purity are major priorities. Ultimately, the final product must meet the relevant regulatory expectations (for example, USP, EMA and FDA requirements).

Overall, microbial cultivation stands out for speed and lower cost, while cell culture is essential for complex biopharmaceuticals that require advanced molecular processing.

Typical applications

  • Microbial culture: Used to manufacture antibiotics (for example, penicillin, streptomycin), amino acids (glutamate, lysine), industrial enzymes (amylases, proteases), biofuels (ethanol) and simpler recombinant proteins. Examples include recombinant human insulin produced in coli, growth hormone expressed in bacteria, recombinant vaccines produced in yeast (such as hepatitis B), and food additives or enzymes produced by fungi and bacteria.
  • Cell culture: Central to the production of therapeutic monoclonal antibodies (oncology and autoimmune indications) and complex glycosylated proteins (for example, erythropoietin and clotting factors). It is also widely used for viral vaccines (virus propagation in animal cells, for example influenza or rabies) and for gene therapy manufacturing (viral vector production). In addition, tissue and cell-based manufacturing continues to grow in importance for regenerative medicine and cell therapies.

Comparative table of key characteristics

CharacteristicMicrobial cultureCell culture (mammalian/insect/plant)
Typical organismBacteria, yeasts (prokaryotes/simple eukaryotes)Animal, plant, or insect cells (complex eukaryotes)
Cell sizeSmall (≈1–5 µm)Larger (≈10–30 µm)
Media typeSimple (salts, sugars, yeast extract)Complex (amino acids, serum or growth factors)
Nutritional requirementsBasic nutrients (C, N, P, S, minerals)Many supplements (hormones, vitamins, lipids)
Operating pH6–8 (bacteria), 4–6 (yeasts)7.0–7.4 (narrow range)
Typical temperature30–37 °C30 °C (insect), 37 °C (mammalian)
Agitation / shearHigh agitation toleratedGentle agitation; shear-sensitive cells
Growth rateVery fast (20–90 min per doubling)Slow (hours/days per doubling)
Typical cell densityVery high (108–109 cells/mL)Lower (106–107 cells/mL)
Product typeEnzymes, metabolites and simpler proteins (insulin, antibiotics)Complex therapeutic proteins (antibodies, clotting factors)
Scale-upEasier to large scale (103–105 L)More limited scale-up (102–104 L, frequent use of SUBs)
Relative costLower (cheaper media, standard consumables)Higher (expensive media, specialised equipment)

Conclusion

In stirred-tank bioreactors (STRs), the difference between microbial and cell culture is not just “which organism you use”, it is how that organism shapes process design and operation. In microbial fermentation, the priority is often delivering enough oxygen and removing heat with high-intensity mixing, because the culture can tolerate it and the kinetics demand it. In cell culture, the focus shifts: you need homogeneous conditions and tight control (pH, DO, CO₂, osmolality) while keeping shear low and minimising bubble-related stress, because viability and, in many cases, product quality are on the line.

If you’re new to bioprocessing, a practical rule of thumb is: microbial equals power and O₂, cell culture equals gentleness and stability. From there, every project should be grounded in data (mixing time, kLa, metabolic profiles and critical quality attributes) and in platform decisions (multi-use vs single-use, feeding strategy, sensors and automation).

In this context, TECNIC offers both stainless-steel bioreactors and single-use bioreactors designed to support every stage of scale-up, from laboratory work through to production. If you want to validate which configuration best fits your process (microbial or cell culture), TECNIC’s team can support you with bioreactor selection, agitation and aeration strategy, and scale-up criteria to keep the process reproducible and transferable across scales.

Microbial vs Cell Culture in Bioreactors FAQ

Frequently asked questions about microbial vs cell culture in bioreactors

1. What is microbial culture in bioprocessing?

Microbial culture is the growth of microorganisms, mainly bacteria or yeasts, under controlled conditions to produce biomass or a target product (for example enzymes, metabolites, or recombinant proteins). In bioreactors, the focus is often on fast growth, strong mixing, oxygen transfer, and heat removal.

2. What is cell culture in biopharma manufacturing?

Cell culture typically refers to growing eukaryotic cells (mammalian, insect, or plant cells) to make complex biological products such as monoclonal antibodies, viral vectors, or glycosylated proteins. In bioreactors, conditions must be stable and gentle to protect viability and product quality.

3. What is the main difference between microbial culture and cell culture in bioreactors?

Microbial culture is usually faster, more tolerant to shear, and often needs high oxygen transfer. Cell culture is slower, more shear-sensitive, and needs tighter control of pH, DO, CO2, osmolality, and sterility. Those differences affect agitation, aeration, and scale-up strategy.

4. Why is oxygen transfer often harder in microbial fermentation?

Many microbial processes have high oxygen demand because cells grow and metabolise quickly. Meeting that demand can require higher power input, stronger agitation, and higher gas flow. In practice, oxygen transfer can become a bottleneck, especially as density increases.

5. Why are mammalian cells more sensitive to shear than bacteria or yeast?

Mammalian cells lack a rigid cell wall, so strong turbulence, bubble bursting, and high local energy dissipation can damage membranes and reduce viability. That is why cell culture bioreactors often use gentler agitation and controlled aeration strategies.

6. Why is cell culture media more expensive than microbial media?

Cell culture media typically includes many defined nutrients and supplements (amino acids, vitamins, lipids, and growth factors). It also requires strict handling and sterile filtration. Microbial media can often be simpler (salts and a carbon source), depending on the organism and process.

7. What pH and temperature ranges are common for microbial culture vs cell culture?

Many bacteria run near neutral pH and around 30 to 37 °C, while yeasts often tolerate slightly acidic pH. Mammalian cell culture typically runs close to physiological pH (around 7.0 to 7.4) and 37 °C, with tighter control because cells are less tolerant to drift.

8. How does scale-up differ for microbial fermentation and cell culture?

Microbial fermentation can scale to very large volumes, but oxygen transfer and heat removal become critical. Cell culture scale-up is often more limited and focuses on maintaining uniform conditions with low shear, stable gas handling, and tight process control, sometimes using single-use bioreactors.

9. What products are typically made with microbial culture vs cell culture?

Microbial culture is commonly used for enzymes, metabolites, and simpler recombinant proteins. Cell culture is used for complex therapeutic proteins (like monoclonal antibodies) and for processes that need eukaryotic machinery, for example viral vaccine production or viral vector manufacturing.

10. What are the most common contamination risks in microbial and cell culture?

Both are vulnerable to contamination, but cell culture is usually less forgiving because growth is slower and conditions are more selective. Typical risks include bacteria, fungi, and mycoplasma in cell culture. Good aseptic technique, validated sterilisation steps, and routine monitoring are essential in both cases.

References
  • A Decade of Microbial Fermentation - BioProcess International. Context on microbial fermentation in bioprocessing and how upstream platforms have evolved.
  • Cell Culture Bioreactor - ScienceDirect Topics. High-level overview of cell culture bioreactors, with concepts relevant to operating constraints vs microbial systems.

This article provides a technical, data-driven overview of microbial culture vs cell culture in stirred-tank bioreactors (STRs). It compares how each system impacts media requirements, growth kinetics, oxygen transfer needs, agitation and shear sensitivity, process monitoring, and scale-up from laboratory to pilot and production. The content is structured to help junior bioprocess professionals understand why the same bioreactor platform is operated very differently depending on whether you are running a microbial fermentation or a cell culture process.

This article has been reviewed and published by TECNIC Bioprocess Solutions, a manufacturer of scalable stirred-tank bioreactors, tangential flow filtration systems, and single-use consumables for bioprocess development, pilot operation, and GMP manufacturing.

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Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Microbial configuration

The microbial configuration of the eLab Advanced is equipped with a Rushton turbine specifically designed for high-oxygen-demand processes such as bacterial and yeast fermentations. The radial-flow impeller generates strong mixing and intense gas dispersion, promoting high oxygen transfer rates and fast homogenization of nutrients, antifoam and pH control agents throughout the vessel. This makes it particularly suitable for robust microbial strains operating at elevated agitation speeds and aeration rates.

Operators can adjust agitation and gas flow to reach the required kLa while maintaining consistent mixing times, even at high cell densities. This configuration is an excellent option for users who need a powerful, reliable platform to develop and optimize microbial processes before transferring them to pilot or production scales.

Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Technical specifications

Materials and finishes

Typical
  • Product-contact parts: AISI 316L (1.4404), typical Ra < 0.4 µm (16 µin)
  • Non-contact parts/skid: AISI 304/304L
  • Seals/elastomers: platinum-cured silicone, EPDM and/or PTFE (material set depends on selection)
  • Elastomers compliance (depending on selected materials): FDA 21 CFR 177.2600 and USP Class VI
  • Surface treatments: degreasing, pickling and passivation (ASTM A380 and ASTM A968)
  • Roughness control on product-contact surfaces

Design conditions

Pressure & temperature

Defined considering non-hazardous process fluids (PED group 2) and jacket steam/superheated water (PED group 5), depending on configuration and project scope.

Reference design envelope
ModeElementWorking pressure (bar[g])Working pressure (psi[g])T max (°C / °F)
ProcessVessel0 / +2.50 / +36.3+90 / 194
ProcessJacket0 / +3.80 / +55.1+90 / 194
SterilisationVessel0 / +2.50 / +36.3+130 / 266
SterilisationJacket0 / +3.80 / +55.1+150 / 302
Jacket working pressure may also be specified as 0 / +4 bar(g) (0 / +58.0 psi[g]) depending on design selection; final values are confirmed per project.

Pressure control and safeguards

Typical
  • Designed to maintain a vessel pressure set-point typically in the range 0 to 2.5 bar(g)
  • Aseptic operation commonly around 0.2 to 0.5 bar(g) to keep the vessel slightly pressurised
  • Overpressure/underpressure safeguards included per configuration and regulations
  • Pressure safety device (e.g., rupture disc and/or safety valve) included according to configuration

Agitation

Reference ranges
Working volumeMU (Cell culture), referenceMB (Microbial), reference
10 L0 to 300 rpm0 to 1000 rpm
20 L0 to 250 rpm0 to 1000 rpm
30 L0 to 200 rpm0 to 1000 rpm
50 L0 to 180 rpm0 to 1000 rpm

Integrated peristaltic pumps (additions)

Typical

The equipment typically includes 4 integrated variable-speed peristaltic pumps for sterile additions (acid/base/antifoam/feeds). Actual flow depends on selected tubing and calibration.

ParameterTypical valueNotes
Quantity4 units (integrated)In control tower; assignment defined by configuration
Speed0-300 rpmVariable control from eSCADA
Minimum flow0-10 mL/minExample with 0.8 mm ID tubing; depends on tubing and calibration
Maximum flowUp to ~366 mL/minExample with 4.8 mm ID tubing; actual flow depends on calibration
Operating modesOFF / AUTO / MANUAL / PROFILEAUTO typically associated to pH/DO/foam loops or recipe
FunctionsPURGE, calibration, totaliser, PWMPWM available for low flow setpoints below minimum operating level

Gas flow control (microbial reference capacity)

Reference

For microbial culture (MB), gas flow controllers (MFC) are typically sized based on VVM targets. Typical reference VVM range: 0.5-1.5 (to be confirmed by process).

Working volume (L)VVM minVVM maxAir (L/min)O2 (10%) (L/min)CO2 (20%) (L/min)N2 (10%) (L/min)
100.51.55-150.5-1.51-30.5-1.5
200.51.510-301-32-61-3
300.51.515-451.5-4.53-91.5-4.5
500.51.525-752.5-7.55-152.5-7.5
O2/CO2/N2 values are shown as reference capacities for typical gas blending strategies (10% O2, 20% CO2, 10% N2). Final gas list and ranges depend on process and configuration.

Instrumentation and sensors

Typical

Instrumentation is configurable. The following list describes typical sensors integrated in standard configurations, plus common optional PAT sensors.

Variable / functionTypical technology / interfaceStatus (STD/OPT)
Temperature (process/jacket)Pt100 class A RTDSTD
Pressure (vessel/lines)Pressure transmitter (4-20 mA / digital)STD
Level (working volume)Adjustable probeSTD
pHDigital pH sensor (ARC or equivalent)STD
DO (pO2)Digital optical DO sensor (ARC or equivalent)STD
FoamConductive/capacitive foam sensorSTD
Weight / mass balanceLoad cell (integrated in skid)STD
pCO2Digital pCO2 sensor (ARC or equivalent)OPT
Biomass (permittivity)In-line or in-vessel sensorOPT
VCD / TCDIn-situ cell density sensorsOPT (MU)
Off-gas (O2/CO2)Gas analyser for OUR/CEROPT
ORP / RedoxDigital ORPOPT
Glucose / LactatePAT sensorOPT

Automation, software and connectivity

Typical

The platform incorporates TECNIC eSCADA (typically eSCADA Advanced for ePILOT) to operate actuators and control loops, execute recipes and manage process data.

Main software functions
  • Main overview screen with process parameters and trends
  • Alarm management (real-time alarms and historical log) with acknowledgement and comment option
  • Manual/automatic modes for actuators and control loops
  • Recipe management with phases and transitions; parameter profiles (multi-step) for pumps and setpoints
  • Data logging with configurable period and export to CSV; PDF report generation
Common control loops
  • Temperature control (jacket heating/cooling)
  • Pressure control (headspace) with associated valve management
  • pH control via acid/base addition pumps and optional CO2 strategy
  • DO control with cascade strategies (agitation, air, O2, N2) depending on package and configuration
  • Foam control (foam sensor and automatic antifoam addition)
Data integrity and 21 CFR Part 11

Support for 21 CFR Part 11 / EU GMP Annex 11 is configuration- and project-dependent and requires customer procedures and validation (CSV).

Utilities

Reference

Utilities depend on final configuration (e.g., AutoSIP vs External SIP) and destination market (EU vs North America). The following values are typical reference points.

UtilityTypical service / configurationPressureFlow / powerNotes
ElectricalEU base: 400 VAC / 50 Hz (3~)N/AAutoSIP: 12 kW; External SIP: 5 kWNA option: 480 VAC / 60 Hz; cabinet/wiring per NEC/NFPA 70; UL/CSA as required
Process gasesAir / O2 / CO2 / N2Up to 2.5 bar(g) (36.3 psi)According to setpointTypical OD10 pneumatic connections; final list depends on package
Instrument airPneumatic valvesUp to 6 bar(g) (87.0 psi)N/ADry/filtered air recommended
Cooling waterJacket cooling water2 bar(g) (29.0 psi)25 L/min (6.6 gpm)6-10 °C (43-50 °F) typical
Cooling waterCondenser cooling water2 bar(g) (29.0 psi)1 L/min (0.26 gpm)6-10 °C (43-50 °F) typical
Steam (External SIP)Industrial steam2-3 bar(g) (29.0-43.5 psi)30 kg/h (66 lb/h)For SIP sequences
Steam (External SIP)Clean steam1.5 bar(g) (21.8 psi)8 kg/h (18 lb/h)Depending on plant strategy

Compliance and deliverables

Typical

Depending on destination and project scope, the regulatory basis may include European Directives (CE) and/or North American codes. The exact list is confirmed per project and stated in the Declaration(s) of Conformity when applicable.

ScopeEU (typical references)North America (typical references)
Pressure equipmentPED 2014/68/EUASME BPVC Section VIII (where applicable)
Hygienic designHygienic design good practicesASME BPE (reference for bioprocessing)
Machine safetyMachinery: 2006/42/EC (until 13/01/2027) / (EU) 2023/1230OSHA expectations; NFPA 79 (industrial machinery) - project dependent
Electrical / EMCLVD 2014/35/EU; EMC 2014/30/EUNEC/NFPA 70; UL/CSA components and marking as required
Materials contactEC 1935/2004 + EC 2023/2006 (GMP for materials) where applicableFDA 21 CFR (e.g., 177.2600 for elastomers) - materials compliance
Software / CSVEU GMP Annex 11 (if applicable)21 CFR Part 11 (if applicable)
Standard documentation package
  • User manual and basic operating instructions
  • P&ID / layout drawings as per project scope
  • Material certificates and finish/treatment certificates (scope dependent)
  • FAT report (if included in contract)
Optional qualification and commissioning services
  • SAT (Site Acceptance Test)
  • IQ / OQ documentation and/or execution (scope agreed with customer)
  • CSV support package for regulated environments (ALCOA+ considerations, backups, time synchronisation, etc.)

Ordering and configuration

Project-based

ePILOT BR is configured per project. To define the right MU/MB package, volumes and options (utilities, sensors, software and compliance), please contact TECNIC with your URS or request the configuration questionnaire.

The information provided above is for general reference only and may be modified, updated or discontinued at any time without prior notice. Values and specifications are indicative and may vary depending on project scope, configuration and applicable requirements. This content does not constitute a binding offer, warranty, or contractual commitment. Any final specifications, deliverables and acceptance criteria will be confirmed in the corresponding quotation, technical documentation and/or contract documents.

Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Technical specifications

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Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Technical specifications

Models and working volumes

Tank

The ePlus Mixer platform combines an ePlus Mixer control tower with Tank frames and eBag 3D consumables. Tank can be supplied in square or cylindrical configurations (depending on project) to match the bag format.

Tank modelNominal volumeMinimum volume to start agitation*
Tank 50 L50 L15 L
Tank 100 L100 L20 L
Tank 200 L200 L30 L
Tank 500 L500 L55 L
*Values based on agitation start interlocks per tank model. Final performance depends on the selected eBag 3D, fluid properties and configuration.

Design conditions and operating limits

Reference

Reference limits are defined for the ePlus Mixer and the Tank. It is recommended to validate the specific limits of the selected eBag 3D and single-use sensors for the customer’s process.

ElementOperating pressureMaximum pressure (safety)Maximum working temperature
ePlus Mixer (control tower)ATM0.5 bar(g)90 °C
TankATM0.5 bar(g)45 °C
Jacket (if applicable)N/A1.5 barDepends on utilities / scope
The 0.5 bar(g) limit is associated with the equipment design, the circuit is protected by a safety valve. Confirm final limits on the equipment nameplate and project specification.

Materials and finishes

Typical
  • Control tower housing and frame: stainless steel 304
  • Product-contact metallic hard parts (if applicable): stainless steel 316 (defined in project manufacturing documentation)
  • Non-product-contact metallic parts: stainless steel 304
  • eBag consumable: single-use polymer (supplier dependent, gamma irradiation / sterilisation per specification)
  • Vent filters: PP (polypropylene), per component list
For GMP projects, the recommended documentation package includes material certificates, surface finish certificates (Ra if applicable) and consumable sterility/irradiation certificates.

Agitation system

Magnetic

Non-invasive magnetic agitation, the impeller is integrated in the eBag 3D Mixer format, avoiding mechanical seals. Agitation speed is controlled from the HMI, with start interlocks linked to the tank model and minimum volume.

Reference speed range
  • Typical agitation range: 120 to 300 rpm (configuration dependent)
  • Magnetic drive motor (reference): Sterimixer SMA 85/140, 50 Hz, 230/400 V, 0.18 kW
  • Gear reduction (reference): 1:5
  • Actuation (reference): linear actuator LEYG25MA, stroke 30–300 mm, speed 18–500 mm/s (for positioning)
Final rpm and mixing performance depend on tank size, bag format and process requirements.

Weighing and volume control

Integrated

Weight and derived volume control are performed using 4 load cells integrated in the tank frame legs and a weight indicator. Tare functions are managed from the HMI to support preparation steps and additions by mass.

ComponentReference modelKey parameters
Load cells (x4)Mettler Toledo SWB505 (stainless steel)550 kg each, output 2 mV/V, IP66
Weight indicatorMettler Toledo IND360 DINAcquisition and HMI display, tare and “clear last tare”
For installation engineering, total floor load should consider product mass + equipment mass + margin (recommended ≥ 20%).

Pumps and fluid handling

Standard

The platform includes integrated pumps for additions and circulation. Final tubing selection and calibration define the usable flow range.

Included pumps (reference)
  • 3 integrated peristaltic pumps for additions (acid/base/media), with speed control from HMI
  • 1 integrated centrifugal pump for circulation / transfer (DN25)
Peristaltic pumps (reference)
ParameterReferenceNotes
Quantity3 unitsIntegrated in the control tower
Pump headHYB101 (Hygiaflex)Example tubing: ID 4.8 mm, wall 1.6 mm
Max speed300 rpmSpeed control reference: 0–5 V
Max flow (example)365.69 mL/minDepends on tubing and calibration
Centrifugal pump (reference)
ParameterReference
ModelEBARA MR S DN25
Power0.75 kW
FlowUp to 42 L/min
PressureUp to 1 bar
For circulation and sensor loops, the eBag 3D format can include dedicated ports (depending on the selected consumable and application).

Thermal management (optional jacket)

Optional

Tank can be supplied with a jacket (single or double jacket options). The thermal circuit includes control elements and a heat exchanger, enabling temperature conditioning depending on utilities and project scope.

  • Jacket maximum pressure (reference): 1.5 bar
  • Thermal circuit safety: pressure regulator and safety valve (reference set-point 0.5 bar(g))
  • Heat exchanger (reference): T5-BFG, 12 plates, alloy 316, 0.5 mm, NBRP
  • Solenoid valves (reference): SMC VXZ262LGK, 1", DC 24 V, 10.5 W
  • Jacket sequences: fill / empty / flush (scope dependent)
The tank maximum temperature may depend on the thermal circuit and consumable limits. Confirm final values with the selected eBag 3D specification.

Instrumentation and sensors

Optional SU

Single-use sensors can be integrated via dedicated modules. The following references describe typical sensors and interfaces listed in the datasheet.

VariableReference modelInterface / protocolSupplyOperating temperatureIP
pHOneFerm Arc pH VP 70 NTC (SU)Arc Module SU pH, Modbus RTU7–30 VDC5–50 °CIP67
ConductivityConducell-P SU (SU)Arc Module Cond-P SU, Modbus RTU7–30 VDC0–60 °CIP64
TemperaturePt100 ø4 × 52 mm, M8 (non-invasive)Analog / acquisition moduleProject dependentProject dependentProject dependent
Measurement ranges and final sensor list depend on the selected single-use components and project scope.

Automation, software and data

Standard + options

The ePlus SUM control tower integrates an industrial PLC and touch HMI. Standard operation supports Manual / Automatic / Profile modes, with optional recipe execution depending on selected software scope.

Software scope (reference)
  • Standard: eBASIC (base HMI functions)
  • Optional: eSCADA Basic or eSCADA Advanced (project dependent)
  • Trends, alarms and profiles, profiles up to 100 steps (depending on scope)
  • Data retention (reference): up to 1 year
Connectivity (reference)
  • Industrial Ethernet and integrated OPC server (included)
  • Remote access option (project dependent)

Utilities and facility interfaces

Typical

Installation requirements depend on jacket and temperature scope and the customer layout. The following values are typical references.

UtilityPressureFlowConnectionsNotes
Electrical supplyN/AReference: 18 A380–400 VAC, 3~ + N, 50 HzConfirm per final configuration and destination market
EthernetN/AN/ARJ45OPC server, LAN integration
Tap water2.5 barN/A1/2" (hose connection)Jacket fill and services, tank volume about 25 L
Cooling water2–4 bar10–20 L/min2 × 3/4" (hose connection)Heat exchanger and jacket cooling
Process air2–4 barN/A1/2" quick couplingUsed for jacket emptying
DrainN/AN/A2 × 3/4" (hose connection)For draining
ExhaustN/AN/AN/AOptional (depending on project)
Stack light (optional)N/AN/AN/A3-colour indication, as per scope
During FAT, verify in the installation checklist that the available utilities match the selected configuration and scope.

Documentation and deliverables

Project-based

Deliverables depend on scope and project requirements. The following items are typical references included in the technical documentation package.

  • Datasheet and user manual (HMI and system operation)
  • Electrical schematics, PLC program and backup package (scope dependent)
  • P&ID, layout and GA drawings (PDF and/or CAD formats, project dependent)
  • Factory Acceptance Test (FAT) protocol and FAT report (as per contract)
  • Installation checklist
  • Material and consumable certificates, as required for regulated projects (scope dependent)
On-site services (SAT, IQ/OQ) and extended compliance packages are optional and defined per project.

Ordering and configuration

Contact

The ePlus Mixer scope is defined per project. To select the right tank size, bag format, sensors and optional jacket and software, please share your URS or request the configuration questionnaire.

The information provided above is for general reference only and may be modified, updated or discontinued at any time without prior notice. Values and specifications are indicative and may vary depending on project scope, configuration and applicable requirements. This content does not constitute a binding offer, warranty, or contractual commitment. Any final specifications, deliverables and acceptance criteria will be confirmed in the corresponding quotation, technical documentation and/or contract documents.

Cellular configuration

The cellular configuration of the eLab Advanced is equipped with a pitched-blade impeller designed to support efficient mixing for cell culture processes in both laboratory development and early scale-up. The blade geometry promotes mainly axial flow, helping to distribute gases, nutrients and pH control agents uniformly throughout the vessel while keeping shear stress at a moderate level. This makes it suitable for mammalian, insect and other shear-sensitive cell lines when operated with appropriate agitation and aeration settings. In combination with the vessel aspect ratio and baffle design, the pitched blade supports stable foaming behavior and reproducible oxygen transfer, which is essential when comparing batches or transferring processes between working volumes.

Operators can fine-tune agitation speed to balance oxygen demand and mixing time without excessively increasing mechanical stress on the culture. 

Scale

Bioreactors engineered for smooth scale-up

From S to XL, with a clear scale path

Move from laboratory to pilot and production with a structured range: eLab (0.5–10 L), ePilot (30–50 L), eProd (100–2000 L). Scale with clearer continuity across platforms, supporting the same key control priorities and configuration paths for a smoother transition between volumes.