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United Kingdom
Viral vectors, Genomics

Cell culture media mixing in a benchtop LevMixer™ single-use mixer

Oct 15, 2025

Mustapha Hohoud, Senior Engineer, Bioprocess

Stijn De Backer, Downstream Field Application Specialist


Powder-liquid mixing is a common mixing-technology requirement in the biopharmaceutical industry for media and buffer processing. Single-use mixing technology is typically used in-house to dissolve and mix media or buffers from powdered components and is typically followed by a filtration step to ensure a sterile and ready-to use-solution.

We demonstrate the use of the benchtop LevMixer™ 10 L single-use mixing system for efficient powder-liquid mixing of cell-culture media

  • LevMixer™ 10 L single-use mixer provided highly effective mixing of HyClone™ peak expression medium and HyClone™ Dulbecco’s modified Eagle medium with high glucose, allowing mixing with a strong and solid vortex.
  • Post-filtration of the Supor™ Prime filter showed a comparable performance to the reference filter tested, indicating it is a reliable choice for sterile filtration as being an essential factor in maintaining media purity and quality.
  • Consistent pH and conductivity measurements before and after filtration confirmed that both the LevMixer™ mixer and the Supor™ Prime filter preserved the integrity of the media, which is critical for reproducibility in experimental and industrial settings.

Introduction

In this application note, we describe the preparation of two ready-to-use powder mixture media—the animal-derived component-free (ADCF) HyClone™ peak expression medium and HyClone™ Dulbecco's modified Eagle medium (DMEM) with high glucose—using the benchtop LevMixer™ 10 L single-use mixing system.

We performed sterile filtration of the media using a single-use Supor™ Prime filter comparing chemically defined media against classical media. Chemically defined media with premixed powder components and conditioning offer significant advantages in research and biopharmaceutical production by ensuring consistency and reproducibility, minimizing contaminants, and simplifying downstream processing due to the absence of undefined components such as serum.

Fig 1. In this study, we demonstrate the effective mixing of HyClone™ peak expression medium and HyClone™ DMEM high-glucose powder medium using the benchtop LevMixer™ 10 L single-use mixing system.

Materials and methods

For each experiment, we installed and set up the LevMixer™ 10 L single-use mixing system according to the instructions for use.

We then placed the single-use biocontainer bag in the mixer and deployed to obtain a final 3D and cubical shape after which we calibrated the single-use pH sensor with the precalibrated label.

The single-use biocontainer bag was filled with 9 kg of demineralized water (considering a density of 1000 kg/m³) to reach a volume of 90%. Then, mixing was started at the max speed of 2900 rpm, at room temperature (20°C ± 2°C) and without control. After 1 min of stable mixing, we added the media through the powder port located on top of the mixing system.

Individual procedures provided with the media were then followed. The recommended dissolution time for the HyClone™ peak expression medium was of 20 min and 10 min for the HyClone™ DMEM high-glucose concentrations. Once the powder was dissolved, we supplemented media with the right amount of sodium bicarbonate to achieve a certain concentration and pH (Table 1).

As a next step, around 10 min after, the speed was reduced to 2000 rpm and sodium hydroxide (for the HyClone™ peak expression medium) or hydrochloric acid (for HyClone™ DMEM high-glucose medium) were added to adjust the pH to the targeted range of 7.0 to 7.40.

After a stabilization time of around 10 min, the remaining volume of water was added to obtain the final solution of 10 L at the right concentration.

We filtered the resulting solution over a sterilizing grade Supor™ Prime filter using a peristaltic pump. Pressure was monitored to evaluate the possible fouling of the membrane.

We used the Supor™ EX ECV sterilizing grade filter in Mini Kleenpak™ capsule as a reference filter. This is a typical polyethersulfone (PES) media filter.

The filter capacity was determined by Pmax analysis, see below.

We tested filter integrity post-filtration using a bubble-point (BP) test, see below.

Table 1. HyClone™ media components and concentrations

 Media  Quantity of media (g) in 10 L  Concentration g/L  NaHCO3 added (g) in 10 L  NaHCO3 added (g/L)
 HyClone™ peak expression medium  251.7  2.52  25.0  2.5
 HyClone™ DMEM high glucose  134.0  13.4  37.0  3.7

Mixing times

We evaluated mixing times from the time when the powder mix was added until it was visually dissolved (visual mixing time) and with the time taken to achieve 95% mixing (T95) when the pH values have stabilized within the range of ± 5% of the end value (95%; 105%).

Fig 2. Example of a chart showing a pH shift with the T95 and stable reading in the range of ± 5%.

Sterile filtration Pmax

Our filterability test was performed at a constant flow rate using a peristaltic pump in the test setup shown in Figure 3.

Fig 3. The Pmax test setup.

The results obtained were extrapolated using direct linear scale-up calculations based on the ratio of filter area between the test system and the process-scale filter. This is applicable when the provided process fluid sample volume allows for a filtration volume through the test filter system directly equivalent to the process-scale volume. An extrapolation method, Pmax, may be applied to trials where equivalent sample volume is not filtered, either due to sample volume or time constraints.

Pmax calculations cannot be applied when no increase occurred and/or the course of pressure increase cannot be fitted to the underlaying model (resistance model).

Method procedure constant flow

We installed a 3 cm² Supor™ Prime sterilizing grade filter (DC3) or a 2.8 cm² Supor™ EX ECV sterilizing grade filter (KS2) in a filter capsule and connected them to a product reservoir containing the fluid sample. We filled the reservoir with the sample, and set the peristaltic pump to deliver flow rates of 7 and 14 mL/min. Once the system was ready, the pump was activated and the manual valve opened to initiate the flow. A beaker was placed on a tared balance to collect the filtrate. The flow rate was then adjusted to a scaled-down value based on customer requirements and equipment limitations. The pump was started again, and the timer initiated simultaneously.

Throughout the filtration process, key parameters such as upstream pressure, filtrate volume, filtration time, conductivity, and turbidity were monitored and recorded at fixed intervals determined by the product's filterability. The test concluded when one of the predefined stop criteria was met.

Sterile filtration integrity test: Bubble point (BP)

We assessed the integrity of the test filters with the BP nondestructive integrity test method and the filters wetted with water. The reference value for the BP was 4.1 bar (60.2 psi, 0.4 MPa). This value corresponds to the lowest BP value of a test filter that fully retained Brevidimonas Diminuta (B. Diminuta) during bacteria retention testing.

The BP test is designed to detect the largest pores of a membrane filter. It is based on measuring the gas flow across a completely wetted membrane at increasing gas test pressure, until the point at which the wetting fluid is expelled from the pores, and bulk flow is measured.

Results

In Figures 4 and 5, you can see the evolution of the pH reading per step in the mixing process for each medium.

Fig 4. Chart of the pH reading recorded for the HyClone™ peak expression medium preparation in the LevMixer™ 10 L single-use mixing system.

Fig 5. Chart of the pH reading recorded for the HyClone™ DMEM high glucose preparation (4500 mg/L) in the LevMixer™ 10 L single-use mixing system.

Table 2. Process information and mixing times

 Media  pH adjustment  pH before adjustment  pH after adjustment  Powder addition time (min)  Visual mixing time (with powder addition[min])  pH-based mixing time (with powder addition [s]), T95  pH-based mixing time (with powder addition [min, s]), T99
 HyClone™ peak expression medium (ADCF)  35 mL of 1 M NaOH  6.93  7.06  2  < 10 min  52 s  1 min 51 s
 HyClone™ DMEM high glucose  5 mL of 5 M HCl  7.77  7.29  < 1  ~ 2 min  53 s  1 min 32 s

 

Table 3 and Table 4 show the throughput at a constant flow rate of 7 and 14 mL/min for both the Supor™ Prime filter and a benchmark Supor™ EX EKV polyether sulfone (PES) filter.

The pressure increase noted between the different flow rates was only due to the increase in flow rate and not a higher fouling occurring as the pressures stayed stable throughout the filtration.

Table 3. Throughput, sterile filtration of HyClone™ expression medium

 Filter  Bench-scale filter EFA tested (m2)  Filtered amount (g)  Filtration time (min)  Test average flux (LMH)  Test throughput (L/m2)  Test final pressure (bar)
 Supor™ EX ECV*  0.00028  226.6  31  1566.4  809.3  0.1
 Supor™ Prime*  0.00030  221.8  31  1533.2  792.1  0.1
 Supor™ EX ECV  0.00028  437.7  31  3025.6  1563.2  0.3
 Supor™ Prime  0.00030  431.6  31  2983.4  1541.4  0.2

 

* Filtered at a constant flow rate of 7 mL/min

Filtered at a constant flow rate of 14 mL/min

1 bar = 14.5 psi = 1 MPa

Table 4. Throughput, sterile filtration of HyClone™ DMEM high-glucose medium

 Test identification, HyClone™ DMEM high glucose  Filter  Bench-scale filter, EFA tested (m2)  Filtered amount (g)  Filtration time (min)  Test average flux (LMH)  Test throughput (L/m2)  Test final pressure (bar)
 Supor™ EX ECV (benchmark filter)*  Supor™ EX ECV*  0.00028  210.0  30  1500.0  750.0  0.2
 Supor™ Prime*  Supor™ Prime*  0.0003  208.0  30  1485.7  742.9  0.1
 Supor™ EX ECV  Supor™ EX ECV  0.00028  422.6  30  3018.6  1509.3  0.3
 Supor™ Prime  Supor™ Prime*  0.0003  424.4  30  3031.4  1515.7  0.3

 

* Filtered at a constant flow rate of 7 mL/min

Filtered at a constant flow rate of 14 mL/min

1 bar = 14.5 psi = 1 MPa

Table 5 shows the integrity test results. We assessed the integrity of the test filters with the BP nondestructive integrity test method and the filters wetted with water. All filters used in this study passed the integrity test.

Table 5. Integrity test results

 Media and filters  Filter  BP (bar)*  Result
 

 HyClone™ peak expression powder medium

     
   Supor™ EX ECV (benchmark filter)  4.20  Pass
   Supor™ Prime  4.65  Pass
   Supor™ EX ECV  4.75  Pass
   Supor™ Prime  4.65  Pass
 
 HyClone™ DMEM high-glucose powder medium   
   Supor™ EX ECV  4.85  Pass
   Supor™ Prime  4.70  Pass
    Supor™ EX ECV  4.70  Pass
   Supor™ Prime  4.70  Pass
 
 Supor™ EX ECV  BP min  3.58  
 Supor™ Prime  BP min  4.15  

* 1 bar = 14.5 psi = 1 MPa

Filtered at a constant flow rate of 7 mL/min

Filtered at a constant flow rate of 14 mL/min

We measured conductivity of the media to verify if the filtrations influenced the initial properties of the media (Table 6).

Table 6. Conductivity, pH, and temperature of the media tested at different flow rates on benchmark filter and post Supor™ Prime sterilizing-grade filters used at different flow rates

Flow rates
 7 mL/min  14 mL/min

HyClone™ peak expression medium

 Prefiltration Conductivity (mS/cm)
Temperature (°C)
pH
10.46
20.00
7.30
10.46
20.00
7.30 
 

 Post-benchmark filter filter

Conductivity (mS/cm)
Temperature (°C)
pH
10.53
20.00
7.30
10.46
20.00
7.30  
   Post Supor™ Prime filter  Conductivity (mS/cm)
Temperature (°C)
pH
10.48
20.00
7.30
10.48
20.00
7.30 
 
 HyClone™ DMEM high-glucose medium    Prefiltration  Conductivity (mS/cm)
Temperature (°C)
pH
14.70
19.10
7.50
14.94
19.10
7.50 
   Post-benchmark filter filter  Conductivity (mS/cm)
Temperature (°C)
pH
14.97
19.30
7.50
14.92
19.30
7.50  

Post Supor™ Prime filter  Conductivity (mS/cm)
Temperature (°C)
pH
14.85
19.30
7.50 
1481
193
7.50  

Conclusion

The LevMixer™ 10 L single-use mixing system demonstrated strong efficiency in preparing both the and the HyClone™ peak expression powder medium and the HyClone™ DMEM high-glucose powder medium.

We demonstrated the mixer’s ability to dissolve and mix those powdered media with a solid and strong vortex.

The Supor™ Prime filter showed a comparable performance to the Supor™ EX ECV sterilizing grade reference filter tested, indicating it is a reliable choice for sterile filtration as being an essential factor in maintaining media purity and quality.

Consistent pH and conductivity measurements before and after filtration confirmed that both the LevMixer™ 10 L single-use mixing system and the Supor™ Prime filter preserved the integrity of the media, which is critical for reproducibility in experimental and industrial settings.

The successful results achieved at bench scale further suggest promising scalability for larger-volume applications, making the LevMixer™ 10 L single-use mixing system and the Supor™ Prime well-suited solutions for biopharmaceutical manufacturing.

Acknowledgments

The contributions made to this application note were made by Mustapha Hohoud, Senior Engineer Bioprocess, and Stijn De Backer, Downstream Field Application Specialist.

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