PendoTECH Single-Use Pressure Sensor: Performance Review from Four Peer-Reviewed Studies
Across four peer-reviewed deployments in tangential flow filtration and alternating tangential flow perfusion, the PendoTECH single-use pressure sensor family is a credible primary pressure element for single-use bioprocessing under 25 psi. The MEMS-based chip resolves TMP-drop of ~1.2 psi per centimetre along a UF cassette [1] and tracks fouling-driven TMP escalation to 0.9–0.95 bar in ATF perfusion [3]. Its main limitations are the 75 psi ceiling (which excludes high-pressure chromatography), the looser accuracy in the vacuum regime, and the operational overhead of tracking single-use consumables.
PendoTECH single-use pressure sensor at a glance
The PendoTECH single-use pressure sensor is an in-line, disposable pressure element designed for flexible-tubing single-use bioprocess assemblies. A MEMS-based piezoresistive chip (the vendor's proprietary MEMS-HAP high-accuracy pressure chip) is bonded into a moulded polycarbonate or polysulfone housing that connects directly to the fluid path via hose-barb, luer, or sanitary fitting, so there is no separate diaphragm or fill fluid. PendoTECH was acquired by Mettler-Toledo in 2020 and the sensors are now sold under the Mettler-Toledo Pendotech brand. Product details below are sourced from the vendor specification sheet and the accuracy and implementation technical note; field performance data comes from independent studies cited throughout this review.
| Specification | Value |
|---|---|
| Measurement principle | MEMS-based piezoresistive pressure chip (MEMS-HAP), in-line contact with fluid |
| Operating pressure range | −7 to 75 psi (~−0.5 to 5.2 bar) |
| Accuracy (vendor-claimed) | ±2% of reading (0 to 6 psi), ±3% of reading (−7 to 0 and 6 to 30 psi), ±5% of reading (30 to 75 psi) |
| Response time | Effectively instantaneous at typical bioprocess flow rates (millisecond-scale MEMS response) |
| Operating temperature | Rated for typical bioprocess ambient use; not autoclavable |
| Sterilisation | Gamma and x-ray irradiation compatible up to 50 kGy; supplied non-sterile or pre-sterilised in single-use assemblies |
| Process connection | Hose barb 1/8" to 1.5" ID, luer, sanitary flange, molded connector; integral 12" cable |
| Fluid-contact materials | Polycarbonate or caustic-resistant polysulfone; USP Class VI compliant, EMEA 410 Rev 2 compliant |
| Continuous use life | Validated for up to 90 days of continuous fluid contact (93-day 10 psi durability study) |
| Typical use envelope | Tangential flow filtration TMP monitoring, ATF perfusion cell retention, single-use bioreactor headspace pressure, chromatography column inlet/outlet |
What the peer-reviewed literature says
Four peer-reviewed studies published between 2023 and 2025 deployed the PendoTECH single-use pressure sensor as the primary pressure element in bioprocess research. All four papers use two or more sensors flanking a filter to derive transmembrane pressure directly from measured upstream and downstream values, which is the canonical control-loop configuration the vendor documents. None of the papers reports a sensor-hardware failure over the observation windows tested; the reported failures are process failures (membrane fouling, protein deposition, extractable-vesicle accumulation) that the pressure sensor faithfully detected.
Cunha et al. 2023 in Biotechnology Progress [1] is the sharpest test of the sensor's pressure-resolution because the study measures the axial pressure gradient along a modified flat-sheet 30 kDa regenerated cellulose UF cassette during bovine IgG concentration to more than 200 mg/mL. The authors used PendoTECH pressure transmitters (PMAT4A monitor family) to record local pressure at multiple axial positions and derived that the transmembrane pressure drop remained approximately constant at 1.2 psi per centimetre along the membrane while axial pressure fell by roughly 58 psi across the cassette. Resolving a 1.2 psi/cm gradient over the full 75 psi operating envelope is the practical benchmark: the sensor cleared it with the resolution needed for confocal correlation of protein-deposition thickness to local TMP.
Veje et al. 2024 in the Journal of Membrane Science [3] uses PREPS-N-038 sensors on the permeate side and PREPS-N-5-5 sensors on the feed side of two polysulfone hollow-fibre modules attached to a CHO recombinant-protein perfusion bioreactor. Short flux-step experiments identified critical flux up to 69 LMH without exceeding the critical fouling boundary. Prolonged operation at 8.3 LMH produced TMP escalation from baseline to 0.9–0.95 bar (~13 psi) accompanied by measurable membrane pore-size change; protein transmission through the fibre stayed above 88% throughout. The pressure sensors resolved TMP with enough fidelity to draw the flux-vs-fouling operating curve that separates safe-perfusion flux from the fouling regime.
Madabhushi et al. 2025 in Biotechnology and Bioengineering [2] used PendoTECH pressure sensors at the inlet and outlet ports of small-scale offline hollow-fibre model filters to isolate the contribution of individual perfusion-culture components to fouling. Working with recombinant GS-knockout CHO K1 cells expressing a monoclonal antibody at target 85–100 million cells/mL in 3 L glass and 50 L Xcellerex XDR single-use bioreactors, the study established that simethicone-based antifoam accumulates over a 28-day perfusion campaign and, at 500 ppm, is by itself sufficient to cause complete filter blockage. The pressure sensors were the primary readout for both the offline model and the perfusion bioreactor cell-retention loop. Vu et al. 2024 in Biotechnology Progress [4] extends the same approach to a stacked-filter geometry, using PendoTECH transmitters in the retentate loop and near the inlet and outlet of 20 cm hollow-fibre segments to quantify hydraulic-resistance reduction and confirm Starling-flow suppression at 3 L and 50 L perfusion scales.
Performance data from cited studies
| Study | Conditions | Pressure metric | Reported value / drift | Conclusion |
|---|---|---|---|---|
| [1] Cunha 2023 | Flat-sheet 30 kDa RC UF cassette, 150 kDa bovine IgG concentration to >200 mg/mL, PMAT4A monitors | Axial P and derived TMP-drop along cassette | Axial P fell ~58 psi across module; TMP drop constant at ~1.2 psi/cm along membrane length | Sensor resolved a per-cm pressure gradient over the full 75 psi envelope with confocal-correlatable fidelity |
| [2] Madabhushi 2025 | Perfusion CHO K1 mAb, 3 L glass and 50 L Xcellerex XDR SUB, 85–100 M cells/mL, 28-day runs | Filter inlet/outlet P, TMP profile | Complete filter blockage at 500 ppm simethicone antifoam; significant fouling 75–250 ppm | Sensor pair reliably detected antifoam-driven TMP escalation and complete blockage endpoints |
| [3] Veje 2024 | ATF perfusion, polysulfone hollow-fibre, CHO recombinant protein, PREPS-N-038 (permeate) + PREPS-N-5-5 (feed) | Critical flux, TMP escalation at fixed flux | Critical flux up to 69 LMH; TMP rose to 0.9–0.95 bar at 8.3 LMH prolonged operation | Resolved the flux-vs-fouling operating boundary directly from measured TMP |
| [4] Vu 2024 | Stacked 20 cm TFF filters, 3 L and 50 L perfusion, retentate-loop and inlet/outlet P | Hydraulic resistance, retentate-loop P profile | Lower hydraulic resistance confirmed for segmented permeate; improved sieving at both scales | Pressure sensors verified the Starling-flow suppression hypothesis quantitatively at scale |
Every row is a separate peer-reviewed publication; see References section for full citations. Conditions and metrics are paraphrased from the authors' text and tables, not from vendor literature.
Limitations and failure modes reported
Across the reviewed studies and the vendor validation record, the following limitations recur. Each bullet is tagged with the specific citation or vendor document that describes it.
- Rated to 75 psi maximum — the sensor is unsuitable for high-pressure chromatography, high-pressure homogenisation, or any application where transient overpressure can exceed the ceiling; a hardline overpressure trip in the control system is still required (vendor specification sheet).
- Accuracy in the −7 to 0 psi vacuum regime is looser (±3% of reading) than in the 0 to 6 psi positive regime (±2%) — a real limitation for permeate-side monitoring where TMP can transiently go negative [3].
- The sensor is a dedicated single-use consumable with a validated 90-day continuous-use envelope — longer campaigns require scheduled sensor replacement at a manifold change; extending beyond 90 days is outside the vendor validation record (vendor validation guide).
- Extreme in-process fouling — for example antifoam accumulation exceeding roughly 250 ppm simethicone in intensified perfusion — produces a runaway TMP spike the sensor faithfully detects but cannot prevent, so a pressure-triggered process-abort strategy is required in the control layer [2].
When the literature recommends PendoTECH single-use pressure sensors
Recommended for
- Ultrafiltration TMP monitoring under 25 psi, where per-cm axial gradients need to be resolved [1]
- ATF and TFF perfusion cell-retention loops with hollow-fibre modules, feed and permeate side [3]
- 28-day-plus intensified perfusion campaigns where antifoam-driven fouling must be detected early [2]
- Multi-scale (3 L to 50 L) perfusion process development where sensor cross-manifold consistency matters [4]
Caveats / not recommended for
- Pressure above 75 psi — excludes high-pressure chromatography and high-pressure homogenisation (vendor specification sheet)
- Fine vacuum monitoring — looser accuracy in the −7 to 0 psi range constrains permeate-side low-TMP resolution [3]
- Continuous campaigns beyond 90 days without scheduled sensor replacement — outside the vendor validation envelope (vendor validation guide)
- As the only line of defence — a pressure-triggered abort strategy is still required because the sensor detects but cannot prevent runaway fouling [2]
Use cases documented in the literature
Specific deployments reported in the cited studies. Each card corresponds to a real published bioprocess use case.
150 kDa bovine IgG to >200 mg/mL retentate
Modified flat-sheet 30 kDa RC UF cassette with PendoTECH PMAT4A monitors resolving axial pressure profile and TMP drop of ~1.2 psi/cm along the membrane, later correlated to confocal-imaged protein deposition.
[1]28-day intensified perfusion, 3 L glass + 50 L XDR
PendoTECH pressure sensors at the inlet/outlet of small-scale offline hollow-fibre models and the perfusion bioreactor cell-retention loop identified simethicone-antifoam accumulation as the dominant fouling driver.
[2]Polysulfone hollow-fibre CHO recombinant protein
PREPS-N-038 (permeate) and PREPS-N-5-5 (feed) sensors quantified critical flux up to 69 LMH and TMP escalation to 0.9–0.95 bar at prolonged 8.3 LMH operation with >88% protein transmission.
[3]3 L and 50 L stacked hollow-fibre segments
Retentate-loop and inlet/outlet PendoTECH transmitters confirmed lower hydraulic resistance in segmented-permeate stacked TFF, quantifying the Starling-flow suppression that drove the improved sieving coefficient.
[4]Sizing the TFF or ATF membrane behind the pressure sensors?
The TFF membrane sizing and diafiltration calculator returns membrane area, diavolume schedule, and TMP-flux envelope from your feed volume, target concentration, and flux target — a natural downstream companion to reading TMP off a PendoTECH pair.
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Frequently asked questions
What does the PendoTECH single-use pressure sensor actually measure?
How accurate is the PendoTECH single-use pressure sensor in real bioprocess use?
Can PendoTECH single-use pressure sensors be gamma-sterilised?
What is the operating pressure range and where does it saturate?
How does PendoTECH compare to a reusable stainless-steel pressure transducer?
Which PendoTECH model should I use for what tubing size?
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What are the reported limitations of PendoTECH single-use pressure sensors?
References
- Cunha, F., Zuponcic, J., Rossi, F., Springer, G., Ximenes, E., Bruns, N., Moomaw, J.F., Bowes, B.D., Qian, K.K., Yu, Z., Yang, D., Corvari, V.J., Ardekani, A., Reklaitis, G., Ladisch, M. (2023). Intramodule pressure profiles and protein accumulation during tangential flow filtration. Biotechnology Progress. DOI: 10.1002/btpr.3389.
- Madabhushi, S.R., Zuo, Q., Zhou, C., Phuangthong, C., Ruppert, N., Tang, T., Pelaez, F. (2025). Systematic Investigation of Impact of Antifoam and Extracellular Vesicles on Fouling of Hollow Fiber Filters in Intensified Perfusion Processes Highlights the Key Impact of Antifoam. Biotechnology and Bioengineering. DOI: 10.1002/bit.28987.
- Veje, M.H., Quirós, M., Kristensen, P., Jørgensen, M.K. (2024). Investigation of fouling in perfusion cell culture processes using alternating tangential flow filtration. Journal of Membrane Science, 701, 122764. DOI: 10.1016/j.memsci.2024.122764.
- Vu, J., Gadberry, J.A., Coffman, J., Lee, K. (2024). Improved sieving coefficient in perfusion cell culture with reduced effective filtration length of hollow fibers. Biotechnology Progress. DOI: 10.1002/btpr.3472.