1. Problem Description and Scope
This manual provides a structured approach for the diagnosis and correction of measurement errors in industrial flow meters. Inaccurate flow measurements can lead to significant operational inefficiencies, loss of product quality, increased energy costs and in critical cases even safety risks. These errors often manifest themselves as deviating process values, absent signals, sporadic or fluctuating measurements, and persistent measurement drift. Diagnosis focuses on a wide range of common flow meter technologies, including electromagnetic, Coriolis, vortex, differential pressure (such as orifice plates and Venturi tubes), and ultrasonic flow meters.
The severity of a measurement error is classified as follows:
- Critical: Direct impact on safety, environmental compliance, or primary product quality. Requires immediate action.
- Major: Leads to significant loss of efficiency, increased energy consumption, or batch consistency deviations. Requires rapid planning and implementation of corrective actions.
- Minor: Slight deviations that primarily affect process optimization without direct critical consequences. Requires planning for routine maintenance.
The diagnosis in this guide includes effects related to installation, changes in process conditions, calibration drift, and the formation of scale or contamination.
2. Safety measures
CAUTION REQUIRED! Prior to any diagnostic or maintenance work on flow meters or related piping, it is essential to strictly follow all applicable safety procedures.
- Lockout/Tagout (LOTO): Ensure that all energy sources (electrical, pneumatic, hydraulic, mechanical) are isolated and locked according to NEN-EN-ISO 14118 and company standards. Check for absence of voltage with a suitable multimeter (e.g. Fluke 1587 FC) before working with electrical components.
- Personal Protective Equipment (PPE): Always wear the required PPE for the specific process intervention. This includes at least safety glasses (EN 166), chemical-resistant gloves (EN 374), safety shoes (EN ISO 20345) and, if necessary, hearing protection (EN 352) and respiratory protection (EN 140/143).
- Stored Energy and Hazardous Materials: Use extreme caution with pressurized pipes, hot fluids, corrosive chemicals, or cryogenic media. Completely depressurize and bleed piping systems before loosening flanges or fittings. Follow the procedures for the safe handling of hazardous substances in accordance with the safety data sheets (SDS).
- ATEX directive: Work in potentially explosive areas only with intrinsically safe equipment (in accordance with ATEX directive 2014/34/EU) and follow the specific work permit procedures for 'hot work' or 'cold work'.
- Access and Fall Hazard: Ensure safe access to the flow meter. Use approved ladders or scaffolding and take measures against the risk of falls.
3. Required Diagnostic Tools
The effective diagnosis of flowmeter errors requires specific instrumentation. The table below describes the essential tools:
| Tool | Specification / Model | Measuring range / Accuracy | Goal |
|---|---|---|---|
| Digital Multimeter | True RMS, CE, CAT III/IV, e.g. Fluke 179 | Voltage: 0-1000 V AC/DC (±0.5%); Current: 0-10 A AC/DC (±0.7%); Resistance: 0-50 MΩ (±0.9%) | Checking supply voltage, signal currents (4-20 mA), resistance of sensors and cabling, grounding. |
| Process Calibrator (HART/Fieldbus) | CE, intrinsically safe (if ATEX), e.g. Fluke 754 | Source/Measure 4-20 mA (±0.01%); Voltage 0-30 V; Resistance; Frequency; HART communications | Simulating and measuring 4-20 mA signals, checking flow transmitters, HART communication for diagnosis and configuration. |
| Pressure measuring equipment (Digital Manometer) | Calibrated, accuracy ±0.05% of full scale, e.g. Fluke 718 | Depending on process pressure: e.g. 0-10 bar; 0-100 bar | Checking system pressure, pressure difference across differential pressure gauges (DP gauges), detection of cavitation. |
| Temperature meter (PT100 with Datalogger) | Accuracy ±0.1 °C, range -50 to 250 °C, e.g. Testo 925 | Depending on process: -200 to 800 °C | Measuring process temperature for density and viscosity compensation, detection of overheating or undercooling. |
| Infrared (IR) Thermometer / Thermal Camera | IR thermometer: ±1.5 °C, range -30 to 900 °C; Thermal camera: resolution 320x240, thermal sensitivity <0.05 °C, e.g. Flir T series | Varies by model | Contactless temperature measurement, detection of unwanted temperature gradients, checking heat exchange in the pipe. |
| Vibration analyzer | FFT analysis, 10 Hz - 20 kHz, e.g. SKF Microlog Analyzer | Measuring range acceleration, speed (mm/s RMS) and displacement | Identify mechanical vibrations that can affect vortex or ultrasonic meters. Limit value e.g. ISO 10816: < 4.5 mm/s RMS (good condition). |
| Portable Ultrasonic Flowmeter (Clamp-on) | Accuracy ±1-2% of measured value, CE, e.g. Katronic KATflow 200 | Varies by pipe diameter and fluid | Non-invasive verification of the existing flow meter, checking for unexpected flow patterns or abnormalities. |
| Endoscope / Videoscope | Flexible, diameter > 5 mm, length > 1 m, IP67, e.g. Olympus IPLEX G Lite | Not applicable | Visual inspection of the inside of the pipe and the sensor (electrodes, vortex shedder, orifice plate) for contamination, wear or damage. |
| Ultrasonic Thickness Gauge | Accuracy ±0.01 mm, range 0.63 - 500 mm, e.g. Cygnus 4+ | Not applicable | Measuring pipe wall thickness to detect erosion or internal deposits that affect the flow profile. |
4. Initial Assessment Checklist
Before beginning detailed diagnostics, a thorough initial assessment is essential to save time and determine the right direction. Record all observations:
| Observation / To Check | Details / To Note | Goal |
|---|---|---|
| Visual Inspection | Leaks, physical damage to meter/pipe/cabling, excessive vibration, insulation defects, correct installation orientation. | Quick identification of obvious mechanical problems. |
| Alarm history | Check the SCADA/DCS logs or internal meter diagnostics for errors, alarms, or warnings (e.g. 'sensor faulty', 'lower range', 'higher range'). | Provides insight into the nature and time of the occurrence of the fault. |
| Process parameters | Record actual values of pressure (bar), temperature (°C), liquid level, density, viscosity (cP) and other relevant process variables at the time of the error. Compare with normal operating values. | Detection of deviations in process conditions that can influence the flow measurement. |
| Recent Changes | Ask about recently performed maintenance, process changes (product, recipe), calibrations, or installation work in the area surrounding the flow meter. | Can demonstrate a direct correlation between a recent activity and the occurrence of the error. |
| Environmental factors | Check for electromagnetic interference (EMI) from nearby electrical equipment (motors, VFDs), strong external vibrations, extreme ambient temperatures, or humidity. | Potential external influences that could disrupt the electronics or measuring principles. |
| Grounding Status (Magmeters) | Check the integrity and correct connection of the flow meter grounding and the process line. | Crucial for the stability of the signal in electromagnetic flow meters. |
5. Systematic Diagnosis Flowchart
Follow this structured flowchart to isolate the root cause of flowmeter measurement errors. Always start at 'Start' and follow the paths based on observed symptoms and test results.
- Start: Anomalous Flow Measurement (None, Inaccurate, Erratic, Drift)
- Check Basic Function and Signal Integrity
- Is there any output from the flow meter (display, 4-20 mA, pulse)?
- No: No output.
- Check supply voltage: Measure with multimeter. Expected: 24 VDC (±10%).
- Result OK: Go to 1.1.1.2.
- Result NOT OK: Solve power supply problem (fuse, broken cable, defective power supply unit).
- Check signal wiring (4-20 mA, pulse): Measure resistance, check for opens or shorts.
- Result OK: Go to 1.1.1.3.
- Result NOT OK: Repair cabling.
- Check internal diagnosis of the meter: Read error codes via display or HART communicator.
- Error code present: Consult manual for specific error code solution.
- No error code / Problem persists: The problem probably lies with the sensor itself or primary measuring elements. Go to 1.2.
- Check supply voltage: Measure with multimeter. Expected: 24 VDC (±10%).
- Yes: Output present, but different. Go to 1.2.
- No: No output.
- Is there any output from the flow meter (display, 4-20 mA, pulse)?
- Evaluate Installation Effects
- Does the installation meet the minimum straights (upstream/downstream)? (e.g. 5D upstream, 2D downstream for DP meters; 10D/5D for vortex/ultrasonic; consult OEM manual and NEN-EN-ISO 5167 for specific requirements).
- No:
- Probable cause: Insufficient straight section, flow profile disturbance (swirl, turbulence).
- Action: Consider relocating the meter or installing flow conditioners/rectifiers.
- Yes: Go to 1.2.2.
- No:
- Is there excessive vibration at the meter? Use vibration analyzer (reference ISO 10816, > 4.5 mm/s RMS is problematic).
- Yes:
- Probable cause: External vibrations affect sensor (especially vortex, ultrasonic, Coriolis).
- Action: Isolate meter from vibration sources, check pump alignment/bearings.
- No: Go to 1.2.3.
- Yes:
- Is grounding correct and effective for electromagnetic flow meters? Measure resistance between meter housing/electrode and ground (< 10 Ohm).
- No:
- Probable cause: Improper grounding leads to noise and unstable measurements.
- Action: Improve grounding, check grounding cables and points.
- Yes: Go to 1.3.
- No:
- Does the installation meet the minimum straights (upstream/downstream)? (e.g. 5D upstream, 2D downstream for DP meters; 10D/5D for vortex/ultrasonic; consult OEM manual and NEN-EN-ISO 5167 for specific requirements).
- Evaluate Process Conditions
- Are the process temperature and pressure within the specified range of the flow meter? Measure with pressure and temperature meter. Check that T < max T meter, P < max P meter.
- No:
- Probable cause: Over/under range process conditions, possible phase change, density/viscosity deviations.
- Action: Optimize process, adjust compensation or consider other meter technology.
- Yes: Go to 1.3.2.
- No:
- Are there any changes in fluid composition (gas bubbles, solids, viscosity, density)? Check process logs, take samples.
- Yes:
- Probable cause: Gas inclusions (ultrasonic, magmeter), abrasive solids (erosion), change in density/viscosity (DP, vortex).
- Action: Remove gas via breathers, filter solids, reconfigure meter with new density/viscosity.
- No: Go to 1.4.
- Yes:
- Are the process temperature and pressure within the specified range of the flow meter? Measure with pressure and temperature meter. Check that T < max T meter, P < max P meter.
- Check for deposits / contamination
- Is there deposits or erosion in the pipe or on the sensor? Use an endoscope for internal inspection. Measure pipe wall thickness with ultrasonic thickness gauge to detect erosion or extreme scale.
- Yes:
- Probable cause: Deposits on electrodes (magmeter), on sensors (ultrasonic, Coriolis), or narrowing in orifice/Venturi. Erosion of measuring elements.
- Action: Clean meter and pipe, consider material adjustment, preventative cleaning cycles.
- No: Go to 1.5.
- Yes:
- Is there deposits or erosion in the pipe or on the sensor? Use an endoscope for internal inspection. Measure pipe wall thickness with ultrasonic thickness gauge to detect erosion or extreme scale.
- Check Calibration Status
- Has the flow meter been recently calibrated? What was the result? Check calibration certificates and dates. Recommended interval: annually (NEN-EN-ISO 10012).
- No / Last calibration deviation:
- Probable cause: Calibration drift due to aging, wear, mechanical stress.
- Action: Perform in-situ verification with a portable ultrasonic flow meter or send the meter to an accredited calibration laboratory.
- Yes / Calibration OK: If all of the above checks have failed to identify a cause, consider a deeper analysis of the signal processing or a defective transmitter. End of diagnosis for this flow meter; consider replacement.
- No / Last calibration deviation:
- Has the flow meter been recently calibrated? What was the result? Check calibration certificates and dates. Recommended interval: annually (NEN-EN-ISO 10012).
- Check Basic Function and Signal Integrity
6. Error Cause Matrix
This matrix provides an overview of common symptoms, their likely root causes, the diagnostic tests and the expected results.
| Symptom | Probable Causes (Priority) | Diagnostic Test | Expected Result at Confirmed Cause |
|---|---|---|---|
| No Output / '0' Reading | 1. No power supply / Cable break 2. Defective electronics transmitter 3. Complete blockage (DP meter) |
1. Multimeter on power terminals / cable resistance 2. Process calibrator (4-20mA loop check) / Internal diagnostic meter 3. Endoscope inspection / Pressure drop measurement over meter |
1. 0 VDC / Open circuit (∞ Ω) 2. No current output despite good input / Error code 'Transmitter Defect' 3. Visible blockage / Very high pressure drop |
| Continuous Low or High Measurement | 1. Sensor Error / Calibration Drift 2. Process off-spec (low/high flow) 3. Partial blockage/bypass flow |
1. Calibration check (in-situ or lab) / HART diagnosis 2. Compare with upstream/downstream measurements / Balance sheet account 3. Endoscope inspection / Pressure drop measurement |
1. Large deviation during calibration 2. Other measurements confirm low/high flow 3. Visible partial blockage / Unexpected pressure drop |
| Erratic / Fluctuating Reading | 1. Gas bubbles or solids in liquid 2. External Electromagnetic Interference (EMI) 3. Excessive vibration (Vortex, Ultrasonic) 4. Improper grounding (Magmeter) |
1. Visual inspection (sight glass) / Process analysis 2. Oscilloscope measurement on signal line / EMI detector 3. Vibration analyzer 4. Multimeter on earth resistance |
1. Visible bubbles/solids 2. Noise signal on oscilloscope 3. Vibration values > 4.5 mm/s RMS 4. Earth resistance > 10 Ω |
| Slow Drift / Systematic Deviation | 1. Calibration drift (component aging) 2. Process condition change (T, P, density, viscosity) 3. Light tarnish/coating |
1. Regular calibration check 2. Process analysis / Compare with lab data 3. Endoscope inspection |
1. Measurement value gradually deviates with repeated calibrations 2. Process parameters deviate systematically from reference 3. Visible light deposits/coating on sensors/walls |
| Deviation at High/Low Flow | 1. Insufficient straight section / Flow profile disturbance 2. Meter dimensioned too large/small 3. Damaged measuring element |
1. Check installation drawings / OEM requirements 2. Calculate theoretical pressure drop at high/low flow 3. Endoscope inspection |
1. Installation does not comply with minimum straight sections 2. Pressure drop outside specification range 3. Visible damage to orifice, vortex shedder |
7. Root Cause Analysis for Each Error
7.1. Installation effects
Why it happens: Flow meters require a fully developed and stable flow profile to measure accurately. Insufficiently straight inlets and outlets, bends, valves, pumps, or other piping components directly before or after the meter can disrupt the flow profile by creating turbulence, swirl, or asymmetrical velocity distributions. This mainly affects differential pressure meters (whose measurement depends on a stable velocity profile), vortex meters (which form vortices based on a stable profile), and ultrasonic meters (which send the sound signal through the fluid). Vibrations, from pumps or mechanical resonance, can directly affect the sensitive sensors of vortex and Coriolis meters, leading to noise on the signal or completely unreliable measurements. Improper grounding of electromagnetic flowmeters causes ground loops and introduces electrical noise into the low-level measurement signal, which seriously affects accuracy.
How to confirm: Check the installation drawings and compare them with the actual situation and the OEM installation requirements (e.g. NEN-EN-ISO 5167 for orifice plates). Use a vibration analyzer to measure vibration levels on and around the meter; values above 4.5 mm/s RMS (according to ISO 10816, good condition) indicate a problem. Check the grounding of electromagnetic flow meters with a multimeter; the resistance between the meter body and ground should not exceed 10 Ω.
Damage if unresolved: Persistent inaccuracy, loss of production, and in extreme cases wear of measuring elements due to incorrect flow conditions.
7.2. Process Condition Changes
Why it happens: Many flowmeter principles are sensitive to changes in the properties of the measured fluid. Temperature and pressure changes affect the density and viscosity of liquids and gases. This has direct consequences for differential pressure meters (where the measurement is dependent on density) and vortex meters (where the vortex frequency is somewhat dependent on the Re number, i.e. viscosity). Gas bubbles or trapped solid particles in liquids can scatter ultrasonic signals, disrupt electromagnetic fields, or clog differential pressure gauges, leading to unstable or incorrect readings. Phase change (e.g. cavitation due to too low pressure) also causes measurement errors, because the meter is designed for one specific phase.
How to confirm: Analyze the historical process data (SCADA/DCS) for correlations between measurement errors and fluctuations in temperature, pressure, or product mix. Take samples of the medium to verify the presence of gas or solids. A visual inspection through a sight glass may reveal gas bubbles or particles.
Damage if unresolved: Continuous incorrect batching, incorrect dosages, and potential damage to the meter from abrasive particles.
7.3. Calibration drift
Why it happens: Even the most rugged flowmeters experience calibration drift over time. This can be caused by the natural aging of electronic components, mechanical wear of moving parts (e.g. bearings in turbine meters, but also slight deformation of orifice plates or Coriolis measuring tubes), or exposure to extreme process conditions that lead to mechanical stress. Particularly in demanding environments with high temperatures, pressure cycles, or abrasive media, this drift can occur at an accelerated rate.
How to confirm: The most direct method is a recalibration. This can be done in-situ with a portable reference (such as a clamp-on ultrasonic meter) or, for the highest accuracy, by removing the meter and testing it in an accredited calibration laboratory (in accordance with NEN-EN-ISO/IEC 17025). Compare the new calibration results to the original factory calibration or the last known good calibration. An out-of-specification deviation confirms calibration drift.
Damage if unresolved: Long-term inaccuracy in process control, financial losses due to incorrect billing (if custody transfer), or non-compliance with regulatory requirements.
7.4. Scale / Contamination
Why it happens: Many process fluids, especially in the food, chemical, and wastewater industries, contain particles that can deposit on the internal surfaces of the flowmeter or measuring line. This can vary from hard mineral deposits (e.g. lime), organic biofilms, to polymerization products. In electromagnetic flowmeters, deposits on the electrodes can isolate them from the process fluid, weakening or blocking the inductive signal. In ultrasonic flow meters, deposits can dampen or deflect the ultrasonic pulses. With differential pressure meters (orifice plates, Venturi tubes), deposits lead to a narrowing of the flow opening and thus a change in the pressure difference at the same flow, which results in overestimation of the flow. Erosion caused by abrasive particles can in turn damage measuring elements and lead to incorrectly increased or decreased output.
How to confirm: Use an endoscope for visual internal inspection. For magmeters, check the resistance between the electrodes; an unexpectedly high resistance may indicate insulating deposits. Use an ultrasonic thickness gauge to check for abnormal deviations in pipe wall thickness that indicate significant internal scaling or erosion.
Damage if unresolved: Complete failure of the meter, increased pressure drop due to restriction, structural damage to the meter, and uncontrollable process operation.
8. Step-by-Step Troubleshooting Procedures
Once the root cause has been identified, the correction follows:
8.1. Solution Installation effects
- Disruption Flow profile:
- Solution: If possible, move the flow meter to a section of the pipe that meets the minimum straights (e.g. 5-20 x pipe diameter upstream, 2-5 x pipe diameter downstream, depending on meter type and pipe components).
- Alternative: Install flow conditioners or rectifiers directly before the meter. These effectively reduce swirls and turbulence. Ensure that these are installed in accordance with NEN-EN-ISO 5167 for differential pressure gauges.
- Verification: Monitor the stability of the flow measurement and compare with a reference measurement.
- Vibrations:
- Solution: Mechanically isolate the flow meter from vibration sources. Use flexible connections, vibration dampers, and check the alignment of nearby rotating equipment (e.g. pumps).
- Verification: Measure vibration levels again with a vibration analyzer; aim for values < 2.8 mm/s RMS (good condition).
- Improper Grounding (Magmeters):
- Solution: Check and repair ground connections. Provide a low-impedance ground path (< 10 Ω) between the flow meter, the pipe (if conductive) and the central ground point of the installation. Use proper grounding rings if the pipe is non-conductive or coated.
- Verification: Measure the ground resistance again. Monitor the stability of the 4-20 mA signal with a process calibrator.
8.2. Solution Process Condition Changes
- Abnormal Temperature/Pressure:
- Solution: Optimize process conditions to remain within the operational range of the meter. If this is not possible, the flow meter should be reconfigured with the new density and viscosity values, or consider installing a meter less sensitive to these variations (e.g. Coriolis meter for density independent mass flow).
- Verification: Monitoring temperature and pressure and comparing the flow measurement with known values.
- Gas bubbles / Solids:
- Solution: Install gas separators or air vents upstream of the flow meter. Implement filters to remove solid particles. Adjust flow meter settings for media with higher solids concentrations, if supported.
- Verification: Visual inspection after installation of breathers/filters. The measurement should become more stable.
8.3. Solution Calibration Drift
- Solution: Perform a recalibration. This can be done in the following ways:
- In-situ verification: Use a portable ultrasonic clamp-on flow meter to compare the existing meter. This method is fast, but accuracy is limited by the clamp-on meter and process conditions.
- Laboratory calibration: Remove the flow meter and send it to an accredited calibration laboratory (according to NEN-EN-ISO/IEC 17025) for a primary calibration against a reference standard. This provides the highest accuracy and a new calibration certificate.
- Verification: The meter must be within the specified accuracy limits after calibration. Keep the calibration certificate for compliance.
8.4. Solution Scale / Contamination
- Solution:
- Cleaning: Clean the flow meter and adjacent pipe sections. This can be done mechanically (brushing, scraping after disassembly) or chemically (by rinsing with suitable cleaning agents). For magmeters, carefully clean the electrodes.
- Material selection: If scale is a recurring problem, consider installing a flowmeter with internal materials that are less susceptible to adhesion (e.g. specific coatings or liners).
- Preventive Cycles: Implement periodic cleaning cycles as part of the preventive maintenance plan.
- Verification: Visual inspection after cleaning. The flow measurement should return to expected values and show stability.
9. Preventive Measures
Prevention is essential to ensure the longevity and reliability of flow meters.
| Root cause | Prevention strategy | Monitoring method | Recommended Interval |
|---|---|---|---|
| Installation effects | Correct installation according to OEM manuals and standards (NEN-EN-ISO 5167). Use of flow conditioners where straight stretches are limited. Vibration isolation of pipes. | Periodic visual inspection of installation. Vibration measurements at critical points. Earth resistance measurements (for magmeters). | Annually (visual), every 2-3 years (vibration/grounding) |
| Process Condition Changes | Stabilize process parameters (T, P, flow). Installation of breathers/gas separators and filters. Selection of appropriate flow meter technology for variable process conditions. | Continuous monitoring of process parameters (T, P, density) via SCADA/DCS. Laboratory analysis of medium. | Continuous (SCADA), Quarterly/Semi-annually (lab analysis) |
| Calibration drift | Regular calibration by an accredited lab (NEN-EN-ISO/IEC 17025). Selection of meters with long-term stability. | Comparison of in-situ verification with lab calibration. Analysis of historical calibration data. | Annually or according to NEN-EN-ISO 10012 and OEM recommendation. |
| Scale / Contamination | Selection of gauge with suitable materials/coatings. Automated in-situ cleaning systems (CIP). Periodic manual cleaning. Installation of filters upstream. | Endoscope inspection. Pressure drop monitoring across the meter. Analysis of process medium for contaminating particles. | Depending on process: monthly to semi-annually. |
10. Spare Parts & Components
The timely availability of critical spare parts is crucial for the rapid resolution of flow meter errors. Consult the UNITEC-D e-catalogue for a complete range.
| Item Description | Specification | When To Replace | UNITEC Category |
|---|---|---|---|
| Gaskets / Seals | Material (e.g. PTFE, Viton, EPDM), Pressure class (PN), Temperature class | With every disassembly of flange connections, in case of leakage. | Seals & O-rings |
| Electronic Printed Circuit Boards (Transmitter) | Specific model/revision of flow meter manufacturer, EMC/ATEX certification | When diagnosing defective electronics or communication errors. | Process instrumentation - Electronics |
| Electrodes (Magmeter) | Material (e.g. Hastelloy, Titanium, Platinum), Size | In case of wear, corrosion, irreparable deposits or loss of signal. | Flow meter parts - Electrodes |
| Liners (Magmeter) | Material (e.g. PTFE, PFA, hard rubber), Diameter | In case of wear, damage or delamination. | Flowmeter Parts - Liners |
| Orifice Plate / Venturi Insert | Material (e.g. stainless steel 316L, Hastelloy), Diameter, Pressure class, Flange size | In case of erosion, deformation, damage or irreparable blockage. | Measuring Openings & Restrictions |
| Signal cables / Ground cables | Shielded instrumentation cable (e.g. LiYCY), Earth cable (CU, correct cross-section) | In case of mechanical damage, insulation defects, excessive resistance. | Cabling & Connectors |
For a complete overview and direct ordering options, visit our UNITEC-D e-catalogue.
11. References
- NEN-EN-ISO 5167-1:2003, Measuring liquid flow with differential pressure devices in closed pipes – Part 1: General principles and requirements.
- NEN-EN-ISO 10012:2003, Measurement management systems – Requirements for measuring processes and measuring equipment.
- NEN-EN-ISO/IEC 17025:2017, General requirements for the competence of testing and calibration laboratories.
- NEN-EN-ISO 10816-3:2009, Mechanical vibrations - Measurement and assessment of vibrations of machines - Part 3: Industrial machines with a rated power above 15 kW and rated speeds between 120 rpm and 15 000 rpm when measured on site.
- NEN-EN 166:2001, Personal eye protection – Specifications.
- NEN-EN 374-1:2016+A1:2018, Protective gloves against hazardous chemicals and micro-organisms – Part 1: Terminology and performance requirements for risk.
- NEN-EN-ISO 20345:2022, Personal protective equipment – Safety footwear.
- NEN-EN-ISO 14118:2018, Safety of machines - Preventing unexpected start-up.
- Directive 2014/34/EU (ATEX), Equipment and protective systems intended for use in places where there may be a risk of explosion.
- Manufacturer-specific flow meter installation and maintenance manuals.