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Xi'an Shenghongchuang Instrument Co., Ltd.
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Email: shc-sensor@qq.com
Address: Fortune Building, Sanqiao Street, Xixian New Area, Xi'an, Shaanxi Province
Whether a piezoelectric level sensor can be used for viscous liquids cannot be determined solely by the statement that “the liquid has high viscosity.” These products typically use a pressure-sensing element to detect the hydrostatic pressure of the liquid column and then convert it into liquid level height. In principle, they can be used for continuous level measurement of certain viscous liquids, provided that the medium density remains relatively stable and the liquid column can effectively transmit pressure.
In actual projects, the key factor affecting results is not the viscosity value itself, but whether the medium continuously adheres to the probe diaphragm, pressure port, or mounting flange. Media such as resins, greases, syrups, slurries, inks, and adhesives have poor flowability and can easily leave deposits as the liquid level rises and falls. Long-term accumulation can alter the condition of the pressure-sensitive surface.
Therefore, piezoelectric level sensors are more suitable for media with moderate viscosity, relatively stable flow processes, and no rapid curing or scaling. For operating conditions involving high viscosity, easy solidification, fibrous particles, or frequent start-stop agitation, the mounting structure, diaphragm material, measuring range allowance, and maintenance interval should all be considered during selection.
Hydraulic oil, gear oil, fuel oil, glycerol solutions, and certain greases that remain flowable at low temperatures can generally be measured using submersible or flange-mounted piezoelectric level sensors. For such media, a flush diaphragm structure is recommended to avoid pressure-guiding structures with small openings that are prone to retaining media.
If the viscosity of the measured medium is between tens and hundreds of mPa·s, and there is no obvious crust formation, sedimentation, or solid-phase stratification in the tank, the hydrostatic pressure method generally offers good cost-effectiveness. The measuring range should preferably cover 1.2 to 1.5 times the normal liquid level, allowing room for level fluctuations while reducing the risk of errors caused by long-term full-scale operation.
When viscosity rises above several thousand mPa·s, the sensor is not necessarily unusable, but changes in medium temperature need to be verified. A temperature decrease may significantly reduce liquid flowability and cause diaphragm buildup; a temperature increase may alter density, resulting in noticeable deviations in liquid level calculated from liquid-column pressure.
The table above is intended only for preliminary screening and cannot replace sample testing. In particular, the viscosity and adhesion condition of the same type of resin or oil may vary substantially depending on batch, additives, and on-site temperature. For high-value raw materials or continuous production equipment, simulated operating-condition verification for no less than 24 hours is recommended first.
For applications requiring frequent tank cleaning, flush diaphragm flanges, sanitary clamps, or removable probes are more convenient for maintenance. The sensor mounting position should also avoid directly below the inlet, the impact area of agitator blades, and areas where return liquid columns are concentrated, in order to reduce the effect of instantaneous pressure fluctuations on signal stability.
Xi'an Shenghongchuang Instruments and Meters Co., Ltd. can match pressure, level, and intelligent digital display control instrument solutions for customers based on medium samples, tank structure, and control requirements. For projects requiring non-standard flange sizes, high-temperature-resistant leads, or special corrosion-resistant materials, operating-condition parameters should be clearly specified during the design stage.
Residue on the diaphragm surface creates additional mechanical stress, which may appear as a zero point that does not return promptly after the level falls, or as slow changes in readings. If the residue layer continues to thicken, the error may gradually increase from a few millimeters to several centimeters. When this trend occurs, recalibration alone often cannot fundamentally resolve the issue.
Agitation, circulation pumps, or high-level material feeding can cause viscous liquids to entrain bubbles. Bubbles alter the local effective density and can also cause short-term fluctuations in the pressure signal. The control system can be configured with damping or moving-average processing from 3 seconds to 10 seconds, but excessive damping should be avoided, as it will reduce the response speed of level alarms and interlocks.
Hydrostatic conversion depends on medium density. For example, for a liquid with a density of 1.00g/cm³, a 10-meter liquid column corresponds to approximately 100kPa; when the density changes to 0.90g/cm³, the pressure at the same liquid level decreases by approximately 10%. If formulation temperature varies significantly or oil-water stratification exists, the density compensation method should be rechecked.
For sealed tanks, the influence of vapor-phase pressure must not be ignored. When positive or negative pressure exists in the tank, a differential pressure level transmitter should be selected, or the reference side should be correctly connected to the vapor space. If a standard gauge-pressure product is still used, changes in vapor-phase pressure will be mistaken for changes in liquid level.
Under high-temperature operating conditions, it is also necessary to confirm the allowable ambient temperature of the sensor electronics housing, diaphragm temperature resistance, and cable temperature rating. The applicable medium temperature range of conventional products differs from that of products with heat-dissipation structures or remote seal structures, so procurement must not be based solely on room-temperature parameters.
If a PLC system is already installed on site, 4-20mA output is suitable for interference resistance and long-distance analog signal acquisition; RS485 communication facilitates the reading of multiple parameters, including liquid level, temperature, and fault status. When wiring distance exceeds several hundred meters, communication quality should be assessed in combination with cable specifications, grounding methods, and terminating resistors.
For open tanks, a submersible level sensor can be selected according to depth, but the probe should be fixed in a stable position to prevent long-term swinging and collision with the tank wall. For viscous liquids, a clearance of 50mm to 150mm should be maintained between the probe end and the tank bottom to reduce zero drift caused by bottom sediment covering the pressure-sensitive surface.
For sealed tanks, reactors, and pressurized storage tanks, flange-mounted flush diaphragm pressure transmitters or differential pressure level transmitters are more suitable. The flange face should be as flush as possible with the inner wall of the vessel to avoid dead zones. For equipment with an insulation jacket, flange neck length and installation space should be confirmed in advance.
In terms of materials, 316L stainless steel is suitable for most oils and general chemical media. When encountering strong acids, strong alkalis, or chloride-containing media, Hastelloy, tantalum diaphragms, or PTFE sealing components should be further evaluated. Material selection must take into account medium concentration, temperature, pressure, and cleaning solution composition.
Piezoelectric level sensors can be used for certain viscous liquids, but they are more suitable for applications where the medium is flowable, density is relatively stable, and material buildup is controllable. For highly viscous resins, adhesives, asphalt, or easily cured slurries, flush diaphragm flanges, remote seals, or other non-contact measurement solutions are generally worth prioritizing for comparison.
Before purchasing, it is recommended to compile the medium name, maximum viscosity, temperature range, density, tank height, tank pressure, mounting port dimensions, whether agitation is present, and the required output signal. The more complete the parameters are, the easier it is to determine the level sensor measuring range, diaphragm material, protection rating, and mounting method in one step.
If a level sensor needs to be configured for a viscous liquid storage tank, the above operating-condition data and on-site installation photos can be provided to the technical personnel of Xi'an Shenghongchuang Instruments and Meters Co., Ltd. Professional personnel can then conduct structural verification, provide selection recommendations, and assess non-standard customization, reducing subsequent issues such as material buildup, fluctuations, and frequent maintenance.
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