Ultrasonic · PS7021

Inline Ultrasonic Phase Separation Detector

Phase separation · integral spool

PS7021 decides the phase from sound velocity: time of flight over a fixed path gives the velocity, the amplitude of the same echo gives the scattering, and together they separate heavy phase, rag layer and light phase. Three volt-free relays drive the diverter valve directly. On a pair like dichloromethane and water — a third apart in density yet nearly identical in acoustic impedance — density and impedance instruments cannot tell the phases apart, while the velocities differ by 390 m/s. DN25 / DN32 / DN50 spools, 316L with sapphire windows or PTFE-lined.

Also known as phase separation detector, phase interface detector, liquid-liquid interface detector, extraction interface detector, phase separation sensor, oil-water interface detector

Best fit for
  • Fine chemicals and pharmaceutical intermediates: automatic phase cut when a reactor drains after extraction, washing or back-extraction
  • Phase discrimination between water and organics such as dichloromethane, chloroform, toluene, ethyl acetate and hexane
  • Interface monitoring at the outlet of settlers and coalescers on continuous separations
  • Wrong-tank alarm on solvent recovery loops: heavy phase entering the solvent tank, a full batch before the lab sees it
  • End-of-separation calls on water-wash stages in agrochemical and flavour synthesis
  • Oil / water separator outlets where the velocity gap clears the 30 m/s floor
Not recommended for
  • Pairs whose velocities differ by less than 30 m/s at working temperature (measure a sample; do not infer from the density gap)
  • Miscible systems such as ethanol / water or acetone / water, where no interface exists
  • Lines that routinely carry heavy gas or solids: the amplitude stays low and three-state discrimination degrades
  • Interface LEVEL in a tank or basin — that is an interface level analyser's job, not an inline spool's
  • Concentration measurement on a single phase (choose the PS7020 ultrasonic concentration meter)
  • Any position that cannot be kept full: free-draining lines, falls, siphon breaks

PISONICS | 西安派声

PS7021 series

Inline Ultrasonic Phase Separation Detector

Sound velocity + amplitude · integral spool · no moving parts

Extraction, washing, back-extraction: which phase is in the line right now

—— Phase separation is decided by sound velocity, not by density ——

【Output: heavy / emulsion / light, plus a continuous sound-velocity reading】

What It Is

PS7021 sits in the run between a reactor bottom valve and the diverter valve and answers a question that has a two-second window: is the liquid passing right now the heavy phase, the light phase, or the rag layer between them. Time of flight over a fixed acoustic path gives sound velocity; the amplitude of the same echo gives how much the medium scatters. Velocity separates the two clear phases; amplitude picks the emulsion out of them. Three volt-free relays drive the diverter valve directly.

It measures neither concentration nor density. The discriminator is sound velocity itself — which is what makes the instrument possible and what bounds it: the two phases must differ by at least 30 m/s at working temperature, and the pipe must run full. Colour, turbidity, conductivity, density and vibration play no part in the decision.

How It Works

A pair of transducers faces across the spool; the path length L is fixed by the mechanical build, the same platform as PS7020. The instrument measures arrival time t and reports c = L / t, and takes the peak amplitude A of the same echo as a measure of scattering and absorption. Three rules:

  1. velocity inside the light-phase band with normal amplitude → light phase;
  2. velocity inside the heavy-phase band with normal amplitude → heavy phase;
  3. velocity between the bands, or amplitude below the threshold → emulsion (rag layer), reported as not-decidable.

Which phase is the heavy one depends on the chemistry and is mapped once at commissioning: dichloromethane (1.33 g/cm³) is heavier than water and leaves the reactor first; toluene and ethyl acetate are lighter, so water leads. The instrument does not care about density — it cares which band the velocity falls into.

PS7021 sound-velocity phase separation: time of flight over a fixed path gives velocity, echo amplitude gives scattering, and the two together separate heavy phase, rag layer and light phase

Fig. 1 PS7021: velocity and amplitude read together

Temperature comes from a built-in Pt1000. Organic phases slow down as they warm (-2.7 to -4.9 m/s per °C) while water speeds up (+2.4 m/s per °C), so the contrast widens with temperature rather than closing. Thresholds shift linearly across the temperature band, keeping margin over the whole working range.

Why Not Density

Dichloromethane and water are the common pair on this duty, and the easiest pair to get wrong. Their densities differ by a third (1.33 against 1.00 g/cm³), so the first instinct is a density meter. But an ultrasonic density meter reads acoustic impedance Z = ρ × c, and on this pair the two factors cancel each other:

Temp.Water c, m/sDCM c, m/sΔcWater Z, MRaylDCM Z, MRaylΔZ
10 °C14471129-22 %1.451.52+4.9 %
20 °C14821090-26 %1.481.45-2.3 %
25 °C14971070-29 %1.491.41-5.5 %
35 °C15201031-32 %1.511.34-11.4 %

Around 15 to 20 °C the two impedances are effectively equal. The reflection coefficient at a sapphire face differs by less than 0.4 %, so an impedance instrument is blind through that band; inferred against water's velocity, DCM reads as about 0.98 g/cm³ — lighter than water, the wrong way round. The same pair differs by 390 m/s, about 26 % in sound velocity, with opposite temperature coefficients on top. That is why PS7021 belongs on the sound-velocity branch beside PS7020, not under the PS7000 impedance family.

Chloroform behaves the same way: impedance 1.47 against water's 1.48 MRayl, velocity 979 against 1497 m/s. As a rule, the heavier the halogenated solvent, the slower the sound and the closer its impedance sits to water's.

Thresholds, and Who Sets Them

The instrument ships without thresholds, and should. Sound velocity is an absolute quantity, but your two phases carry dissolved water, salt and product in proportions no handbook table knows. Commissioning is a two-phase calibration:

  1. at working temperature, draw one sample of each phase and read its velocity with the instrument itself — two measured points;
  2. the threshold sits between them, with hysteresis (10 % of the gap by default) so a stationary interface cannot chatter;
  3. the emulsion threshold is referenced to the clear-phase amplitude baseline — 6 dB below baseline by default;
  4. a confirmation window (0.3 s default, settable 0.1 to 5 s) rejects the dropout of a single passing bubble.

Delivery includes a velocity-versus-temperature table for both phases, so that a change of process temperature does not require a service visit. That table is the one thing this instrument needs from your plant, and the one number we will not print in a datasheet on your behalf.

Against the Alternatives

Half a dozen methods do this job, each resting on a premise. Choose by whether the premise holds, not by novelty:

MethodDiscriminatorPremiseOn DCM / water
ConductivityAqueous conducts, organic does notElectrodes may wet the process; aqueous conductivity stable and high enoughWorks, and is cheap. Weakens with pure-water washes or wet organics; awkward to tap into a lined line; electrodes need cleaning
Photoelectric / sight glassTransmittance, colour or refractionThe phases differ optically; the glass stays cleanDCM and water are both clear and colourless, so turbidity- and colour-based units fail; a refractive-index unit does work (1.424 against 1.333)
Density / DPDensity differenceSteady flow, enough static headThe density difference is real, but the response is too slow for a draining batch
Ultrasonic impedanceInterface reflectivityThe phases differ in ρ × cFails — the impedances coincide near ambient (see the table above)
RF admittance / capacitancePermittivity differenceCoating controlled, medium conductivity stablePermittivity differs widely (80 against 8.9), so it works; coating and conductivity drift are the error sources
Operator at a sight glassHuman judgementSomeone is watching, batch to batchWorkable; consistency depends on the shift, and handovers are where batches go wrong
Sound velocity, PS7021Velocity + echo amplitudePhases differ by ≥ 30 m/s; pipe runs full390 m/s apart, independent of colour, conductivity and density; the rag layer is caught by amplitude

No line in that table says the others do not work. A conductivity switch is cheaper wherever the aqueous phase conducts and an electrode may be fitted; a refractive sight-glass unit is as direct where the indices are far apart and the glass stays clean. The place sound velocity owns is both phases clear, both non-conducting, or an aqueous conductivity that moves — where none of those premises hold.

Typical Applications

  • Dichloromethane / water extraction — pharmaceutical intermediates and fine chemicals draining from the reactor bottom; DN32 is the common size
  • Solvent / water washing — interface detection on toluene, ethyl acetate and hexane circuits
  • Continuous separators: phase monitoring at the outlet of a settler or coalescer
  • Solvent recovery loops: an alarm when heavy phase runs into the light-phase tank, a full batch earlier than the lab would find it
  • Water-wash stages in agrochemical and flavour synthesis
  • Oil / water separator outlets, where the velocity gap clears the 30 m/s floor

Technical Specifications

ParameterSpecification
ModelPS7021 series inline ultrasonic phase separation detector (integral spool)
Measuring principleTime-of-flight sound velocity plus received amplitude, read together to identify the phase
Phase statesThree states: heavy phase / emulsion (rag) layer / light phase
Measured quantitiesSound velocity, received amplitude, medium temperature, phase state
Sound-velocity range400 to 3500 m/s
Sound-velocity resolution0.01 m/s
Sound-velocity repeatability±0.2 m/s (constant temperature, single phase)
Discrimination floorThe two phases must differ by at least 30 m/s at working temperature
Phase response time≤ 0.5 s; confirmation window settable 0.1 to 5 s
TemperatureBuilt-in Pt1000; resolution 0.01 °C, accuracy ±0.2 °C
Standard boresDN25 / DN32 / DN50 integral spools; other bores to order
Process connectionHG/T 20592 PN16 flanges; tri-clamp or wafer optional
Wetted materials316L with sapphire windows; PTFE/PFA lined with sapphire windows; Hastelloy C276 optional
Wetted sealsPTFE or FFKM; ordinary FKM is not used
Process temperature-20 to +80 °C; high-temperature variant -20 to +120 °C
Ambient temperature-20 to +60 °C
Pressure rating≤ 1.6 MPa; ≤ 1.0 MPa for the lined spool
Medium requirementsFull pipe; not for lines that normally carry heavy gas or solids
Analogue output2 x 4-20 mA, configurable as sound velocity or phase code (4 / 12 / 20 mA)
Relay outputThree volt-free relays (heavy / emulsion / light), 250 VAC 3 A
Digital communicationRS485 Modbus-RTU; HART 5 optional
Power supplyDC 24 V or AC 100-240 V
DisplayLocal display, bilingual menu, showing sound velocity, amplitude, temperature and phase
Ingress protectionIP66
Hazardous areaEx d IIC T6 Gb (optional)
CalibrationOn-site two-phase calibration: one sample of each phase, thresholds set over the working temperature band

Velocity range, resolution, electrical and hazardous-area figures are shared with the PS7020 platform. Bore sizes, relays, response time and pressure rating are specific to PS7021. A written selection confirmation governs any order.

Ordering

FieldCodeMeaning
Bore25 / 32 / 50 / SPDN25, DN32, DN50 standard spools; SP for a custom bore
WettedS / F / HS = 316L with sapphire windows; F = PTFE/PFA lined with sapphire windows; H = Hastelloy C276 with sapphire windows
OutputR0 / R3R0 = 4-20 mA x2 + RS485; R3 = R0 plus three relays (heavy / emulsion / light)
ExN / EN = general purpose; E = Ex d IIC T6 Gb
Temp.T1 / T2T1 = -20 to +80 °C; T2 = -20 to +120 °C

Example: PS7021-32-F-R3-E-T1 = DN32 PTFE-lined spool with sapphire windows, three relays plus 4-20 mA and RS485, Ex d IIC T6 Gb, standard temperature.

Installation

  • A full pipe is not negotiable. Mount downstream of the bottom valve and upstream of the diverter; never in a free-draining fall or a run that can go part-full
  • As close to the diverter as the layout allows. A DN32 line holds about 0.80 L per metre (0.53 L for the 26 mm lined bore) — that volume is what passes between the call and the valve
  • On horizontal runs, put the path across the horizontal (transducers at 3 and 9 o'clock): gas rides the top, solids sit on the bottom, the horizontal chord is the clean one
  • On vertical runs prefer upward flow, or keep back-pressure so no cavity forms
  • The path is fixed by the spool, so no straight-run requirement applies; still avoid positions that generate gas continuously, such as immediately after a pump or a control valve
  • Lined spools carry vent holes in the shell — do not plug them. Chlorinated solvents permeate fluoropolymer liners slowly and the permeate needs a way out
  • In hazardous areas wire to Ex d IIC T6 Gb practice, with cable entry and bonding per site rules

Field Behaviour and How It Fails

This instrument fails in specific, predictable ways. They belong here rather than on page 40 of a manual:

SymptomCauseBehaviour and remedy
Amplitude drops, state goes to not-decidableGas or flashing. DCM boils at 39.6 °C, so vacuum transfer or a hot summer line breaks out vapourBy design it reports emulsion / not-decidable and the interlock takes the conservative side (hold the current valve position). That is a decision, not a fault
State toggles between two valuesThe interface is parked on the acoustic pathHysteresis and the confirmation window absorb it; raise the window from 0.3 s to 1-2 s on site
Slow one-way driftFilm or crystal layer on the sapphire windowThe amplitude baseline drops first; the sapphire face cleans with a rinse or a wipe
A phase reads differently batch to batchThat phase changed — water content, salt, product concentrationNot instrument drift. Re-establish the band for the new composition, or widen the threshold band
Liquid weeping from a lined spool shellLiner breached, or permeation accumulatingTake it out of service and inspect. This risk is inherent to lined pipe; clear vent holes delay it, nothing removes it

What we need before quoting a model code: composition of both phases and the working temperature range; line size and material (lined or not); diverter valve type and its distance from the measuring point; whether the aqueous phase carries salt or acid; and the area classification. If the velocities are uncertain, send 500 mL of each phase and we will measure both bands before quoting — which serves both sides better than copying a number out of a brochure.

Precision beyond limits

For non-standard ranges, special wetted parts, or hazardous-area variants — talk to a Pisonics engineer.

Frequently asked questions

Dichloromethane is far denser than water — why not use a density or acoustic-impedance meter?

Because an ultrasonic density meter reads acoustic impedance, Z = ρ × c, not density, and dichloromethane happens to be dense and acoustically slow, so the two factors cancel. At 20 °C water is 1.48 MRayl and DCM about 1.45 MRayl, and between roughly 15 and 20 °C they coincide — which is where most plants separate. Inferred against water's velocity, DCM reads about 0.98 g/cm³: lighter than water, the wrong way round.

The same pair differs by 390 m/s in sound velocity (1482 against 1090 m/s, about 26 %), with opposite temperature coefficients, so warming widens the gap. That is why this duty takes the sound-velocity model (PS7021) rather than the impedance one (PS7000). DP and Coriolis meters do read true density and can separate the pair in principle, but they cannot keep up with a draining batch.

How is the rag layer handled — can it be mistaken for the aqueous phase and let through?

The rag layer is a third state, not a grey zone between two. Two quantities catch it.

First, velocity: a dispersion falls between the two bands (Wood's equation, first order, puts 30 vol% DCM near 1338 m/s and 50 vol% near 1256 m/s), and anything outside the clear-phase bands is not reported as a clear phase. Second, and more decisively, amplitude: droplet scattering weakens the echo, and 6 dB below the clear-phase baseline is reported as emulsion / not-decidable by default.

The interlock direction is fixed: on emulsion the instrument holds the valve and raises an alarm rather than switching. It will stop and wait for an operator before it lets a rag layer pass as either phase. The emulsion itself is a separation problem; what the instrument can do is refuse to wave it through.

Our line is DN32 and PTFE-lined — can this be fitted, and what happens at the liner?

Yes. DN32 is one of the standard bores (DN25 / DN32 / DN50). The lined build is a steel shell with a PTFE/PFA liner and sapphire windows that pass through the liner and wet the process.

Measuring through the liner is not an option: PTFE is 2.97 MRayl and strongly attenuating, and the bond between liner and shell changes with temperature and permeation — that turns a fixed acoustic path into a drifting one.

Two ordinary lined-pipe rules also apply. Wetted seals are PTFE or FFKM; ordinary FKM rates only fair against methylene chloride. And the shell's vent holes must stay clear — chlorinated solvents permeate fluoropolymer liners slowly, and trapped permeate lifts the liner off the wall.

Against conductivity and photoelectric (sight-glass) detectors — when should each be chosen?

Choose by whether the premise holds; each method rests on one.

Conductivity assumes the aqueous phase conducts, the organic does not, and an electrode may wet the process. Where that holds it is the cheapest answer. Pure-water washes, wet organics and lined pipe that is awkward to tap all soften it.

Photoelectric / sight glass assumes an optical difference. Turbidity- and colour-based units fail outright on dichloromethane and water — both are clear and colourless — while a refractive-index unit does work (1.424 against 1.333). Both share one weakness: a fouled window.

Sound velocity (PS7021) rests on two conditions only: the phases differ by at least 30 m/s, and the pipe runs full. It is independent of colour, turbidity, conductivity and density, which is why it holds where both phases are clear, both are non-conducting, or the aqueous conductivity moves. The price is a two-phase calibration on site, repeated at product changeover — five minutes, but somebody has to do it.

The item-by-item comparison is here.

Does commissioning need a shutdown, and how are the samples taken?

No shutdown. Calibration needs two velocity bands, and both samples come out of a normal batch: one while the light phase is running steady, one while the heavy phase is, 200 mL or more each. The instrument reads them itself — nothing goes to a lab. It usually fits inside one batch.

Three cautions: sample at process temperature (velocity is temperature sensitive, organics run −3 to −4 m/s per °C); draw the sample near the measuring point; and take the aqueous phase at its real salinity — clean water is not a substitute.

What you end up with is a velocity-versus-temperature table for both phases, delivered with the instrument. If the process temperature changes later, the thresholds shift along that table without a service visit.

How do the three relays drive a diverter valve, and which way does it fail?

Three volt-free contacts carry heavy, emulsion and light. The usual wiring: heavy closed → diverter to the heavy receiver; light closed → light receiver; emulsion closed → hold the current position and alarm for an operator to confirm.

The failure direction is the first thing to settle. Gas, flashing and window film all push the instrument toward not-decidable rather than toward the other phase, so making not-decidable mean stay put runs with the grain of the disturbances. Defaulting it to either phase turns every disturbance into a carry-over incident.

Keep the manual mode and the existing sight glass: the instrument supplies the judgement, not the valve. 4-20 mA trends velocity in the DCS; RS485 exposes phase, velocity, amplitude and temperature for the batch record.

How is it accepted on site — what do you compare it against?

The output is a phase decision, not a concentration you can compare against a titration, so acceptance looks different from a concentration meter's. Three workable tests:

1. Timing against the operator. Run a number of batches and align the instrument's switch instant with the operator's call at the sight glass. The site sets the tolerance; what usually matters is whether the instrument is ever late, since late means carry-over.

2. Sampling around the cut. Draw a sample either side of the instrument's switch instant and check that carry-over sits inside process limits.

3. The velocity itself. Measured band values should match the calibration table, and batch-to-batch drift in one phase should stay within the repeatability seen at calibration (±0.2 m/s). This is the test that separates "the instrument drifted" from "the material changed".

Can it measure how thick the rag layer is, or where the interface sits in a tank?

No — those are different instruments. PS7021 is an inline spool and knows only what is crossing its acoustic path right now: heavy, emulsion or light.

Interface height in a tank or settler belongs to an interface level instrument (magnetostrictive, radar, ultrasonic level, capacitance), mounted on the vessel rather than in the line. Rag layer thickness is the same question.

There is a useful indirect answer, though: time the instrument spends in the emulsion state during a drain, multiplied by flow, gives the volume of rag in that batch. It is not an interface height, but as a trend for how well the break worked or whether settling time is enough, it is often the more direct number.

Does it need a straight run? Can it go right after a pump or a control valve?

No straight run is required. The path length is fixed by the spool and the discriminators are velocity and amplitude, which do not care about the flow profile — unlike DP, vortex or magnetic meters, which live on it.

The position still matters, but for a different reason: phase and gas. Pump discharges, the downstream side of control valves and other throttling points generate gas or flashing continuously, which holds the amplitude down and degrades three-state discrimination. Mount upstream of them, or further downstream where the flow has settled.

Three other rules: a full line is not negotiable; on horizontal runs put the path across the horizontal (3 and 9 o'clock), away from gas at the top and solids at the bottom; and keep the measuring point close to the diverter, because that hold-up is the mixed volume every batch pays.

What about high temperature, sanitary execution and CIP?

Temperature: −20 to +80 °C standard, −20 to +120 °C for the high-temperature variant. Heat actually helps the discrimination: organic velocity falls with temperature while water rises below 74 °C, so the bands spread. Edible oil washing at 80-90 °C is the textbook case.

Sanitary: the standard spool is industrial and flanged. Tri-clamp, polished bore and drainable geometry are a custom build with their own lead time and price — say so at selection rather than assuming the standard spool can enter a sanitary zone.

CIP: the sapphire window is dense and smooth, so hot caustic, hot water or solvent all clean it in place. Compare the amplitude baseline before and after and you know whether the clean worked — far easier than scheduled teardown.

Can it still work if the line carries solids or crystals?

It depends on the load. A light suspension does not move the velocity reading but scatters sound and lowers the echo amplitude — and amplitude is what catches the rag layer, so with heavy solids three-state discrimination degrades to two: light and heavy still separate, emulsion and "solids present" no longer do.

In practice: put the point after settling, filtration or a steady pump; at commissioning re-baseline the amplitude against the real solids-bearing fluid rather than against clear liquid; and if solids content is itself the quantity you want, that is another instrument — PS7000 and the acoustic-impedance method.

Crystals add one more wrinkle: they grow a film on the window. The film shows in the amplitude baseline first, which makes that baseline a useful clean-me reminder.

How wide does the velocity gap have to be, and can it be estimated first?

The floor is 30 m/s at working temperature. Common organic-against-water pairs are far above it: carbon tetrachloride is 572 m/s from water, dichloromethane 428, ethyl acetate 413, toluene 170, m-xylene 155 (handbook values at 25 °C). For those the gap is never the constraint.

Three cases do need arithmetic first: oil against oil (diesel and kerosene are 74 m/s apart), oil against water at ambient (edible oil and water, about 66), and formulated fluids — peroxide working solution, SX organic, a demulsified waste oil.

How to estimate: take handbook values at 25 °C, carry both to working temperature with their coefficients (organics −2.7 to −4.9 m/s per °C, water about +2.4 below 74 °C), then add salt on the aqueous side (roughly +11 m/s per wt% NaCl). Above 100 m/s you are safe; 30 to 100 needs a measurement; below 30, don't.

How many products can one instrument cover, and does a changeover need recalibration?

Eight recipes as standard, each holding a pair of velocity bands and its amplitude threshold; the list extends. Switch from the panel, or let the DCS write a Modbus register — the second follows the batch instruction and removes the "nobody switched it" class of incident.

A product that has never been calibrated needs one pass: two samples, two readings, one stored pair — five minutes, no return-to-factory sampling. Coming back to a known product just recalls its recipe.

When to redo an existing recipe: the composition of that phase moved (water content, salt, product concentration), the temperature band shifted, or acceptance found measured velocity off the stored band by more than the repeatability. Every recalibration records its time and both velocities for the batch record.

How often does the sapphire window need cleaning, and how do you know?

No fixed interval — it depends on the duty. What actually helps: the instrument tells you.

As film, crystal or oil builds on the window, the velocity reading does not move at first, but the amplitude baseline drifts down. Trend the clear-phase baseline: a slow decline means clean it; a sharp drop with velocity still in band is an emulsion slug passing, not deposit. The two shapes are easy to tell apart on a trend.

How to clean: sapphire is dense and smooth, so hot caustic, hot water or a normal solvent will do it, usually in place. On duties that will certainly film — edible oil, spent emulsions — put it on the CIP schedule. Afterwards check whether the amplitude baseline came back: that is the acceptance test for the clean.

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