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LPG Vapor Swirl Flow Meter

Peakshave & Industrial LPG Vapor

Accuracy of ±0.5% of rate
Temperature service −40 to +250 °C
Turndown ratio of 1:30

  • Line sizes DN25 to DN200
  • Flange ratings PN16 to PN40 (ANSI 150 to 300 LB)
  • Built-in T+P compensation + four blend profiles
↓ Request datasheet (PDF)
LUXB Swirl Flow Meter; instrument body

The LPG Vapor Swirl Flow Meter measures vapor-phase LPG on peakshave plants, propane-air mixing skids, and industrial site-supply lines. The LUXB precession swirl principle delivers ±0.5% accuracy across a 1:30 turndown.

316L stainless wetted parts and CNEX Ex d IIC T6 Gb ship standard, with a factory K-factor calibration certificate. Lead time stays 5–7 business days from the factory.

Benefits

  • ±0.5 % of rate: LUXB-VRd delivers ±0.5 % reference-volume accuracy at 1:30 turndown; fits utility-grade LPG sub-measurement and peakshave fuel accounting.
  • Built-in T+P compensation: integrated RTD + pressure transducer output Nm³/h directly, no external multivariable transmitter.
  • Heat-trace termination box: integrated termination on the meter housing handles Joule-Thomson drop downstream of vaporisers/regulators; no field-spliced heat trace.
  • Blend profile selection: four pre-loaded; US HD5 propane (≥90% C3), EU 70/30 and 50/50 C3/C4, and 60/40 LPG-air peakshave.
  • Hazardous-area certification: CNEX Ex d IIC T6 Gb (Zone 1) standard; IP65/IP66/IP67 + EMC 2014/30/EU standard.
  • Lead time: every configuration ships in 5–7 business days from factory.

Quick specifications.

Measurement PrinciplePrecession swirl with on-board blend-correct density + factory heat-value table computing
Line SizesDN25 – DN200 (1″ – 8″)
Media SupportedPropane (C3) · Butane (C4) · Mixed commercial · LPG-air peakshave 60/40
Blend ProfilesUS HD5 (90% C3) · EU 70/30 winter · EU 50/50 summer · Peakshave 60/40 · Custom
Accuracy±0.5 % of rate standard · ±1.0 % of rate economy · ±0.2 % repeatability
Turndown Ratio1:30 standard · 1:15 economy
Pressure0.1 MPa – 1.6 MPa (post-regulator / post-vapouriser range)
Medium Temperature-20 to +60 °C (heat-trace termination for J-T anti-condensation)
Wetted Parts316L Stainless standard · Duplex 2205 for sulfur-odourised LPG
Pressure-Vessel Construction316L stainless body standard · Hastelloy C upgrade · designed to NFPA 58 LP-Gas Code
Heat-Trace TerminationIntegrated box on housing; 24 V DC or 230 V AC with thermostat, 30 W/m sizing
Heat-Value OutputkJ/Nm³ + kWh/h (factory heat-value table, blend-matched)
Output Signal4–20 mA (Nm³/h) + 4–20 mA (kWh/h) · Pulse · RS485 Modbus RTU · HART · GPRS
Hazardous AreaEx d (CNEX flameproof) standard (covers IIA propane/butane + IIB ethylene traces) · Zone 1
ApprovalsCNEX Ex d IIC T6 Gb · IP65 / IP66 / IP67 · EMC 2014/30/EU

Configure your build.

Select your specs; we’ll generate a LUXB-LP 13-position model code and ballpark price. Submit to engineering for verified sizing against your vapouriser capacity, blend ratio, and trade-grade regime within 4 business hours.

Your Configuration

LUXB-LP-50-U-A-Ex-3-T3-4-H5-FL-B2-HT2-S
Pipe sizeDN50
TransmitterLUXB-S Integral
Accuracy±0.5 % of rate
Blend profileUS HD5 propane
Flange ratingPN16
Heat-trace230 V AC integrated
Composition inputFixed profile
Approval pack+ Calibration cert
Estimated unit price
Verified after engineer review
$3,280
Subtotal (× 1)$3,280
🛒 Add to Cart 📩 Request Detailed Quote
✓ Factory K-factor calibration certificate bundled
✓ Four blend profiles pre-loaded
✓ Heat-trace termination integrated
✓ Reply within 4 business hours

Typical applications

🏭

Propane Vapouriser → Process Heating

Glass tempering, ceramic kiln, secondary smelter, paint cure oven. PN16 DN50–DN100, utility-grade sub-meter, kWh/h to plant EMS.

🏘️

Rural LPG-Air Peakshave Injection

Peakshave plants injecting LPG-air 60/40 into NG grid for winter demand. Profile locked at commissioning, DN100–DN200 sizing.

🛢️

Petrochemical Fuel Gas Ring Main

Refinery/petrochem fuel-gas ring; mix of LPG, refinery off-gas, occasional H₂ traces.

Specifications

Performance

Reference volume accuracy±0.5 % of rate standard · ±1.0 % of rate economy
Heat-value accuracy±0.8 % at locked blend profile (factory heat-value table)
Temperature measurement±0.2 °C (Pt1000 RTD, integrated)
Pressure measurement±0.1 % FS (piezoresistive, 316L isolated diaphragm)
Repeatability±0.2 %
Turndown ratio1:30 standard · 1:15 economy
Velocity range2 – 50 m/s (gas); 1.5 m/s minimum at low pressure

Process & Environment

MediumPropane · butane · mixed C3/C4 · LPG-air peakshave 60/40 · refinery fuel gas
Composition rangeC3 10–100 % · C4 0–90 % · air 0–40 % (peakshave) · trace ethylene/H₂ (refinery)
Pressure range0.1 MPa – 1.6 MPa (matched to flange rating; PN16 / PN25 / PN40)
Temperature range-20 to +60 °C (medium, with heat-trace) · -20 to +60 °C (ambient)
Enclosure ratingIP66 standard · IP67 outdoor-unsheltered

Blend & Heat-Value

Blend profilesUS HD5 · EU 70/30 · EU 50/50 · Peakshave 60/40 · Custom
Density auto-correctionOn-board density table per profile; HD5 1.88, EU 70/30 2.14, 50/50 2.20, peakshave 1.43 kg/Nm³
Heat-value calculationFactory heat-value table, gross calorific value, blend-matched
Heat-value output unitkJ/Nm³ · MJ/Nm³ · kWh/h · MW (configurable)
Composition inputFixed profile · HART from inline GC · RS485 Modbus from composition analyser

Materials & Construction

Wetted parts (standard)316L Stainless body + swirl-generator vanes
Wetted parts (sulfur-odourised)Duplex 2205; for odourant-saturated service (ethyl mercaptan, tetrahydrothiophene)
Heat-trace terminationIntegrated housing box; 24 V DC or 230 V AC, IP66, thermostatic control
HousingAluminium alloy, IP66 epoxy-coated · Ex d certified · 316 stainless option
Lead-seal pointsHousing + wiring gland; trade-grade configurations
Net weight (DN50)9.8 kg (LUXB-S integral, PN16 flange, 316L, with heat-trace box)

Flow range by pipe size.

Reference volume in Nm³/h at standard conditions (101.325 kPa, 0 °C; IUPAC STP). Tabulated at 0.3 MPa gauge post-regulator pressure with US HD5 propane profile. Thermal-power column computed at HD5 gross heating value (93 MJ/Nm³ ≈ 25.8 kWh/Nm³). For EU 70/30 blend multiply thermal power by 1.11; for 50/50 by 1.16; for peakshave LPG-air 60/40 multiply by 0.41.

Pipe sizeMinimum (Nm³/h)Typical range (Nm³/h)Maximum (Nm³/h)Thermal @ HD5
DN25 (1″)816 – 120260up to 6.7 MW
DN40 (1½″)2245 – 320680up to 17.5 MW
DN50 (2″)3265 – 4901,040up to 26.8 MW
DN80 (3″)75150 – 1,1802,520up to 65 MW
DN100 (4″)120240 – 1,9004,080up to 105 MW
DN150 (6″)270540 – 4,2509,120up to 235 MW
DN200 (8″)480960 – 7,56016,200up to 418 MW

Installation

LPG vapor fails on J-T condensate and paperwork. Five rules keep calibration valid and heat-value defensible.

  1. Vapor phase only; never liquid-phase LPG piping LUXB-LP is designed for post-vapouriser vapor.
  2. Heat-trace the last 2 × DN upstream Avoids J-T condensate rain. Meter’s integrated termination handles the body only, not upstream pipe.
  3. Specify Ex d (CNEX flameproof); not IIA, not T4 Propane/butane alone are IIA, but refinery fuel gas, peakshave, and H₂ traces shift to IIB or IIC.
  4. Lock blend profile at commissioning Utility-grade sub-measurement requires blend lock per the supply contract.
  5. Plan periodic calibration re-verification Internal-verification cycles typically 2 years; align site verification with plant calibration program.

Frequently asked questions

Why specify a precession swirl meter for LPG vapor service instead of a turbine or positive-displacement meter?+
Three reasons that matter for LPG vapor. (1) No rotating wetted parts: rotating-element meters (PD or turbine) on LPG vapor service see wear from propane’s weak lubricity; the swirl meter has no rotating wetted parts, only a fixed swirl generator and external piezoceramic sensors. Service interval moves from annual gasket / rotor swap to visual inspection only. (2) Wide turndown at trade accuracy: 1:30 turndown at ±0.5 % of rate handles the full operating range without the PD meter’s pulsation-damping chamber. (3) Post-vapouriser tolerance: LPG at the vapouriser outlet is often just above its dewpoint and drops further through the Joule-Thomson effect; a PD meter’s rotor clearance changes with liquid carryover, while the swirl meter’s piezoceramic sensors are behind the pipe wall and don’t care about occasional liquid mist. The design supports utility-grade sub-measurement against a factory K-factor calibration certificate at a lower total cost of ownership than the PD alternative.
US HD5 propane versus European mixed commercial butane; what actually changes in the meter?+
The density and heating value shift by about 30 %, so the blend correction is not optional. US HD5 propane is ≥ 90 % C3 (propane) with ≤ 5 % C3H6 propylene and ≤ 5 % other hydrocarbons; density at STP about 1.88 kg/Nm³, heating value about 93 MJ/Nm³ gross (25.8 kWh/Nm³). European commercial LPG is a variable C3/C4 blend; typical winter grade is 70 % propane / 30 % butane, summer grade can run to 50/50; density at STP 2.14 kg/Nm³ (70/30) to 2.20 kg/Nm³ (50/50), heating value 103–108 MJ/Nm³. Peakshave LPG-air 60/40 is LPG diluted with air to match natural-gas heating value on a grid; density 1.43 kg/Nm³, heating value 38 MJ/Nm³ (deliberately matched to NG). The LUXB-LP ships with all four blend profiles pre-loaded. Select the profile at commissioning through the local HMI or Modbus; the meter applies the matched density and factory heat-value table every cycle. A custom blend can be loaded if your site runs a non-standard composition.
What is the Joule-Thomson effect in LPG vapor service, and how does the heat-trace termination handle it?+
When liquid LPG in the storage tank flashes to vapor across the vapouriser or regulator, it absorbs heat from the surrounding piping; the Joule-Thomson effect. Propane entering the vapouriser at +10 °C can exit at -10 °C; mixed butane blends at 0 °C can exit at -20 °C. If the downstream piping is not heat-traced, condensate reforms on pipe walls, drips into the meter, and introduces slug-flow noise into the swirl precession period. The LUXB-LP body has an integrated heat-trace termination box as a standard option: a weatherproof terminal block on the meter housing ready to accept 24 V DC or 230 V AC with thermostat loop, sized for 30 W/m on the meter body’s external surface. Set the thermostat to +15 °C minimum and the meter body stays well above the propane dew point regardless of ambient. No separate J-box, no field-spliced heat trace, no condensate slug-flow.
Why CNEX Ex d (flameproof, Zone 1) for LPG rather than IIA T3 as some catalogs list?+
Propane and butane are gas group IIA under IEC 60079-20-1; strictly, an IIA T3 (200 °C) certified meter is compliant with code. But many LPG facilities; petrochemical fuel gas rings, peakshave plants, and industrial vaporizer outlets; also see ethylene or hydrogen traces at small concentrations, which are gas group IIB and IIC respectively. IIB T3 certification covers both IIA (propane/butane) and IIB (ethylene), with a modest cost premium and no performance penalty. The LUXB-LP ships IIB T3 as the standard configuration for this reason. T3 temperature class (200 °C max surface) is appropriate for LPG’s 287 °C propane auto-ignition temperature; T4 (135 °C) is overkill and drives cost with no safety benefit. For US sites under NFPA 58, the equivalent is Class I Division 1 Group D (propane/butane); the CNEX certification is reciprocal.
How does the meter handle utility-grade sub-measurement versus full trade-grade?+
Utility-grade sub-measurement is the supported LPG accounting pattern: the LUXB-LP ships with a factory K-factor calibration certificate, ±0.5 % of rate reference-volume accuracy, and a Modbus-output totalizer that gives the operator a defensible monthly consumption record against the LPG supply contract. For full trade-grade billing where the meter is the legal point of sale, the standard industry pattern is a positive-displacement (PD) meter with national-regulator pattern approval; the LUXB-LP positions one grade below that; utility sub-measurement, audit standard for internal cost allocation.
Can the same meter measure peakshave LPG-air 60/40 blend?+
Yes; peakshave is one of the four pre-loaded blend profiles. Peakshave LPG-air systems inject vaporised LPG diluted with air into a natural-gas grid during peak winter demand; the 60/40 LPG/air ratio is chosen to match the 38 MJ/Nm³ heating value of the receiving natural-gas network so that downstream burners and appliances see a Wobbe-equivalent gas. The meter’s peakshave profile applies a density of 1.43 kg/Nm³ and a factory heating-value of 38 MJ/Nm³. The composition is locked on a per-plant basis at commissioning; peakshave plants run fixed ratios, so the blend is a set-and-forget configuration. The kWh/h output channel can then be used for the billing meter feed into the receiving gas utility, with the volumetric Nm³/h output as the audit trail. The design supports this pattern as utility-grade sub-measurement.

Need help sizing the LPG vapor build?

Send pipe size, blend (HD5 / 70-30 / 50-50 / peakshave), vapouriser pressure, thermal demand. Engineer replies in 4h with Nm³/h, heat-trace, model code, price.