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

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 Principle | Precession swirl with on-board blend-correct density + factory heat-value table computing |
|---|---|
| Line Sizes | DN25 – DN200 (1″ – 8″) |
| Media Supported | Propane (C3) · Butane (C4) · Mixed commercial · LPG-air peakshave 60/40 |
| Blend Profiles | US 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 Ratio | 1:30 standard · 1:15 economy |
| Pressure | 0.1 MPa – 1.6 MPa (post-regulator / post-vapouriser range) |
| Medium Temperature | -20 to +60 °C (heat-trace termination for J-T anti-condensation) |
| Wetted Parts | 316L Stainless standard · Duplex 2205 for sulfur-odourised LPG |
| Pressure-Vessel Construction | 316L stainless body standard · Hastelloy C upgrade · designed to NFPA 58 LP-Gas Code |
| Heat-Trace Termination | Integrated box on housing; 24 V DC or 230 V AC with thermostat, 30 W/m sizing |
| Heat-Value Output | kJ/Nm³ + kWh/h (factory heat-value table, blend-matched) |
| Output Signal | 4–20 mA (Nm³/h) + 4–20 mA (kWh/h) · Pulse · RS485 Modbus RTU · HART · GPRS |
| Hazardous Area | Ex d (CNEX flameproof) standard (covers IIA propane/butane + IIB ethylene traces) · Zone 1 |
| Approvals | CNEX 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
✓ 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 ratio | 1:30 standard · 1:15 economy |
| Velocity range | 2 – 50 m/s (gas); 1.5 m/s minimum at low pressure |
Process & Environment
| Medium | Propane · butane · mixed C3/C4 · LPG-air peakshave 60/40 · refinery fuel gas |
|---|---|
| Composition range | C3 10–100 % · C4 0–90 % · air 0–40 % (peakshave) · trace ethylene/H₂ (refinery) |
| Pressure range | 0.1 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 rating | IP66 standard · IP67 outdoor-unsheltered |
Blend & Heat-Value
| Blend profiles | US HD5 · EU 70/30 · EU 50/50 · Peakshave 60/40 · Custom |
|---|---|
| Density auto-correction | On-board density table per profile; HD5 1.88, EU 70/30 2.14, 50/50 2.20, peakshave 1.43 kg/Nm³ |
| Heat-value calculation | Factory heat-value table, gross calorific value, blend-matched |
| Heat-value output unit | kJ/Nm³ · MJ/Nm³ · kWh/h · MW (configurable) |
| Composition input | Fixed 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 termination | Integrated housing box; 24 V DC or 230 V AC, IP66, thermostatic control |
| Housing | Aluminium alloy, IP66 epoxy-coated · Ex d certified · 316 stainless option |
| Lead-seal points | Housing + 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 size | Minimum (Nm³/h) | Typical range (Nm³/h) | Maximum (Nm³/h) | Thermal @ HD5 |
|---|---|---|---|---|
| DN25 (1″) | 8 | 16 – 120 | 260 | up to 6.7 MW |
| DN40 (1½″) | 22 | 45 – 320 | 680 | up to 17.5 MW |
| DN50 (2″) | 32 | 65 – 490 | 1,040 | up to 26.8 MW |
| DN80 (3″) | 75 | 150 – 1,180 | 2,520 | up to 65 MW |
| DN100 (4″) | 120 | 240 – 1,900 | 4,080 | up to 105 MW |
| DN150 (6″) | 270 | 540 – 4,250 | 9,120 | up to 235 MW |
| DN200 (8″) | 480 | 960 – 7,560 | 16,200 | up to 418 MW |
Installation
LPG vapor fails on J-T condensate and paperwork. Five rules keep calibration valid and heat-value defensible.
- Vapor phase only; never liquid-phase LPG piping LUXB-LP is designed for post-vapouriser vapor.
- Heat-trace the last 2 × DN upstream Avoids J-T condensate rain. Meter’s integrated termination handles the body only, not upstream pipe.
- 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.
- Lock blend profile at commissioning Utility-grade sub-measurement requires blend lock per the supply contract.
- Plan periodic calibration re-verification Internal-verification cycles typically 2 years; align site verification with plant calibration program.
Frequently asked questions
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.