HFO & Heavy-Oil Mass Flow Meter

Coriolis for Heavy Fuel Oil, IFO 380, Asphalt, and Heated Crude up to 350 °C

±0.2% custody / 0.5% / 1.0% rate on heavy oil
DN25 to DN150 standard (DN200 by quote)
Insulation jacket up to 350 °C

  • Direct mass flow through 30–380 cSt viscosity range (LWGY out-of-range here)
  • Steam-jacket sandwich shell keeps measuring tube above pour point
  • Ex d [ia] IIC T6 Gb + IP67 + ISO 9001 calibration certificate
↓ Request datasheet (PDF)
HFO & Heavy-Oil Mass Flow Meter; V-tube Coriolis with integrated transmitter and flanged process connection for heavy fuel oil and asphalt custody service

Coriolis for heavy fuel oil bunker, IFO 380, asphalt, and refinery hot residue. Thermal-insulation jacket carries steam at ≤200 °C through the sandwich shell to keep the measuring tube above pour point. Direct mass measurement through the 30–380 cSt viscosity range; LWGY liquid turbine is out-of-range here per the platform binding. Standard build is 316L wetted parts (centistokes-tolerant) in a jacketed Ex d housing. Lead time 5–7 business days.

Benefits

  • 30–380 cSt viscosity range: covers IFO 380, IFO 180, asphalt, and waxed crude at warm operating temperature.
  • Insulation-jacket sandwich shell: steam or hot oil at ≤200 °C / 0.8 MPa keeps the measuring tube above pour point.
  • Direct mass flow output: no density correction needed for variable HFO density across IFO 380 / 180 grade swaps.
  • ±0.2 % custody option: marine bunker terminal billing on dual-pulse audit-trail output.
  • Ex d [ia] IIC T6 Gb: flameproof + intrinsically safe combined for dock-side bunker and refinery hazardous zones.
  • 316L wetted standard, titanium upgrade: standard for IFO 380; titanium for high-sulfur HFO and chloride carry-over.
  • Lead time 5–7 business days from the factory, ISO 9001 calibration with K-factor and density coefficient.

Configure your build.

Select your specs and the configurator returns the model code plus a ballpark unit price. Submit for engineering review and verified sizing within 4 business hours.

Your Configuration

CMFM-HFO-50-J-A2-316L-P25-A300-STD-EX
Pipe sizeDN50
BuildInsulation-jacket (≤350 °C)
Accuracy±0.2 % (custody)
Material316L
Pressure2.5 MPa
Hazardous areaEx d [ia] IIC T6 Gb
Estimated unit price
Verified after engineer review
$8,640
Request Quote on This Build Email Engineering
✓ Jacket steam supply spec verified at quote
✓ HFO grade + viscosity reviewed by application engineer
✓ Reply within 4 business hours

Typical applications

Four heavy-oil applications where the jacketed Coriolis is the standard pick.

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Marine bunker terminal IFO 380 billing

Dock-side bunker line at 110–150 °C. ±0.2% custody, ANSI 300 LB, audit-trail output for delivered-tons invoice.

Power-plant HFO daily-tank delivery

Coal-and-oil-fired plant HFO tank to boiler-fuel pump. DN50–DN100, 4-20 mA + HART to plant DCS.

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Asphalt plant tank-truck loading

Asphalt at 180–200 °C through DN80–DN150. Jacket steam at 200 °C; ±0.5% rate for batch totals.

Refinery hot-residue transfer

Vacuum-residue to coker / asphalt unit up to 350 °C. Jacket at 200 °C; ±0.5% for unit mass balance.

Specifications

Measurement principleCoriolis force on vibrating tube; direct mass flow + density + temperature, viscosity-independent
Applicable mediumHeavy fuel oil 30–380 cSt at warm operating temperature, IFO 380 / IFO 180 marine bunker grades, asphalt 60–250 cSt at 180–200 °C, waxed crude with pour-point heating, refinery hot residue up to 350 °C. Out of scope: cold HFO below pour point (must be pre-heated), rapid-slug two-phase flow.
Pipe size rangeDN25 to DN150 standard (1″ to 6″); DN200 by quote
Accuracy±0.2 % of rate (custody build) / ±0.5 % of rate / ±1.0 % of rate (factory calibration with K-factor and density coefficient)
Density measurement0.3 to 3.000 g/cm³ through the same Coriolis pickup, accuracy ±0.002 g/cm³
Turndown10:1 to 20:1 nominal across the basic accuracy range
Working pressure1.6 / 2.5 / 4.0 / 6.3 MPa metric, ANSI 150 LB / 300 LB / 600 LB, DIN PN16 / PN25 / PN40 / PN63
Medium temperatureup to 350 °C (insulation-jacket build), up to 200 °C (standard non-jacketed build)
Jacket serviceSteam or hot oil at ≤200 °C and ≤0.8 MPa supply, jacket ports 1/2″ NPT (DN25–DN50) or 3/4″ NPT (DN80–DN200), sandwich shell isolated from process medium
Wetted material316L stainless (standard for IFO 380 / IFO 180 / asphalt / hot residue), titanium (upgrade for high-sulfur HFO and chloride carry-over)
Housing material304 stainless sensor housing, aluminium ZL401 transmitter housing
Output signals4-20 mA + Pulse + RS-485 Modbus RTU (standard), 4-20 mA + Pulse + RS-485 + HART (option)
Power supply18–36 V DC (basic), 85–265 V AC self-adaptive; 7 W typical, 10 W AC version
Display3-line LCD with touch keys; instantaneous mass, totalizer, density, temperature
Hazardous areaEx d [ia] IIC T6 Gb (flameproof + intrinsically safe combined) standard for dock-side bunker terminal and refinery hot-residue zones
Ingress protectionIP67
Ambient temperature−20 to +60 °C transmitter
ApprovalsEMC 2014/30/EU (Annex II), ISO 9001 calibration certificate with K-factor and density coefficient. Marine bunker custody (OIML R 117) and fiscal billing (API MPMS) are buyer-arranged with the local notified body.

Installation

Five install rules for the jacketed Coriolis on heavy fuel oil, asphalt, and hot residue service.

  1. Connect steam supply to jacket inlet before service Plumb the jacket inlet port to the plant utility steam header and the jacket outlet to the condensate return before opening process flow. Standard ports are 1/2″ NPT (DN25–DN50) or 3/4″ NPT (DN80–DN200) female.
  2. Run jacket steam to keep tube above pour point Maintain jacket at 130–150 °C for HFO bunker, 200 °C for asphalt and refinery hot residue. Without jacket service the measuring tube can solidify between flow events and resist start-up.
  3. No upstream straight-pipe required The Coriolis principle is independent of velocity profile, so no upstream straight-pipe minimum is required. This is the principal install advantage over turbine and vortex measurement for tight refinery and dock-side bunker layouts.
  4. Pipe support both sides of the sensor Add pipe brackets at fixed steel or concrete close to the sensor flanges. The vibrating tube is sensitive to external pipe vibration from bunker pumps and asphalt circulation pumps; isolate with flexible hose on high-vibration runs.
  5. Earth-ground the sensor housing on a dedicated line Cross-section ≥1 mm². Do not bond welding-system ground to the meter ground during pipe work; transient currents damage the Coriolis pickup. Run a zero-correction cycle after first commissioning with valves closed both sides and the sensor at process temperature.

Frequently asked questions

What is an HFO Coriolis mass flow meter and why does the LWGY turbine not cover heavy fuel oil?+
An HFO Coriolis meter measures the mass flow rate of heavy fuel oil directly; Coriolis force on a vibrating tube, viscosity-independent across the 30 to 380 cSt range that HFO and IFO 380 actually run at warm operating temperature. The LWGY liquid turbine is bound to clean low-viscosity liquid ≤10 cSt at service temperature; HFO at 110 to 150 °C still sits 30 to 380 cSt, far above the turbine accuracy range, with bearing loading and K-factor viscosity-shift making turbine measurement unreliable. This is the explicit fill-in for that LWGY out-of-binding routing; same fuel family, different measurement principle.
How does this build cover IFO 380 vs IFO 180 marine bunker grades?+
Both IFO 380 (maximum 380 cSt at 50 °C) and IFO 180 (maximum 180 cSt at 50 °C) are within the Coriolis viscosity range across the full delivery temperature window. Marine bunker terminals typically heat the bunker line to 110 to 130 °C, where IFO 380 sits around 40 to 60 cSt and IFO 180 sits around 20 to 30 cSt; both well-handled by the jacketed Coriolis. The thermal-insulation jacket carries steam at ≤200 °C through the sandwich shell to keep the measuring tube above pour point during low-flow or shutdown intervals. Direct mass flow output makes IFO 380 vs IFO 180 density differences (typically 0.99 vs 0.98 g/cm³) irrelevant to billing accuracy; no density correction needed for grade swaps.
What is the steam-jacket supply spec for the insulation jacket?+
The jacket supply is steam or hot oil at up to 200 °C and up to 0.8 MPa supply pressure. Connect the jacket inlet on the sensor body to the plant utility steam header before service, and route the jacket outlet to the condensate return. The jacket is a sandwich shell around the measuring tubes; jacket fluid does NOT contact the process medium. Standard jacket-port connections are 1/2″ NPT female on DN25 to DN50 sensors and 3/4″ NPT female on DN80 to DN200. For asphalt service at 180 to 200 °C medium temperature, run the jacket at 200 °C steam. For HFO bunker at 110 to 150 °C, the jacket can run at 130 to 150 °C hot-water trace or 0.4 MPa saturated steam.
What is the procedure for cold-start from a frozen HFO line?+
Never start flow through a Coriolis sensor that is frozen with solidified HFO inside; the vibration tube can be permanently damaged. Cold-start procedure for the insulation-jacket build: (1) verify the line is isolated upstream and downstream; (2) open the jacket steam supply and let the jacket warm the sensor for at least 30 minutes at 150 °C jacket temperature; (3) verify the measuring tube has reached above pour point through the transmitter density reading; if density reads above 1.05 g/cm³ the tube is still cold; (4) crack open the upstream isolation valve slowly to admit warm HFO from a pre-heated tank; (5) when steady flow is established, run a zero-correction cycle at process temperature with valves closed both sides.
How accurate is the meter for marine bunker custody billing?+
The custody build runs ±0.2 % of rate across the turndown range. Density measurement runs ±0.002 g/cm³ through the same Coriolis pickup. For marine bunker terminal billing where the buyer and seller invoice on delivered mass (tons of IFO 380), the ±0.2 % rate accuracy on direct mass output is the published spec. OIML R 117 / API MPMS marine bunker custody certification is buyer-arranged with the local notified body; we ship the meter with ISO 9001 calibration certificate, K-factor, and density coefficient documentation; the buyer arranges the marine custody verification with the port-state authority. We can configure the dual-pulse output and audit-trail logger for that verification process at quote.
What is the lead time and what certifications ship standard?+
Lead time is 5 to 7 business days from order confirmation, factory direct. Each meter ships with an ISO 9001 calibration certificate listing the K-factor, density coefficient, calibrated DN, and tested flow range. Hazardous-area certification is Ex d [ia] IIC T6 Gb (flameproof plus intrinsically safe combined) standard for dock-side bunker terminals and refinery zones. EMC compliance to the EU Electromagnetic Compatibility Directive 2014/30/EU (Annex II) ships standard. IP67 ingress protection ships standard across the range. Marine bunker custody (OIML R 117) and fiscal billing (API MPMS) certifications are buyer-arranged with the local notified body; the factory ships the meter ready for that verification with audit-trail-capable dual-pulse output.

Need help sizing a jacketed HFO build?

Send line size, HFO grade, delivery T, jacket utility, Ex zone. Reply in 1 day; lead time 5–7 business days.