Viscosity is a key property for any heavy fuel oil, affecting pumping, atomization, and combustion quality. Very Low Sulphur Fuel Oil viscosity is typically lower than that of high-sulfur fuel oil (HSFO), but varies significantly by grade (e.g., IFO 180 vs. IFO 380). The Very Low Sulphur Fuel Oil Market has seen the adoption of VLSFO across the global fleet, making understanding its rheological properties essential for ship engineers and bunker managers. This guide provides a comprehensive overview of VLSFO viscosity, measurement, handling, and impact on fuel systems.
What is Viscosity?
Viscosity is a fluid’s resistance to flow (internal friction). For marine fuels, it is typically measured in centistokes (cSt) at a reference temperature of 50°C (122°F). Lower cSt means thinner, more fluid oil. Higher cSt means thicker, more viscous oil that requires heating for pumping and atomization.
Typical Viscosity Ranges for Marine Fuels
| Fuel Type | Typical Viscosity (cSt @ 50°C) | Key Characteristics |
|---|---|---|
| Marine Gas Oil (MGO) | 2-5 cSt | Low viscosity, no heating needed, good atomization |
| VLSFO (IFO 180 grade) | 150-200 cSt | Requires moderate heating (40-60°C) |
| VLSFO (IFO 380 grade) | 300-400 cSt | Requires significant heating (60-80°C) |
| HSFO (IFO 380, 3.5% S) | 350-450 cSt | Similar to VLSFO IFO 380, often higher |
Note: The “IFO” stands for Intermediate Fuel Oil. The number (180, 380) refers to the kinematic viscosity in cSt at 50°C.
Why Viscosity Matters for Engine Operation
1. Pumping and Fuel Transfer
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High viscosity fuels require heating (using steam or electric heaters) in storage tanks, settling tanks, and day tanks to reduce viscosity to pumpable levels (typically <200-300 cSt for centrifugal pumps).
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Rule of thumb: For every 10°C increase in temperature, viscosity is roughly halved (for mineral oils). VLSFO (IFO 380) at 50°C (400 cSt) may need heating to 80-90°C to reach <30 cSt for injection.
2. Atomization (Fuel Injection)
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The fuel injector’s nozzle requires a specific viscosity range (typically 10-20 cSt) for proper atomization. If viscosity is too high, the fuel droplets are large, leading to:
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Incomplete combustion (smoke, soot).
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Carbon deposits on injector tips.
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Higher exhaust gas temperatures.
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Reduced engine efficiency.
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If viscosity is too low (overheating), the fuel can “flash” (vaporize prematurely) causing knocking and fuel pump seizure.
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Viscosity control: Modern marine engines have a viscosity controller (viscometer) that automatically adjusts the fuel heater temperature to maintain constant viscosity at the engine inlet (e.g., 14 cSt).
3. Fuel Pump Lubrication
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The fuel injection pump relies on the fuel itself for lubrication. If viscosity is too low (overheated or too much cutter stock), it can cause fuel pump seizure.
4. Centrifuging (Purification)
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Fuel oil separators (centrifuges) operate most efficiently within a specific viscosity range (typically 30-80 cSt at separation temperature). Viscosity affects the separation efficiency of water and cat fines (catalytic fines from refineries).
VLSFO vs. HSFO Viscosity: Key Differences
| Parameter | HSFO (3.5% S) | VLSFO (0.5% S) |
|---|---|---|
| Base oil composition | High in residual components (asphaltenes). | Lower in asphaltenes (due to desulfurization or blending). |
| Viscosity (IFO 380 grade) | 350-450 cSt @ 50°C | 300-400 cSt @ 50°C (slightly lower). |
| Cold flow properties (pour point) | Variable (can be high). | Can be higher (some VLSFO have high paraffin content, leading to gelling). |
| Viscosity response to heating | Linear reduction. | Nonlinear; some blends may have “abnormal” viscosity curves. |
| Compatibility when blended | Generally good if within same refinery. | Poor compatibility between different VLSFO blends can cause sludge (see article 3 on Very Low Sulphur Fuel Oil storage stability). |
| Cat fines (aluminum & silicon particles) | Moderate levels. | Sometimes higher (because VLSFO may contain cutter stock from cracking processes). |
Challenges Specific to VLSFO Viscosity
1. Higher Cold Flow Issues (Pour Point)
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Some VLSFO blends (especially those with a high paraffinic content from waxy crudes) have a high pour point (the temperature below which the oil stops flowing).
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Risk: Gelling in bunker tanks during cold weather, leading to clogged filters and inability to pump.
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Mitigation: Use bunker heating at lower temperatures than for HSFO. Add pour point depressants (PPD) to the fuel.
2. Unusual Viscosity-Temperature Curves
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Traditional viscosity-temperature charts (designed for conventional residual fuel oils) may not be accurate for some VLSFO blends, especially those containing visbroken or hydrocracked components.
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Impact: The automated viscosity controller (viscometer) may struggle to maintain stable fuel viscosity at the engine inlet, leading to combustion issues.
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Mitigation: Use an in-line viscometer at the engine inlet, not just a temperature control.
3. Compatibility with Bunkered Fuel
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When a vessel takes on VLSFO from a new supplier, it may be incompatible with the previous bunker fuel, forming sludge and increasing viscosity (by orders of magnitude).
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Mitigation: Conduct a compatibility test before loading new fuel (ASTM D7156 or ISO 10307-2). Use a “compatibility additive” if needed.
4. Cat Fines (Catalytic Fines)
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Cat fines (aluminum and silicon oxide particles from the refining process) can be present in VLSFO, especially if the fuel contains light cycle oil (LCO) or clarified oil (CCO).
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Impact: Cat fines are abrasive. In high viscosity fuel, they are suspended. If viscosity is improperly controlled and fuel is overheated, cat fines can precipitate and cause severe engine wear (cylinder liners, piston rings, fuel pumps).
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Mitigation: Efficient centrifuging (purification). Monitor cat fines level (ASTM D5184). Ensure proper settling time in tanks.
Handling Recommendations for VLSFO by Viscosity Grade
IFO 180 VLSFO (lower viscosity, e.g., 150-200 cSt @ 50°C)
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Heating (storage tanks): 40-50°C (to achieve pumpable viscosity).
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Heating (day tank / settling tank): 50-60°C.
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Engine inlet viscosity set point: 10-12 cSt.
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Recommendations: Good for smaller engines and vessels with less heating capacity.
IFO 380 VLSFO (higher viscosity, e.g., 300-400 cSt @ 50°C)
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Heating (storage tanks): 60-70°C.
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Heating (day tank / settling tank): 70-85°C.
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Engine inlet viscosity set point: 12-15 cSt.
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Recommendations: Most common for large two-stroke engines. Requires robust heating system.
Testing and Monitoring Viscosity
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Bunker delivery sample: Have a sample tested by an independent laboratory for viscosity, density, and sulfur content. Ensure it matches the Bunker Delivery Note (BDN).
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Onboard viscometer: Use a vibrating element or capillary type viscometer to continuously monitor viscosity at the engine inlet.
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Fuel temperature sensors: Cross-check with temperature measurements.
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Alarms: Set high and low viscosity alarms to protect the engine.
Regulatory Context and IMO 2020
Very Low Sulphur Fuel Oil IMO 2020 compliance does not specify viscosity limits. However, ISO 8217:2017 (specifications for marine fuels) includes viscosity limits for each grade. For VLSFO (0.5% S), the ISO standard allows a maximum viscosity of 380 cSt at 50°C (for RMG 380) or 180 cSt (for RMG 180). Ship owners must ensure the fuel delivered meets these specifications.
Future Trends in VLSFO Viscosity
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Blending optimization: Refiners are learning to produce VLSFO with better cold flow properties and more consistent viscosity-temperature behavior.
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Biodiesel blending: Some VLSFO may contain a small percentage of bio-components (FAME, HVO), which can affect viscosity and storage stability.
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Viscosity reduction additives: Pour point depressants and viscosity modifiers are becoming more common.
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Alternative fuels: In the longer term, vessels will transition to LNG, methanol, or ammonia, which have very different handling properties (cryogenic for LNG, low viscosity for methanol/ammonia).
Conclusion
Very Low Sulphur Fuel Oil viscosity is a critical operational parameter. The shift from HSFO to VLSFO has introduced new challenges (cold flow, compatibility, cat fines), but proper heating, purification, and monitoring can manage these risks. Ship engineers must understand the specific viscosity grade of their bunker fuel (IFO 180 vs. IFO 380) and adjust heating and separation temperatures accordingly. A well-maintained viscosity control system ensures efficient combustion, protects the fuel injection system, and reduces overall operating costs. Understanding the Very Low Sulphur Fuel Oil price vs high sulfur spread and the properties of the fuel are both essential for effective marine fuel management.
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