"> Flue Gas IG System - Equipment Database
Also listed under Inert Gas Systems (23 models)

Flue Gas IG System

medium 2 models total

A flue gas inert gas system draws already-available boiler exhaust rather than burning extra fuel to make inert gas, at the cost of only working while the boiler is actually firing at a sufficient rate.

Read more — Flue Gas IG System explained

What makes a flue gas inert gas system different from a dedicated IG generator

A flue gas inert gas system draws its gas directly from the ship's boiler uptake rather than burning fuel specifically to produce inert gas. Boiler flue gas already has an oxygen content low enough, typically around 2 to 4 percent, to inert cargo tanks once it has been cleaned and cooled, so a flue gas system avoids the extra fuel consumption a dedicated combustion-type generator needs. The trade-off is dependency: flue gas systems only produce usable gas while the boiler is actually firing at a sufficient rate, which is straightforward on a steam tanker running cargo pumps off the boiler but can be a limitation on vessels where boiler load varies independently of inerting demand.

Flue gas inert gas system, process flow
Process flow of a flue gas inert gas system: boiler flue gas passes an isolating valve into a seawater scrubber and demister, is drawn on by the IG blower, then passes through the water-sealed deck seal to the cargo tank IG main.

Main components

Scrubber tower

Flue gas is drawn through a water spray scrubber that cools the gas and removes sulphur dioxide and particulates before it goes anywhere near the cargo tanks, since raw flue gas is both too hot and too dirty to inject directly.

Gas blower

One or more blowers, sized with standby capacity, raise the scrubbed gas to the pressure needed to push it through the deck main and maintain positive pressure in the cargo tanks against any inward leakage.

Deck water seal

A water-filled seal on deck, positioned between the blower and the cargo tanks, that lets gas flow forward to the tanks under normal operation but automatically blocks any flashback of cargo vapour toward the machinery space if pressure conditions reverse.

Non-return valve and deck isolating valve

A mechanical non-return valve backs up the water seal as a second line of defence against reverse flow, with an isolating valve allowing the whole system to be shut off from the cargo tanks for maintenance.

Oxygen analysers

Continuous oxygen monitoring at the scrubber outlet and, separately, in the cargo tank atmosphere itself, since the gas leaving the scrubber and the gas actually present in a tank some distance away are not always the same reading.

Selection and sizing

Capacity is set by the volume of the largest cargo tank or tank group that has to be inerted or gas-freed within the operational time allowed, plus the topping-up flow needed to hold tank pressure positive during discharge as cargo is pumped out and gas space expands. Because output depends on boiler firing rate, the system's practical capacity has to be checked against realistic boiler load during cargo operations, not against the boiler's maximum rated output.

Regulations and class

SOLAS Chapter II-2 requires inert gas systems on the tanker types and sizes specified in the regulation, with oxygen content in the cargo tank atmosphere kept at or below 8 percent by volume, and typically maintained closer to 5 percent or less in practice as a working margin. Class surveys check the deck water seal, non-return arrangements and oxygen analyser calibration on a running schedule, since these are the components that prevent flammable vapour from reaching an ignition source outside the tank.

Typical faults

  • Deck water seal running dry or with insufficient water level, removing the physical barrier against flashback
  • Scrubber water supply interrupted, allowing hot, corrosive, unscrubbed gas toward the blower and deck main
  • Oxygen analyser drift or fouling, giving a false low reading while actual tank oxygen content has risen
  • Blower capacity insufficient to keep pace with cargo discharge rate, letting tank pressure fall and drawing in outside air

What to look for in a supplier

  • Scrubber and blower capacity matched to the vessel's actual boiler output under realistic cargo operation conditions, not a nameplate best case
  • Deck water seal design proven for the vessel's expected list and trim range, since a seal that only works upright is a real limitation at sea
  • Oxygen analyser systems with independent calibration gas supply and a maintenance record that can be checked at survey
  • Documented flashback protection philosophy covering both the water seal and the mechanical non-return valve as separate, redundant barriers

Check the deck seal water level before every cargo operation, not on a calendar schedule; it is the one component standing between a routine inerting job and flammable vapour reaching the engine room side of the system.

2 manufacturers · 2 models

Alfa Laval

1
Alfa Laval (Smit) Smit Gas Inert Gas System
Smit Gas Inert Gas System
3000-15000 m³/h IG · Flue Gas → Inert Gas · Flue‑gas inert gas generation system
Medium
Flue Gas → Inert Gas
Type
Flue Gas IG System
Common Failures & Inspection Points
  • Fouling, scaling or blocked spray paths reduce treatment effectiveness and cause abnormal pressure drop or emissions readings
  • Pump, blower or fan faults cause low circulation or gas flow and system shutdown
  • Analyzer or sensor contamination causes incorrect gas-quality, emissions or oxygen readings
  • Seal, valve or piping leakage causes liquid or gas leakage and unstable process pressure
  • Control, dosing or interlock faults cause off-specification gas, alarm conditions or automatic shutdown
Service: Inspect treatment vessels or generators, pumps, fans or blowers, spray or filtration equipment, analyzers, drains and control interlocks. Trend gas quality, pressure drop and liquid-treatment condition where applicable. Verify shutdown and isolation functions according to the approved procedure. Refer to manufacturer, vessel and statutory documentation for the exact figure for gas quality, emissions, pressure and chemical limits.
Spare Parts: Carry pump and valve seals, analyzer consumables, filters, spray nozzles, dosing parts, fan or blower service items, sensors and control relays.
Strengths
  • Uses waste heat from the ship's boiler, reducing fuel consumption for IG production.
  • Integrated scrubber meets MARPOL Annex VI SOx limits while supplying IG.
  • Proven modular design with a long service record on oil and chemical tankers.
  • Can achieve O₂ content below 3 % to satisfy SOLAS requirements.
  • Supported by Alfa Laval’s global after‑sales network.
Weaknesses
  • Scrubber nozzle erosion is a common wear issue requiring periodic replacement.
  • Deck seal water level loss can interrupt IG flow and needs vigilant monitoring.
  • Blower bearing failures have been reported, increasing maintenance intervals.
  • O₂ analyzer calibration drift necessitates regular verification.
  • Higher initial capital cost compared with simple sea‑water IG plants.
Typical Vessels: Oil tankerChemical tankerProduct tanker
Certifications: SOLAS
Decision Guide: Choose if: the vessel is a SOLAS‑mandated oil or chemical tanker, you want to exploit boiler exhaust heat for IG, and you can accommodate regular scrubber maintenance. Avoid if: the ship lacks suitable flue gas temperature, budget constraints favor a simpler sea‑water IG system, or you prefer a low‑maintenance solution.
Use Cases: SOx control, tanker inerting, nitrogen generation and cargo-atmosphere management.

Wärtsilä

1
Marine IG System
5000-25000 m³/h IG · Flue Gas → Inert Gas · Flue Gas Inert Gas Generation System
Medium
Flue Gas → Inert Gas
Type
Flue Gas IG System
Common Failures & Inspection Points
  • Fouling, scaling or blocked spray paths reduce treatment effectiveness and cause abnormal pressure drop or emissions readings
  • Pump, blower or fan faults cause low circulation or gas flow and system shutdown
  • Analyzer or sensor contamination causes incorrect gas-quality, emissions or oxygen readings
  • Seal, valve or piping leakage causes liquid or gas leakage and unstable process pressure
  • Control, dosing or interlock faults cause off-specification gas, alarm conditions or automatic shutdown
Service: Inspect treatment vessels or generators, pumps, fans or blowers, spray or filtration equipment, analyzers, drains and control interlocks. Trend gas quality, pressure drop and liquid-treatment condition where applicable. Verify shutdown and isolation functions according to the approved procedure. Refer to manufacturer, vessel and statutory documentation for the exact figure for gas quality, emissions, pressure and chemical limits.
Spare Parts: Carry pump and valve seals, analyzer consumables, filters, spray nozzles, dosing parts, fan or blower service items, sensors and control relays.
Strengths
  • High IG production capacity suitable for large crude and product tankers
  • Integrated with exhaust gas cleaning (scrubber) allowing combined installation in ECA‑compliant ships
  • Modular design simplifies installation and future upgrades
  • Proven track record on many vessels worldwide, offering reliable compliance with IMO D‑2
  • Automatic monitoring and alarm functions for blower performance and water seal level
Weaknesses
  • Complex system requiring regular maintenance of scrubber packing and IG blower components
  • Higher initial capital cost compared with simple air‑based IG generators
  • Space intensive; needs dedicated machinery space adjacent to the exhaust line
  • Sensitivity to seawater ingress can trigger water‑seal alarms and affect gas quality
  • Potential for blower motor failure if not inspected according to schedule
Typical Vessels: Crude Oil TankerProduct TankerChemical Tanker
Certifications: IMO D-2USCG Type ApprovalDNV Classification Society Approval
Decision Guide: Choose if the vessel requires a high‑capacity inert gas supply, operates in emission control areas where a scrubber is already installed, and must meet IMO D‑2 compliance. Avoid if space is limited, cargo turnover is low (making a simpler air‑based IG system more economical), or the operator prefers lower upfront cost over integrated performance.
Use Cases: SOx control, tanker inerting, nitrogen generation and cargo-atmosphere management.