An open loop scrubber sprays untreated seawater through the exhaust stream to absorb sulphur oxides, then discharges the wash water overboard after treatment, trading a simple process for a discharge that a growing number of ports now restrict or ban.
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An open loop scrubber draws seawater directly from the sea chest, sprays it through a tower against the rising exhaust gas, and discharges the wash water overboard after settling and monitoring, with no recirculation and no chemical dosing beyond what the seawater's own natural alkalinity provides. This sets it apart from a closed loop scrubber, which recirculates a caustic-dosed fresh water stream and only bleeds off a small treated portion, and from a hybrid scrubber, which can switch between the two modes. Open loop needs seawater with enough natural alkalinity…
An open loop scrubber draws seawater directly from the sea chest, sprays it through a tower against the rising exhaust gas, and discharges the wash water overboard after settling and monitoring, with no recirculation and no chemical dosing beyond what the seawater's own natural alkalinity provides. This sets it apart from a closed loop scrubber, which recirculates a caustic-dosed fresh water stream and only bleeds off a small treated portion, and from a hybrid scrubber, which can switch between the two modes. Open loop needs seawater with enough natural alkalinity to neutralise the sulphuric acid formed when SO2 dissolves, which is why it performs less consistently in low-alkalinity waters such as parts of the Baltic.
Vertical vessel where seawater is sprayed countercurrent to the exhaust gas across spray nozzles or a packed bed, stripping SO2 and much of the particulate matter.
High-capacity pumps drawing large volumes of seawater, since open loop operation depends on flow rate rather than chemical dosing to achieve the required wash ratio.
Settling tank or hydrocyclone removing particulates and free oil from the discharge stream before it goes overboard, feeding sludge to a residue tank.
Continuously measures wash water pH, PAH (polycyclic aromatic hydrocarbon) content, turbidity and flow, alongside SO2/CO2 ratio in the cleaned exhaust, to prove compliance.
Allows the engine to run on the scrubber or bypass it if fitted with dual-fuel capability to run on compliant low-sulphur fuel instead.
Sizing follows engine exhaust gas flow at full load, not ship size directly. The scrubber and its exhaust gas system must handle the combined main engine and auxiliary engine exhaust volumes it is designed to serve, at the required SO2 reduction to meet a 0.10% or 0.50% sulphur-equivalent limit depending on the operating area. Wash water flow rate, usually expressed in m3 per MWh of engine power scrubbed, is the other key sizing figure, since it drives pump capacity, piping diameter and the footprint of the treatment skid.
| Fault | Consequence |
|---|---|
| Spray nozzle scaling or blockage | Uneven gas-liquid contact, SO2 reduction falls below the required ratio |
| Wash water pump cavitation at low sea chest level or in heavy weather | Loss of wash flow, automatic changeover to low-sulphur fuel or engine power reduction |
| pH monitor fouling or drift | Discharge criteria breach going undetected, or false compliance failures forcing unnecessary bypass |
| Tower internals corrosion from continuous acidic wash | Structural thinning over time, requiring coating renewal or plate replacement at dry dock |
Check the port and coastal state discharge ban list before the voyage is planned, not after the ship arrives outside the limit; an open loop scrubber that cannot discharge has to switch to compliant fuel, and that fuel has to already be aboard.
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