Well fluids from the Tern wellheads are routed to two parallel separation trains, Train A and Train B. Train A comprises a 3-phase (oil, gas and produced water) Production Separator. Separated oil is routed to a 2-phase (oil and produced water) Train A Dehydrator where further produced water is removed. Oil from the Dehydrator is cooled and pumped via a metering skid to the export pipeline. Train B comprises a 3-phase Production Separator from which oil is cooled, pumped and mixed with Train A oil prior to metering. Well fluids from the Hudson field are routed to the 3-phase Hudson Production Separator. Separated oil can be routed through the 2-phase Hudson Dehydrator and thence to coolers and segregated metering prior to mixing with the Train A and B oil prior to export. Produced water from the Production Separators and Dehydrators is treated before disposal overboard. Gas from the Separators is co-mingled and compressed in three stages of compression. Fuel gas is taken from the discharge of the second stage of compression. Compressed gas is used for gas-lifting both the Tern and Hudson oil production wells. Gas is treated in a treatment packing prior to metering and export by pipeline.