As originally conceived the works comprised reservoirs covering 2.6 hectares designed to retain six hours’ flow of sewage. No sewage treatment was provided and the sewage was discharged untreated into the
River Thames on the
ebb tide. Following the
Princess Alice disaster in 1878 a Royal Commission was appointed in 1882 to examine Metropolitan Sewage Disposal. It recommended that a
precipitation process should be deployed to separate solids from the liquid and that the solids should be burned, applied to land or dumped at sea. A precipitation works using
lime and
iron sulphate was installed at Crossness in 1888–91. Sludge was disposed of in the Barrow Deep and later in the
Black Deep in the outer
Thames estuary. In the year 1912/13 the Crossness works received and treated 49,534 million gallons (225.2 million m3) of sewage, and disposed of 880,000 tons of sludge. The cost of operating the Crossness works was £44,269. In 1919/20 the corresponding figures were 41,209 million gallons (187.3 million m3), of sewage, 767,000 tons of sludge sent to sea, entailing 767 sludge vessel voyages, and the costs were £52,282.
Advanced treatment Work began in the early 1960s to install a modern treatment plant capable of treating 450,000 cubic metres per day of sewage. The cost of the works was £9 million at 1963 prices. The plant comprised storm tanks, detritus channels, primary sedimentation, mechanical aeration, final sedimentation and sludge digestion. Following the 1964 upgrade the works at Crossness began to produce a
nitrifying effluent whereupon
sulphide disappeared from the tideway; an excess of
nitrate provided a safeguard against sulphide formation in the river. The plant provides 6 MW of power for use at the treatment works.
New processes In 2010–14 the Crossness works were upgraded at a cost of £220 million, increasing capacity by 44% to reduce storm sewage flowing into the Thames during heavy rainfall. The upgrade involved the installation of new renewable energy sources including a 2.3 MW wind turbine, a
thermal hydrolysis plant, an advanced digestion plant, and an odour control treatment system. The project enabled the plant to treat 13 cubic metres of sewage per second and incorporated new inlet works, primary settlement tanks, secondary biological treatment implementing the
activated sludge process and final settlement tanks. It also included the installation of associated sludge thickening and odour treatment facilities. The hydrolysis plant burns combustible sludge flakes created after waste water treatment to 160 °C, producing 50 per cent more
biogas than anaerobic digestion process. The project included the installation of eight new primary settlement tanks where sewage is collected to remove primary sludge passing through two 1.2 km-long culverts of 2 m diameter. Sewage passes through a pair of new aeration lanes into twelve final settlement tanks of 40 m diameter. The activated sludge plant includes six aeration lanes of 69 m with total volume of 86,000 cubic metres and a treatment capacity of 564,000 cubic metres per day. It includes
anoxic zone mixers, a fine bubble diffused aeration system and five centrifugal blowers giving an air flow of up to 21,000 cubic metres per hour. Additional sludge storage and thickening facilities store the additional sludge. The five raw sludge gravity belt thickeners have a capacity of 6,055 cubic metres per day each. == Crossness Pumping Station ==