Osprey Corporation Ltd articles
Problem
In 2006 William Blythe requested that FTL/Osprey make an assessment of the suitability of switching and upgrading one of their early TurboScrubber units. The previous TurboScrubber unit absorbed H2S to 99.997% efficiency into NaOH to handle Chlorine & Chlorine Di- oxide emissions from process reactors.
Problem
Improving SO2 Removal from AV Cell’s plant in Canada.
Problem
Cooling process water at Huhtamaki`s Maine pulp & paper facility whilst ensuring continuous non-clogging operation.
Problem: How to meet the MACT emission standards at the Eli Lilly plant.
Osprey Corporation have installed their TurboScrubber systems in many Potash processing systems in the U.K. and Canada. These include Cleveland Potash for their exhaust dryer system as well as many Nutrien (formerly PCS) mine sites throughout the Saskatchewan province of Canada. Final stage processing of Potash involves the drying of the product, as such dust emission and vapour phase organics are produced.
Problem: Installing of our first full scale TurboScrubber® plant on a 3MW developmental Gasifier plant.
Problem
Installed in 1998, this Turboscrubber® unit treats the exhaust gases from various reactors, stills and packaging stations in William Blythe’s Tin Plant Recovery Section at Stannic.
FTL/Osprey have in collaboration with their Australian licensee received an order for the design and supply of five TurboScrubber systems for the mining industry. The project is part of $1.45 billion investment by Inco Limited at its Goro Nickel facility in the French Overseas Territory of New Caledonia.
Suncor Energy approached Osprey/FTL with an emission problem from their Stuart Oil Shale project in Queensland Australia, extracting crude oil from oil shale using a new technology.
Problem
Removal of Hydrogen Sulphide from gas streams with significant Carbon Dioxide partial pressures have been severely limited in the efficiency of absorption mass transfer rates, due to the interference between the two components. Kronos needed both an increase in throughput by de-bottlenecking the existing unit which was dynamically limited by its original design, and an improvement in H2S removal to meet tighter downstream waste gas emission limits.