GHD-Black & Veatch (GHD-BV) have completed design and specification of the ash thickening plant at Tarong Power Station, including operation of a pilot plant. Construction of the plant is in progress and commissioning is planned for early-2004._x000D_
The objective of the new plant is to convert the low concentration (lean phase) ash slurry currently generated by the power station into concentrated slurry which will then be pumped to the existing ash dam. Water recovered from the lean slurry will be returned to the power station for reuse. The drivers behind this project are to extend the life of the ash dam and to reduce water pumping costs. A maximum flow of 1000 litres per second is expected in the thickening plant._x000D_
The process involves a screening phase, which removes large material that could cause blockages or equipment damage. A 50 metre diameter thickener then concentrates the screened lean ash slurry to 55 - 60 per cent w/w solids. In addition, the thickener plant will allow the harvesting of floating cenospheres (hollow, spherical ash particles) from the lean slurry. Cenospheres are currently collected from the surface of the ash dam and drained on a pad adjacent to the dam._x000D_
The new system will use a surface skimmer to remove the cenospheres from the thickener and transfer them to settling ponds for further classification. The settling ponds simulate the detention on the existing ash dam, and allow entrained fine ash and slow settling cenospheres time to settle. As settling occurs in ponds, the slow settling cenospheres can be completely recovered whereas when they settle in the dam, the opportunity for recovery is lost. Cenospheres are a valuable by-product produced during the combustion process, and recycling of this material reduces the waste generated by the power station. Water recovered from the thickener drains to a three megalitre reservoir. Water is drawn from the reservoir for thickener plant service water and various other uses in the power station. The bulk of the water is used to sluice ash from the power station to the thickening plant._x000D_
In the current configuration, surface water from the ash dam is reused but must be pumped several kilometres back up to the power station. The dam also holds an inventory of several thousand megalitres of water and has significant evaporative losses. Therefore the current raw water make up demand is substantial. In addition, some areas of the power station traditionally using raw water will be modified as part of this project to allow the use of recovered water, further reducing the raw water demand. The design incorporates many features of sustainable water management. By more effectively recovering water from the lean ash slurry, the amount of raw water make up required by the system will be significantly reduced. This method of water recovery provides a more sustainable and energy efficient ash-transport mechanism.