{"id":9045,"date":"2020-06-30T14:35:52","date_gmt":"2020-06-30T06:35:52","guid":{"rendered":"http:\/\/dmi65.com\/?page_id=9045"},"modified":"2020-06-30T15:53:39","modified_gmt":"2020-06-30T07:53:39","slug":"water-treatment-power-generation","status":"publish","type":"page","link":"https:\/\/dmi65.com\/pt-br\/industries\/water-treatment-power-generation\/","title":{"rendered":"Water Treatment for Power Generation"},"content":{"rendered":"

[vc_row][vc_column][vc_column_text css=”.vc_custom_1593503585420{margin-top: 15px !important;margin-bottom: 15px !important;}”]Water Treatment for Power Generation:<\/strong> In January of 2016 Quantum Filtration Medium conducted a series of site visits to assess the options for upgrading the water treatment plant supplying water to the Kuala Langat Power Plant (KLPP)<\/a>. The goal was to highlight low cost options with a low impact on plant serviceability to increase the plant performance, efficiency and reliability, and ability to better cope with the seasonal load changes experienced in the raw water supply.<\/p>\n

The operation of KLPP has begun since 1996 using combined cycle gas turbine and the plant is currently contributing 675MW of electricity generation capacity to the grid. The ability of the plant to supply electricity to the grid according to its obligation under the Power Purchase Agreement depends on a number of factors including reliable clean water supply for the purpose of cooling. On average, KLPP draws 20,000 cubic meters of treated water for its daily operation. For optimal operation and life of the plant, the water needs to be as clean as possible with low content of organic or inorganic substance that would impact the plant operation.<\/p>\n

There are four mains areas of the plant where the potential for considerable improvements were identified.
\n\u2022 The possibility of adding bore water to the raw water supply
\n\u2022 Clarification of the raw water before entering the plant
\n\u2022 Optimisation of the flocculent\/polymer dosing program (inc. type and dosing rate)
\n\u2022 Changing of the media in the rapid sand filters to DMI65\u00ae[\/vc_column_text][\/vc_column][\/vc_row][vc_row][vc_column][vc_column_text css=”.vc_custom_1593503610377{margin-bottom: 0px !important;}”]BORE WATER ADDITION<\/strong><\/p>\n

It was suggested that the area surrounding the plant be assessed for suitability and potential quality and quantity of several bores to add to the plant raw water supply. The addition of bores would not only provide greater flexibility in terms of seasonal blending with river water to ensure sufficient quantities of water in the dry season, could also be used to lower suspended solids and turbidity loadings on the plant during the wet season.<\/p>\n

There is a likelihood that there will be traces of iron and manganese in the bore water, but the use of DMI65 filtration media will remove this and provide an improvement to the usual mechanical filtration duties.<\/p>\n

CLARIFICATION<\/strong><\/p>\n

The high turbidity and suspended solids levels in the raw water could be greatly reduced by clarification prior to entering the water treatment plant. The existing plant is fixed in size and capacity, however a pre-clarification stage will dramatically reduce the load on the current plant.<\/p>\n

A traditional clarifier and upstream floc\/polymer dosing system to handle 1ML\/hr would cost well over USD $1M and take up a considerable land area to install and was therefore not practical in this case. With a very low retention time this type of system would also require very high chemical usage.<\/p>\n

POLYMER OPTIMISATION<\/strong><\/p>\n

A range of polymer samples were supplied during the site visit. Jar testing has been carried out using the range of samples and highlighted a particular polymer most suited to this raw water. A local polymer supply company is able to supply a very similar product in powdered form and at a very reasonable price that would suit the mixing\/batching system mentioned above.<\/p>\n

MEDIA CHANGE-OUT IN RAPID SAND FILTERS<\/strong><\/p>\n

During our visit one of the rapid sand filters was drained for inspection. The sand in the filters has never been changed and is now very hard-packed and is in need of replacement. The filter was filled whilst we were watching and the infiltration rate of the incoming water was very poor with most of the water just flowing across over the top of the sand and down through cracks in the hard packed sand rather than down through it. We proposed to replace the media with DMI65\u00ae filtration media<\/a>.<\/p>\n

The DMI65 will remove the existing and cope with any rise in iron or manganese levels that can be encountered in raw water sources with varying quality. The DMI65 requires a low level of free chlorine (0.2-0.3mg\/L) to activate the media. This is easily achieved as it only requires moving of the existing chlorine dosing point to just prior to the media filters. The chlorine residual will remain and still act as disinfection for the treated water lagoon.<\/p>\n

The DMI65\u00ae also provides the perfect filtration coefficient resulting in excellent mechanical filtration lowering suspended solids and turbidity levels.<\/p>\n

The addition of the DMI media and replacement of the filtration nozzles improved not only the quality of water from the media filters, but also the quantity of water through the filters.<\/p>\n

Sample Results<\/p>\n

\"\"<\/p>\n

With a peak NTU of 1000 and an average inlet TSS of 286 you can see that the outlet of lagoon B has been maintained generally around 80 NTU with an average of 86 NTU.<\/p>\n

OVERALL PLANT OUTPUT<\/strong><\/p>\n

The results from the plant post media filters after the replacement of the old sand media with the new DMI65 media have been consistently excellent.<\/p>\n

The expected results from the media filters after the upgrade were:<\/p>\n