Pilot filtration study to reduce fouling on Marbella seawater RO plant

Autor: Mariana Vodnar, Craig Roger Bartels, Stefan Rybar, Miguel Esteban Martin, Mike Jefferies
Rok vydání: 2008
Předmět:
Zdroj: Desalination. 220:228-238
ISSN: 0011-9164
DOI: 10.1016/j.desal.2007.01.031
Popis: The seawater RO plant at Marbella had operated intermittently, and at low flowrates, since its construction 10 years ago. This was because the plant had been designed to operate at times of water shortage, to provide water when the conventional supplies were not available. During the early part of the 21st century, the mode of the plant changed, and it was expected to operate at design capacity for most of the time. This brought two facts to light — that during high abstraction rates the intake water quality deteriorated significantly, and that the filtration system that had been installed was not capable of adequately filtering the feed water to make it suitable for feeding to a reverse osmosis plant. The plant was originally built using DuPont B10 permeators. Due to the unavailabilty of these permeators, the plant is currently being converted, stream by stream, to spiral wound membranes supplied by Hydranautics. At design flowrates, the DuPont system fouled rapidly, and required cleaning every two weeks. The spiral trains fouled more slowly, but still required cleaning at a higher frequency than would be considered normal for this type of plant. A pilot filtration plant was installed on site to attempt to find the following; • An optimum coagulant for the water. • An approximate dose rate for that coagulant. • The effect of different media on the quality of filtered water. • The length of run between backwashes using different media. • The quality of water that can be achieved using this coagulant and media. By installing pressure tapping points along the length of the filter, the area of differential pressure could be measured. This was used to ensure depth filtration was taking place, and the foulants were being removed through the length of the bed rather than surface filtration. The trials lasted a total of three months and achieved all of the targets set. The SDI typically achieved by the main plant was approximately 5. The pilot filter showed that the SDI could be reduced to below 2 by modifying the filters and applying a coagulant. Filter runs achieved by the pilot filters were in excess of 48 h. Following the trials, the plant commenced replacing the media in the filtration system, and is expected to install a coagulant dosing system once this was complete. This paper describes the pilot plant built, the selection of the media, and the coagulants used, and presents the operating data produced from the trials.
Databáze: OpenAIRE
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