Scaling
21 - 26 of 26 results
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Controlling fouling of membrane filtration installations (nanofiltration and reverse osmosis) is a major challenge for the water industry. Fouling affects the plant performance and increases the costs of plant operation. Diagnosis of the type(s) and extent of fouling is the essential first step for
Desalination 153 (2002)
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The water state in the CaSO4 solutions where concentrations ranged from 0.68–7.08 g/l was studied by the differential-scanning calorimetry. In the low-temperature range, 248.8 K, a peak was detected at the beginning of a CaSO4 concentration of 1.7 g/l. Its appearance could be attributed to an initia
Desalination 147 (2002)
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It is common practice in electrodialysis demineralization of calcium hydrocarbonate natural waters to restrict the current density by the limiting diffusion one. Exceeding this value causes the irreversible water dissociation at the interface of the anion-exchange membrane and solution and selective
Desalination 145 (2002)
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Predicting scale formation in desalination plants is a matter of a number of calculations. The accuracy of these calculations is dependent on accurate data, and representative operating conditions. These calculations are normally carried out by using software, supplied either by the membrane manufac
Desalination 139 (2001)
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In nanofiltration and reverse osmosis membrane systems 75–90% of the feed water is conversed to product, and as a consequence dissolved compounds are concentrated in the membrane concentrate. Subsequently, sparingly soluble inorganic compounds such as calcium carbonate and barium sulphate become sup
Desalination 138 (2001)
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CEDEX (Centro de Estudios y Experimentacion de Obras Publicas) and EMALSA (Empresa Mixta de Aguas de Las Palmas, S.A. ) had been performing experimental tests for seawater desalination at Las Palmas, Gran Canaria Is., Spain, using a TOYOBO hollow-fiber membrane. A Hollosep HM10255FI module made by T
Desalination 125 (1999)
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