Research Abstracts
2111 - 2120 of 3156 results
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A method to determine the critical concentration Rayleigh number in isothermal membrane transport processes was worked out. This method is based on equations which include the diffusive permeability coefficient, Tks; solution parameters (density, D; kinematic viscosity, <; diffusion coefficient, Dks
Desalination 168 (2004)
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The aim of this work is to improve a mathematical model to describe the volume-decreasing diafiltration process by including macrosolute rejection. Water consumption in this continuous process was analyzed and a significant advantage when comparing both the classical diafiltration process and multi-
Desalination 165 (2004)
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Within the lifetime of most membranes some fouling will adversely affect membrane performance and cleaning will be necessary. The cleaning will depend on the type of deposit such as organic fouling, inorganic scaling or colloidal deposition. However strong the circumstantial evidence as to the ident
Desalination 167 (2004)
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Two hollow-fibre ultrafiltration membrane modules of the waste-water treatment facilities of a cosmetics company were analysed to investigate the causes of membrane damage and rapid fouling of the membranes. This autopsy consisted of visual inspection of the membranes and the module, a bubble-point
Desalination 165 (2004)
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Described herein is a case study of long-term reverse osmosis plant operation based on TFC membrane technology developed by CSMCRI, Bhavnagar, India. The plant supplies safe drinking water containing 175 ppm to the population of the Kasari village. The plant provides 2000 L/h desalinated water conta
Desalination 165 (2004)
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Southern Tunisian’s natural brines represent an important source of mineral salts with a high economic value. These salts are recoverable by simple solar evaporation. Indeed, during isothermal solar evaporation it is possible to recover mineral salts and to determine the precipitation sequences of t
Desalination 166 (2004)
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A hybrid process, consisting of ozonation and membrane filtration, followed by activated carbon filtration, was studied in pilot scale for drinking water production from river water. The main focus of this study centred on tests to determine the effect of ozone on the filtration and fouling behaviou
Desalination 168 (2004)
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One of the largest seawater reverse osmosis (SWRO) desalination plants in the world commissioned at Addur, Kingdom of Bahrain survived the numerous obstacles that brought down the plant’s production capacity to its lowest level. The drastic production loss, ever increasing heavy chemical cleaning pr
Desalination 165 (2004)
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2 The crystallization of K2SO4 in the system K+, Mg2+/Cl!, SO4 / H2O involving the reaction 2KCl + MgSO4 K2SO4 + 2KCl was studied. Independently of the experimental procedure applied, it was confirmed that schoenite (K2SO4.MgSO4.6H2O) is an inevitable intermediate product of the considered transform
Desalination 167 (2004)
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The seawater extracted from a depth of 30 m has a constant temperature of about 18°C. This water can be used as cold source for the conditioning of Salammbô Museum aquariums (Tunisia). With this intention a passive system, using capillary polypropylene exchangers, is carried out. The tests show that
Desalination 166 (2004)
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