Ceramic membrane
11 - 20 of 22 results
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In this paper, a two-step membrane treatment for acidic rinsing water is described including project idea, laboratory tests, pilot plant experiments and finally plant construction. The task is to recover metal and sulphuric acid from rinsing water originating from the electro-zinc coating line at Sa
Desalination 224 (2008)
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Micro/sub-micron emulsion and related systems have received a lot of attention in the last years for their common use as vehicles for topical administration. These systems can be defined as fine emulsion dispersion with droplet sizes in the sub-micron range. The main advantages of such systems are h
Desalination 224 (2008)
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Biological wastewater treatment plants (BWWTP) are widely used to treat effluents from chemical process industry. However, there exist refractory substances, such as phenolic compounds, which require previous treatments. Advanced oxidation processes (AOP) are thoroughly being studied as pre-treatmen
Desalination 221 (2008)
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In the ultrafiltration (UF) of disperse dye solutions using ceramic membrane, backflushing is necessary to minimize the formation of fouling by disperse dye, and to enhance the permeate flux. In this work, the effects of backflushing on the ultrafiltration performance and decolorization were investi
Desalination 202 (2007)
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The ceramic microfiltration system with periodic N2-back-flushing was operated for treating paper wastewater discharged from a company making toilet papers by recycling milk or juice cartons. Two kinds of alumina membranes with 7 channels used here for recycling paper wastewater. The optimal N2 filt
Desalination 202 (2006)
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Ceramic microfiltration combined with powdered activated carbon adsorption (PAC-MF) was tested for organic and microbial control using river water laden with sewerage effluents. The PAC-MF was compactly configured with PAC adsorption and MF filtration zones in one reactor. It was operated with PAC a
Desalination 202 (2006)
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The surface properties of both suspensions and membranes vary with solution environments in the microfiltration of mineral particulate suspensions using ceramic membranes. It remained uncertain which one might be more important in determining the filtration flux. In this paper the influences of pH a
Desalination 177 (2005)
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The use of inorganic membranes in pollution treatment is actually limited by the cost of such membranes. Advantages of inorganic membranes over organic ones are their chemical, thermal and pH resistance. In this study, low cost ZnAl2O4-TiO2 ultrafiltration membranes were tested for removing Cd(NO3)2
Desalination 168 (2004)
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In order to avoid hydrophilic behaviour of ceramic membranes prepared with metal oxides, alumina and zirconia membranes with 200 and 50 nm pore diameters were grafted with fluoroalkylsilanes. The grafting was controlled by TGA, and the hydrophobicity was characterised by water contact angle and perm
Desalination 168 (2004)
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The aim of the study was to compare potato and potato–tapioca hydrolysate quality obtained by membrane filtration with the application of tubular ceramic membranes. The substrate for membrane filtration was maltodextrins obtained by enzymatic hydrolysis of potato and a mixture of potato and tapioca
Desalination 162 (2004)
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