Research Abstracts

2181 - 2190 of 3156 results

The management of residual sludge is an important subject. New environmental laws require the elimination of this waste by only two ways: incineration and agricultural use. In order to reach this goal, mechanical dewatering can be used as a first step due to its low energy cost. However, the final m
Desalination 167 (2004)

The reuse of effluents for irrigation and indirect potable water uses is rapidly developing as an alternative to seawater desalination. This paper explores two membrane-based options available to treat sewage for water reuse, tertiary filtration (TF) of the effluent from a conventional activated slu
Desalination 167 (2004)

All MSF desalination plants have been operated at a top brine temperature below 120°C. That is because of sulfate scaling phenomena, which usually occurs when the temperature is higher than 120°C. This type of scaling is hard scale that cannot be removed easily by chemical or mechanical cleaning. In
Desalination 167 (2004)

Multi-stage flash (MSF) and reverse osmosis (RO) are the most common techniques for seawater desalination. A significant difference between these methodologies consists of their different energy requirements, i.e., thermal energy for MSF and mechanical energy for RO plants. The presence of both desa
Desalination 166 (2004)

a process flow sheet and a plan view are given. A preliminary study on further R&D actions and possible measures to enhance plant economy are also discussed.
Desalination 168 (2004)

The Mirfa power and desalination plant was built in the Abu Dhabi Emirate, United Arab Emirates, in the early 1990s. Plant capacity is16.5 MGD. It was decided to increase the plant’s capacity to satisfy rapid urban and industrial development in the Emirate. A comprehensive study was carried out to i
Desalination 166 (2004)

Experimental data on desorption isotherms of three types of clay at different temperatures (40, 50 and 60°C) were determined using a static method. The results were fitted by the famous Guggenheim-Anderson-deBoer (GAB) model. The thermodynamic functions, differential heat of sorption, net integral e
Desalination 166 (2004)

We report the results of experiments conducted under the well known ACS ED membrane, using the membrane potential technique, in order to obtain the transference numbers of Na+ and Br! before and after lengthy filtration studies using brackish waters from France and Senegal. With a change of the Br!
Desalination 167 (2004)

Several configurations of polygeneration systems, conceived for a dairy industry requiring cold, heat, power and water for its operation, are presented. For these systems, a single fuel is used to produce cold, steam (heat), electricity and water from a combined cycle integrated and optimized with h
Desalination 166 (2004)

Water scarcity in Mediterranean areas such as Comunidad Valenciana (Spain) makes water reuse necessary in high water-consuming industries. Previous studies by our research group showed that nanofiltration (NF) membrane permeates could be reused in some processes of finishing, dyeing and printing in
Desalination 167 (2004)