Determining the best location is a complex process that faces decision makers. In the City of Tartous, Syria, this problem springs while selecting the best location for wastewater treatment plant (WWTP) because of the large number of criteria and co
nstrains and the uncertainty in expert's judgments. To solve this problem, we designed a frame work containing multi-criteria decision making (MCDM) technique that is fuzzy analytic hierarchy process (FAHP) to handle the uncertainty situations and geographical information system (GIS) to determine the best location.
In this paper, the FAHP idea was developed to calculate weights of the criterias, the GIS was used to overlay and generate criteria and suitability maps. The study ends with a map of the best sites for constructing wastewater treatment plants by extended aeration method in Tartous region in Syria.
Mixtures of polycarboxylic acids and their salts with sodium
tripolyphosphate and sodium pyrophosphate have been investigated in the
presence of ammonium oxalate and sodium carbonate. Some of these mixtures
demonstrated good chelating power synerg
y and some mixures inhibited the
chelating power of the individual components from which the mixures
composed of. The chelating power synergy of some mixtures can be used for
enhancing the function of the builders and consequently decrease the weight of
the detergent meanwhile the inhibition of the chelating power in the other
mixtures can be used for precipitating their components in the treated water in
optimum conditions. It is worth to mention that the chelating powers of sodium
tripolyphsphate and citric acid increased as many as 3-88 times by changing
some experimental conditions.
A new ion exchanger has been prepared from syrian petroleum coke (S. P.
C) of high sulphur content. Preparation of this ion exchanger was carried out
by simple treatment of S. P. C with oleum at room temperature followed with
statical ion exchange
in aqueous sodium chloride solutions.
The First, SPC ion exchanger with granular structure resulted from
reacting 20 gr of the SPC granules with 20 ml of oleum. Where as a friable ion
exchanger was produced when 40 ml of oleum were used in the process.
The adsorption capacity of the two SPC ion exchangers was found out to be
100 mgeq and 170 mgeq respectively.