Physico-chemical changes in cladodes of Opuntia ficus-indica as a function of the growth stage and harvesting areas

The physicochemical properties of cladodes Opuntia ficus-indica (OFI) vary widely during maturation. However, few studies have been performed to evaluate changes in chemical characteristics on the pad depending on the maturity stages. Chemical proximate analysis like the content of total sugars, protein, dry matter, pH, conductivity and ash, depending on the variation of weight of the pad and the growing region was done to determine the changes of characteristics of nopal. Significant changes in physicochemical properties were observed among harvesting sites and during the growing stages. The principal component analysis was then performed to evaluate the relationship between harvesting sites, growth stages, and physicochemical properties. Results highlighted that Sidi El Aidi can be categorized as a poor ecotype among the studied ecotypes, besides, overall harvesting sites pH and proteins had a significant negative correlation with ash, total sugars, reducing sugars, conductivity proteins decrease with increasing age of nopals while total sugars, reducing sugars, and ash content showed the opposite trend. The high total sugar content, minerals of nopal pad (weight higher than 200 g) and proteins (weight lower than 200 g) could be an interesting source of these important components for human diets and also could be used in food, cosmetics, and pharmaceutical industry.

Removal of Basic Red 46 dye from aqueous solution by adsorption onto Moroccan clay

In this study, Moroccan crude clay of Safi, which was characterized by X-ray diffraction, is used as adsorbent for the investigation of the adsorption kinetics, isotherms and thermodynamic parameters of the Basic Red 46 (BR46) in aqueous solutions at various dye concentrations, adsorbent masses and pH values. The results showed that the adsorption capacity of the dye increased by initial dye concentration and pH values. Two kinetic models (the pseudo-first-order and the pseudo-second-order) were used to calculate the adsorption rate constants. The adsorption kinetics of the basic dye followed pseudo-second-order model. The experimental data isotherms were analyzed using the Langmuir, Freundlich and Dubinin-Radushkevish equations. The monolayer adsorption capacity for BR46 dye is 54 mg/g of crude clay. Nearly 20 min of contact time was found to be sufficient for the dye adsorption to reach equilibrium. Thermodynamical parameters were also evaluated for the dye-adsorbent system and revealed that the adsorption process is exothermic in nature.

Discoloration of a red cationic dye by supported TiO(2) photocatalysis

The degradation under UV, visible and sunlight irradiation of C.I. Basic Red 46 (BR 46) dye used for acrylic fibers dyeing has been studied in a lab-scale continuous system with two different immobilized TiO(2) systems. Catalyst I was based on TiO(2) particles deposited on cellulose fibers; Catalyst II combined TiO(2) particles deposited on a layer of cellulose fibers (as in Catalyst I) with a layer of carbon fibers and finally a layer of cellulose fibers. The treatment of aqueous dye solutions and industrial wastewater contaminated with the same dye has been evaluated in terms of color removal and chemical oxygen demand (COD) decrease. With UV light, aqueous solutions containing dye were decolorized slightly more rapidly with Catalyst II than with Catalyst I. Sunlight was also very effective and experiments involving sunlight irradiation showed Catalyst II to be the more efficient, giving more than 90% discoloration after 20 min of treatment. Comparing the discoloration yield by adsorption or under visible light for both catalysts, it was observed that the difference between them is below 5%. The adsorption kinetics was found to follow a second-order rate law for Catalyst I and a first-order rate law for Catalyst II. The kinetics of photocatalytic degradation under UV or sunlight were found to follow a first-order rate law for both catalytic systems. Under sunlight the COD removal yield for textile wastewater reaches 33% with Catalyst I against 93% with Catalyst II.