-Rémédiation de pollution par l'huile par des déchets plastiques-Deux problèmes écologiques sont considérés dans ce travail. Un des problèmes est de trouver une application utile des déchets de plastiques, polyéthylène (PE) et polypropylène (PP), qui augmentent jour après jour partout dans le monde. Le deuxième problème est la rémédiation de pollution par l'huile dans des environnements aquatiques. Nous avons utilisé le PE et les poudres feuilles de PP pour absorber l'huile dans de l'eau, par simple contact pendant quelques minutes. L'effet sur l'activité des polymères de soumettre les poudres et les feuilles à une faible dose de radiation γ (3 Mrad) a été étudiée. L'examen des polymères avant et après absorption d'huile par calorimétrie différentielle (DSC) et par microscope électronique de balayage (MEB) a permis d'éclaircir les comportements de ces polymères. Abstract-Adsorption of Spilled Oil from Seawater by Waste Plastic-Two environmental problems are encountered in this work. A solution of one problem is to find a useful application of the waste plastics; polyethylene (PE) and polypropylene (PP), which increases day after day all over the world. The second problem is the oil spill in aquatic locations. We used PE and PP waste powders and sheets to sorb the oil from water, via simple contacting for few minutes. The effect of subjecting the powders and sheets to a low dose of γ-irradiation (3 Mrad) on the activation of the current polymers was investigated. Differential scanning calorimetric (DSC) and scanning electron microscopic (SEM) examinations of the neat and oil sorbing polymers were performed to throw light on the behaviours of these polymers.

Soils polluted by waste lubricant oils may affect the hydrosphere compromising the quality of drinking water resources and threatening the aquatic ecosystems. The objective of this study focused to remove waste-lubricant oils from different polluted sites in El-Minia governorate. In this respect some samples were collected from four different industrial sites and identified as sand, loamy sand, clay loam and loam. Then the field conditions were simulates using two experimental models packed with contaminated soil. The remediation processes carried out in both models using surfactant enhanced by air injection then by water washing. The parameters such as soil type, soil heterogeneity, time and washing process was investigated. The results indicated that the high efficiency of oil removal is obtained from sand where the clay loam gives the worst results. The results also reveal that, the high flushing and washing duration time can be attributed to the high percentage of mud in some sites over other sites. This means that the performance of surfactant flushing/water washing can be adversely affected by geologic heterogeneity. Finally, it’s suitable to use pressurized liquid technologies in heterogeneous media, but cleanup times will be longer and more difficult than for the other similar homogeneous media.

Surfactants enhanced air sparging actually acts to displace the organic contaminant entrapped in soil pores. In this work, a comparison study was carried out between two air-flushing modes, namely, continuous air flushing and pulsed air flushing, which was conducted to remediate soil contaminated with waste-lubricant oil. Therefore, coarse sand was artificially polluted and mixed well with waste-lubricant oil at different concentrations of 10, 25 and 50 wt% to give the soil an oil blend. Then a laboratory glass column was established and backed with contaminated soil to study the effect of flow rate, pollutant and surfactant concentrations on the removal of waste-lubricant oil from soil. The contaminated soil was washed with pure water and flushed with both air-flushing modes at a pressure of 2 kPa and flow rate of 6 L min⁻¹. After that fixed 300 mL nonionic surfactant solutions (NPEO_9.3) at concentrations of 3, 5 and 7 wt%, were poured individually along with air injection at the same pressure and flow rate. The treated soil was washed several times with pure water to eliminate the residual surfactant solutions. It was found that water washing and air injection remove 27 % of oil; however, air injection along with surfactant solutions increased the oil removal efficiency up to 90 %. Moreover, both air-flushing modes succeeded in removing the pollutant with majority to pulsed air mode over continuous mode; therefore, pulsed air flushing was applied for 25 and 50 wt% waste lubricant oils in presence of 3 wt% nonionic surfactant.

Four samples from different crude oils were used for this study: light and heavy crude oils from Iran and two crude oils from Egypt, namely, Ras Gharb and Suez mix. The asphaltenes were separated from these crude oils and then the maltene (non‐asphaltenic fraction) was fractionated into waxes, aromatics, and resins. All fractions were characterized using FTIR and UV spectroscopic analyses in addition to gel permeation chromatograph (GPC). These fractions were tested for their emulsion stability. For chemometric analysis different parameters (variables) have been used to study the effect of different fractions (objects) on the emulsion stability. Such variables included the integrated areas under the stretching absorption peaks of CH in the range of 3000–2800 cm⁻¹, C˭O in the range of 1750–1650 cm⁻¹, and the aromatic C˭C in the range of 1650–1550 cm⁻¹, as well as UV absorption value at 235 nm and average molecular weight (MW). Principal component analysis (PCA) and multiple linear regression (MLR) were conducted for examining the relationship between multiple variables and the stability of water‐in‐crude oil emulsions. The results of PCA explain the interrelationships between the observations and variables in multivariate data. The correlation coefficients between different parameters derived from PCA reveals that the UV absorption value and MW are strongly correlated with emulsion stability. It also reveals that the resins, asphaltenes, and maltene have better emulsion stability than waxes and lower molecular weight aromatics. The linear relationship between the parameters and the stability of water‐in‐crude oil emulsions using MLR was modeled according to the better statistical results. The obtained mathematical model can be used to predict the stability of water‐in‐crude oil emulsions from the chemical groups and functionalities in each crude oil fraction.

In this study, computer software was used in order to estimate the scaling tendency of the commingling of two incompatible waters existed in Egyptian oil reservoirs of Gulf of Suez area. The chemical analyses of the two incompatible waters (injection and formation waters) have been used as input data to the computer simulator. The reservoirs characterized by a temperature of 90–127°C, and salinity of 100,000–230,000 ppm. The scaling results for the commingling of both injection and formation water at reservoir temperatures and pressures are recorded. The results of theoretical software and laboratory jar-testing were compared. It was found that mixing of the injection water and formation water may lead to calcium carbonate and barium sulphate scaling at 40% formation water in absence of scale inhibitor. Two types of commercial scale inhibitors (AII and SII) were evaluated using both jar test method and National Association of Corrosion engineers standard test methods. The results showed the mastery of AII over the commercial inhibitor SII in preventing of both scales.

This work pertains to study the asphaltenes aggregates' settling behavior of crude oil in absence and presence of oil‐soluble surfactants including long‐chain fatty acid in the form of amidation and estrification. First, the onset points as a function of light absorbed asphaltenes aggregates were quantified before and after adding asphaltenes dispersants using ultra violet spectroscopy, and the photograph fractal‐like aggregate structures were quantified using Carl Zeiss Trinocular microscope. Second the shear rates against shear stress induced aggregation were also measured in absence and presence of different concentrations of asphaltenes dispersants using Brookfield digital rheometer model LVDV‐III⁺. The results reviled that the asphaltenes aggregates are found to depend on toluene–heptane ratios. In absence of dispersant the accumulated and aggregates clusters of asphaltenes are formed at heptane: toluene ratio of 50∶50. Whereas, in the presence of dispersant the asphaltenes are solvated at heptane: toluene ratio of 60∶40, followed by appearance of stronger and dots aggregates clusters at a ratio of 70∶30, and finally, a larger aggregates growing at heptane: toluene ratio of 80∶20. The dispersant solvates the asphaltenes and maintains them in solution, while their surface activity remains high. This means that the dispersant apparently functioned well in decreasing the degree of flocculation and precipitation beyond the critical micelle concentration (CMC) of asphaltenes at 0.0027 g/L. Also, the reduction in the viscosity in presence of dispersant suggests that the asphaltenes aggregates are highly porous and very fragile.