Unprocessed petroleum hydrocarbons often contain high concentrations of mercury (Hg), which can severely damage the metal components of a processing plant and pose a health risk to the workers and the natural environment. Although Hg removal units can significantly reduce the Hg concentration in the export products, they are often installed in the final stage of the processing plant, thus failing to protect the production facilities. In this study, Hg distribution within a natural gas processing plant was studied to identify the most effective place for a Hg removal unit. Additionally, the impact of sampling container materials and their acidification was evaluated, and Hg species in the condensate were quantified. Total Hg concentration was significantly higher in all samples stored in glass in comparison to that with plastic containers. However, the acidification effect of the containers was more pronounced for Hg in nonpolar solutions. Interestingly, the assessment of Hg distribution within the gas plant showed that the export gas is being enriched in Hg, whose concentration rose from 1.25 to 4.11 μg/Sm3 during the processing steps. The second stage separator was identified as the source of excess Hg, which partitioned from the liquid phase of condensate to the gas phase as a result of reduced operational pressure and temperature. The dominant Hg species found in the analyzed gas condensates were elemental Hg (Hg0) and inorganic Hg with the methylmercury fraction comprising up to 18%. However, it was also found that the % fraction of individual Hg species varied along the plant units most likely as a result of Hg0 migration to the export gas. Therefore, to protect all treatment facilities from Hg contamination, the Hg removal unit should be installed after the second stage compressor.

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A highly porous phosphorous-containing activated carbon derived from pistachio nutshells (PNS) was synthesis as a potential sorbent for uranium (VI) from sulfate media. The prepared phosphate activated carbon (PAC) was visualized under SEM and TEM which revealed a highly porous structure. The extraction of U(VI) from acidic media using PAC was investigated by a batch method and various parameters such as pH, equilibrium contact time, liquid to solid ratio, and initial U(VI) concentration were examined. Under the stated conditions, the optimum pH for U(VI) adsorption was found to be 3.5. The adsorption capacity of uranium upon PAC under the optimum conditions was found to be 335 mg/g. The experimental results were applied for Langmuir, Freundlich, Temkin, and Dubinin-Radushkevich (D-R) isotherm models. The thermodynamic equilibrium constant and the Gibbs free energy were determined (ΔG° from -4.72 to -7.65 kJ/mol) and results indicated the spontaneous nature of the adsorption process. Kinetics data were best described by pseudo second-order model.

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