Petroleum wastewater: Environmental protection, treatment, and safe reuse: An overview.

Oil petroleum production consumes about 1.0-7.2 bbl. The needed water for such production ranges between 0.47 and 7.2 L water to 1.0 L crude. Between 80 and 90% of the consumed water is disposed of as wasted effluents. Consequently, there is an important connection between petroleum production and the contamination of the environment and surface water in addition to their ecotoxicological effects. The objective of the present review is to through light on the hazardous impact of petroleum wastewater on the environment and water ways. The present study presents several wastewater treatment technologies in handling the petroleum produced water (PPW) and reducing the hazardous impact to the environment. Safe reuse is also presented including simple, advanced, and environmentally friendly techniques. The reported treatment technologies are divided into five main categories: membrane technologies, biological treatment processes, electro-chemical coagulation, physical/chemical treatment processes (dissolved air flotation (DAF)/air flotation (IAF), adsorption, and chemical flocculation), and catalytic oxidation including chemicals such as advanced and Fenton oxidation processes (AOPs). The analysis and observation of each treatment process are also presented. Implementing of these processes in sequential and/or in combined to avoid the drawbacks of any poor treatment are discussed. The present review discusses; also, in detail each of these treatment technologies and their efficiency including the observation and conclusions of each one. The study shows; also; how the final treated effluent can be reused for non-potable purposes as an additional water resource according to the degree of decontamination. An additional advantage of treatment is protection of both the environment and the water ways by avoiding any discharge of such hazardous wastewater.

Stem powder and its active carbon of Arachis hypogaea plant for lead (II) removal: application to treat battery-based industrial effluents.

Stem powder and its active carbon of Arachis hypogaea plant are identified to have strong adsorptivity for lead ions. The bio-sorbents are characterized by conventional methods including XRD and FTIR analysis. These biomaterials are investigated for their maximum adsorption for lead ions by optimizing the extraction conditions. The maximum removal is observed in the pH range of 6-7 for both sorbents. With stem powders, the removal is 76.0% from a simulated lead solution of concentration: 20.0 mg/L with 1.5 g/L of the sorbent and at an equilibration time of 2.0 h. With the active carbon, the maximum extraction of: 86.0% is observed at pH: 6.5 with 1.0 g/L of the sorbent after an equilibration time of 1.5 h. The sorption capacities are 32.0 mg/g for stem powders, and 40.5 mg/g for active carbon. Many co-ions have marginal interference. Spent adsorbents can be recycled after regeneration. Thermodynamic investigations reveal the spontaneity and endothermic nature of adsorption. High ΔH values viz., 26.45 kJ/mole for AHSP and 46.40 kJ/mole for AHSAC, confirm the bonding of Pb2+ ions with the sorbents is either "ion-exchange" and/or a sort of "complex formation." The disorder at the solid and liquid boundary is indicated by high positive ΔS values and it is a favorable condition for good Pb2+ adsorption. On analysis of different kinetic and isotherm models, the sorption of Pb2+ ions follows Pseudo-2nd order and Langmuir models. This confirms the mono-layer adsorption of Pb2+ ions on the humongous surface of the sorbent. The adsorbents are successfully applied to treat industrial effluent samples.

In the present investigation, stem powder and its active carbon of Arachis hypogaea plant are identified to have strong adsorptivity for highly toxic lead ions. Successful methodologies are developed for the maximum extraction of lead ions from industrial wastewater at a convenient nearly neutral pH. The adsorption capacities are as high as: 32.0 mg/g for stem powders and 40.5 mg/g for active carbon. The sorbents are characterized and the sorption mechanism is investigated. The novelty of the present investigation is that highly toxic lead ions can be easily removed from polluted water by using simple bio-adsorbents by adopting convenient procedures.

Tratamento de efluentes: remoção de detergente utilizando processo Fenton com ultrassom e prego reutilizado / Effluent treatment: detergent removal using Fenton ultrasound process and reused nail

RESUMO Diferentes metodologias são descritas na literatura para tratamento de efluentes industriais. Entretanto, a maioria dos processos não são totalmente eficientes quando o efluente apresenta baixo conteúdo de partícula coloidal suspensa e alta concentração de matéria orgânica e detergentes. Entre os métodos que são estudados para eliminar detergente e matéria orgânica de efluentes industriais, o processo Fenton é uma estratégia atraente. No presente estudo, foi aplicada uma metodologia para remoção de detergente de efluentes líquidos utilizando processo Fenton com ultrassom e prego reutilizado. A otimização de parâmetros para tratamento do efluente foi realizada por meio das análises de pH, detergente, cor, turbidez, demanda química de oxigênio, demanda bioquímica de oxigênio, óleos e graxas, e sólidos suspensos. Os melhores resultados foram obtidos em pH 3,5, com 90 mg L−1 de peróxido de hidrogênio e um prego de ferro (2,7g) tanto para o processo Fenton como para o Fenton com ultrassom. Nessas condições, os valores de remoção de detergente foram de 99,4%. Em pH 2,5, 4,5 e 5,5, os valores obtidos para remoção de detergente foram menores, 75,2, 89,5, 68,4%, respectivamente. Resultados semelhantes foram obtidos para cor, turbidez, demanda química de oxigênio e demanda bioquímica de oxigênio. A reutilização dos pregos mostrou que a eficiência média na remoção de detergente até o quarto ciclo foi acima de 90%, e, a partir do quinto ciclo, observou-se uma diminuição gradativa, sendo a diferença entre o primeiro e o sexto ciclo em torno de 10%.

ABSTRACT Different methodologies are described in the literature for the industrial effluents treatment. However, most processes are not fully efficient when the effluent has low suspended colloidal particle content and high concentration of organic matter and detergents. Among the methods that are studied to eliminate detergent and organic matter from industrial effluents, the Fenton process is an attractive strategy. In the present study, a more sustainable methodology was applied to remove detergent and organic matter from liquid effluents using Fenton process with ultrasound and recycled nail. The optimization of parameters for effluent treatment was carried out through the analysis of pH, detergents, color, turbidity, chemical oxygen demand, biochemical oxygen demand, oils and greases, and suspended solids. The best results were obtained at pH 3.5, with 90 mg L−1 of hydrogen peroxide and an iron nail (2.7 g) both for the Fenton process and Fenton with ultrasound. Under these conditions, detergent removal values were 99.4%. At pH 2.5, 4.5, and 5.5, the values obtained for detergent removal were lower, 75.2, 89.5, and 68.4%, respectively. Similar results were obtained for color, turbidity, chemical oxygen demand, and biochemical oxygen demand. The reuse of the nails showed that the average detergent removal efficiency up to the fourth cycle was above 90%, and, from the fifth cycle, a gradual decrease was observed, with the difference between the first and sixth cycles being around 10%.

Treatment of As-rich mine effluents and produced residues stability: Current knowledge and research priorities for gold mining.

Refractory ores, in which gold is often embedded within As-bearing and acid-generating sulfide minerals, are becoming the main gold source worldwide. These ores require an oxidizing pre-treatment, prior to cyanidation, to efficiently breakdown the sulfides and enhance gold liberation. As a result, large volumes of As-rich effluents (> 500 mg/L) are produced through the pre-oxidation of refractory gold ores and/or the exposure of As-bearing tailings upon exposure to air and water. Limited information is available on performant treatment of these effluents, especially of pre-oxidation effluents characterized by a complex chemistry, extremely acidic or alkaline pH and high concentrations of arsenic. The treatment of As-rich effluents is mainly based on precipitation (using Al or Fe salts and/or Ca-based compounds) and (electro)-chemical or biological oxidation processes. A performant treatment process must maximize As removal from contaminated mine water and allow for the production of residues that are geochemically stable over the long term. An extensive literature review showed that Fe(III)-As(V) precipitates, especially bioscorodite and (nano)scorodite, appear to be the most appropriate forms to immobilize As due to their low solubility and high stability, especially when encapsulated within an inert material such as hydroxyl gels. Research is still required to assess the long-term stability of these As-bearing residues under mine-site conditions for the sustainable exploitation of refractory gold deposits.

From spent Mg/Al layered double hydroxide to porous carbon materials.

Adsorption has been considered as an efficient method for the treatment of dye effluents, but proper disposal of the spent adsorbents is still a challenge. This work attempts to provide a facile method to reutilize the spent Mg/Al layered double hydroxide (Mg/Al-LDH) after the adsorption of orange II (OII). Herein, the spent hybrid was carbonized under the protection of nitrogen, and then washed with acid to obtain porous carbon materials. Thermogravimetric analysis results suggested that the carbonization could be well achieved above 600°C, as mass loss of the spent hybrid gradually stabilized. Therefore, the carbonization process was carried out at 600, 800, and 1000°C, respectively. Scanning electron microscope showed that the obtained carbon materials possessed a crooked flaky morphology. Nitrogen adsorption-desorption results showed that the carbon materials had large BET surface area and pore volume, e.g., 1426 m(2)/g and 1.67 cm(3)/g for the sample carbonized at 800°C. Moreover, the pore structure and surface chemistry compositions were tunable, as they were sensitive to the temperature. Toluene adsorption results demonstrated that the carbon materials had high efficiency in toluene removal. This work provided a facile approach for synthesizing porous carbon materials using spent Mg/Al-LDH.

Alternativas para o tratamento de efluentes da indústria galvânica / Alternatives for the galvanic wastewater treatment

Os métodos de precipitação química, cristalização e extração líquido-líquido foram aplicados visando propor alternativas para o tratamento de efluentes líquidos gerados pela indústria de galvanoplastia. Efluentes de diversas empresas do setor, localizadas no estado de Minas Gerais (Brasil), foram coletados e caracterizados. O efluente estudado, proveniente de empresa de galvanização de zinco a quente, continha cerca de 90 g/L de ferro total, 35 g/L de zinco e menores quantidades de Al, Ni e Cu, em meio ácido clorídrico (pH = 0,6). A separação seletiva entre ferro e zinco não se mostrou eficiente por precipitação, sendo a técnica adequada somente no tratamento do efluente, ao contrário da cristalização e extração líquido-líquido utilizando-se TBP como agente extratante. A integração destas técnicas ainda requer estudos mais detalhados visando à otimização de custos e das condições operacionais.

Separation methods such as chemical precipitation, crystallization and liquid-liquid extraction have been investigated aiming to treat effluents generated by the galvanic industry. Effluent samples generated by several companies located in the state of Minas Gerais (Brazil) were collected and chemically characterized. For this work, a typical zinc hot-dip galvanizing effluent containing about 90 g/L of total iron, 35 g/L of zinc and minor amounts of Al, Ni, Cu, in HCl medium (pH = 0.6) was treated. A selective separation between metals zinc and iron was not achieved by chemical precipitation, which was found adequate to threat water only. On contrary, zinc and iron was separated very efficiently by crystallization and liquid-liquid extraction using TBP as extractant agent. The integration of these methods to recover zinc and iron from effluent still requires more detailed studies.