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1.
PLoS One ; 12(2): e0170985, 2017.
Artículo en Inglés | MEDLINE | ID: mdl-28234917

RESUMEN

The present feature describes for the first time the application of spores from Aspergillus sp. IMPMS7 to break out crude oil-in-water emulsions (O/W). The fungal spores were isolated from marine sediments polluted with petroleum hydrocarbons. The spores exhibited the ability to destabilize different O/W emulsions prepared with medium, heavy or extra-heavy Mexican crude oils with specific gravities between 10.1 and 21.2°API. The isolated fungal spores showed a high hydrophobic power of 89.3 ± 1.9% and with 2 g of spores per liter of emulsion, the half-life for emulsion destabilization was roughly 3.5 and 0.7 h for extra-heavy and medium crude oil, respectively. Then, the kinetics of water separation and the breaking of the O/W emulsion prepared with heavy oil through a spectrofluorometric technique were studied. A decrease in the fluorescence ratio at 339 and 326 nm (I339/I326) was observed in emulsions treated with spores, which is similar to previously reported results using chemical demulsifiers.


Asunto(s)
Emulsionantes/química , Emulsiones/química , Esporas Fúngicas/metabolismo , Agua/química , Aspergillus/química , Aspergillus/metabolismo , Emulsionantes/metabolismo , Sedimentos Geológicos/química , Sedimentos Geológicos/microbiología , Interacciones Hidrofóbicas e Hidrofílicas , Petróleo/efectos adversos , Esporas Fúngicas/química , Contaminación Química del Agua/efectos adversos , Contaminación Química del Agua/prevención & control
2.
J Biosci Bioeng ; 114(4): 440-5, 2012 Oct.
Artículo en Inglés | MEDLINE | ID: mdl-22704814

RESUMEN

A considerable portion of oil reserves in Mexico corresponds to heavy oils. This feature makes it more difficult to recover the remaining oil in the reservoir after extraction with conventional techniques. Microbial enhanced oil recovery (MEOR) has been considered as a promising technique to further increase oil recovery, but its application has been developed mainly with light oils; therefore, more research is required for heavy oil. In this study, the recovery of Mexican heavy oil (11.1°API and viscosity 32,906 mPa s) in a coreflood experiment was evaluated using the extremophile mixed culture A7, which was isolated from a Mexican oil field. Culture A7 includes fermentative, thermophilic, and anaerobic microorganisms. The experiments included waterflooding and MEOR stages, and were carried out under reservoir conditions (70°C and 9.65 MPa). MEOR consisted of injections of nutrients and microorganisms followed by confinement periods. In the MEOR stages, the mixed culture A7 produced surface-active agents (surface tension reduction 27 mN m⁻¹), solvents (ethanol, 1738 mg L⁻¹), acids (693 mg L⁻¹), and gases, and also degraded heavy hydrocarbon fractions in an extreme environment. The interactions of these metabolites with the oil, as well as the bioconversion of heavy oil fractions to lighter fractions (increased alkanes in the C8-C30 range), were the mechanisms responsible for the mobility and recovery of heavy oil from the porous media. Oil recovery by MEOR was 19.48% of the residual oil in the core after waterflooding. These results show that MEOR is a potential alternative to heavy oil recovery in Mexican oil fields.


Asunto(s)
Industria Procesadora y de Extracción/métodos , Yacimiento de Petróleo y Gas/microbiología , Petróleo/metabolismo , Thermoanaerobacter/metabolismo , Alcanos/metabolismo , Hidrocarburos/metabolismo , México , Datos de Secuencia Molecular , Tensión Superficial , Tensoactivos/metabolismo , Thermoanaerobacter/genética , Thermoanaerobacter/aislamiento & purificación , Viscosidad
3.
Water Res ; 38(14-15): 3313-21, 2004.
Artículo en Inglés | MEDLINE | ID: mdl-15276748

RESUMEN

Refinery wastewaters may contain aromatic compounds and high concentrations of sulfide and ammonium which must be removed before discharging into water bodies. In this work, biological denitrification was used to eliminate carbon, nitrogen and sulfur in an anaerobic continuous stirred tank reactor of 1.3 L and a hydraulic retention time of 2 d. Acetate and nitrate at a C/N ratio of 1.45 were fed at loading rates of 0.29 kg C/m3 d and 0.2 kg N/m3 d, respectively. Under steady-state denitrifying conditions, the carbon and nitrogen removal efficiencies were higher than 90%. Also, under these conditions, sulfide (S(2-)) was fed to the reactor at several sulfide loading rates (0.042-0.294 kg S(2-)/m3 d). The high nitrate removal efficiency of the denitrification process was maintained along the whole process, whereas the carbon removal was 65% even at sulfide loading rates of 0.294 kg S(2-)/m3 d. The sulfide removal increased up to approximately 99% via partial oxidation to insoluble elemental sulfur (S0) that accumulated inside the reactor. These results indicated that denitrification is a feasible process for the simultaneous removal of nitrogen, carbon and sulfur from effluents of the petroleum industry.


Asunto(s)
Carbono/aislamiento & purificación , Nitritos/química , Nitrógeno/aislamiento & purificación , Azufre/aislamiento & purificación , Eliminación de Residuos Líquidos/métodos , Acetatos/química , Bacterias Anaerobias/metabolismo , Biomasa , Reactores Biológicos , Carbono/metabolismo , Hidrocarburos Aromáticos/química , Nitratos/química , Nitratos/metabolismo , Nitritos/metabolismo , Nitrógeno/metabolismo , Oxidación-Reducción , Petróleo , Compuestos de Amonio Cuaternario/química , Sulfuros/química , Azufre/metabolismo
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