Jesús Rodríguez-Martínez
Research Subjects
Jesús Rodríguez-Martínez has a total of 5 co-authors. Here are the top co-authors by number of shared publications:
- Silvia Yudith Martínez Amador
Universidad Autónoma Agraria Antonio Narro
2 shared publications C. A. Aguilera
Universidad Autónoma de Coahuila, Facultad de Ciencias Químicas, Departamento de Biotecnología, Blvd. V. Carranza y José Cárdenas Valdés, colonia República, CP 25280. Saltillo, Coahuila, Mexico
1 shared publicationG. Y. Garza
Universidad Autónoma de Coahuila, Facultad de Ciencias Químicas, Departamento de Biotecnología, Blvd. V. Carranza y José Cárdenas Valdés, colonia República, CP 25280. Saltillo, Coahuila, Mexico
1 shared publicationS. G. J. Sosa
Universidad Autónoma de Coahuila, Facultad de Ciencias Químicas, Departamento de Biotecnología, Blvd. V. Carranza y José Cárdenas Valdés, colonia República, CP 25280. Saltillo, Coahuila, Mexico
1 shared publicationYolanda Garza-García
Autonomous University of Coahuila
1 shared publication
Latest Publications
- 20 December 2005
- Published by Wiley in Engineering in Life Sciences
- Vol. 5 (6) , 568-573
Influence of Nitrate and Sulfate on the Anaerobic Treatment of Pharmaceutical Wastewater
Anaerobic treatment of wastewater from the pharmaceutical industry, which contained about 3.2 g/L of sulfate, was carried out in an Upflow Anaerobic Sludge Blanket (UASB) reactor. After a startup period of 120 days, a chemical oxygen demand (COD) removal efficiency of more than 90 % was obtained along with an organic loading rate (OLR) of 1.5 g COD/(L day). During the same period, the sulfate removal was about 90 %. However, the performance of the reactor was affected when the loading rate was increased to 2.09 g COD/(L day). It was found that the accumulation of sulfides, combined with a decrease in the pH, affected the reactor performance. In batch reactor studies with pharmaceutical wastewater it was observed that methane production began only after the initiation of nitrate consumption. The denitrification process can inhibit sulfate reduction at high nitrate concentrations, but compared to reactors without nitrate, the sulfate reduction process and sulfide formation were quickly initiated at low nitrate concentrations. The methanogenic activity was however affected by the presence of more than 2 g/L of sulfate.
- 20 December 2005
- Published by Wiley in Engineering in Life Sciences
- Vol. 5 (6) , 568-573
Influence of Nitrate and Sulfate on the Anaerobic Treatment of Pharmaceutical Wastewater
Anaerobic treatment of wastewater from the pharmaceutical industry, which contained about 3.2 g/L of sulfate, was carried out in an Upflow Anaerobic Sludge Blanket (UASB) reactor. After a startup period of 120 days, a chemical oxygen demand (COD) removal efficiency of more than 90 % was obtained along with an organic loading rate (OLR) of 1.5 g COD/(L day). During the same period, the sulfate removal was about 90 %. However, the performance of the reactor was affected when the loading rate was increased to 2.09 g COD/(L day). It was found that the accumulation of sulfides, combined with a decrease in the pH, affected the reactor performance. In batch reactor studies with pharmaceutical wastewater it was observed that methane production began only after the initiation of nitrate consumption. The denitrification process can inhibit sulfate reduction at high nitrate concentrations, but compared to reactors without nitrate, the sulfate reduction process and sulfide formation were quickly initiated at low nitrate concentrations. The methanogenic activity was however affected by the presence of more than 2 g/L of sulfate.
- 4 June 2005
- Published by Oxford University Press (OUP) in Journal of Industrial Microbiology and Biotechnology
- Vol. 32 (11-12) , 691-696
Comparative anaerobic treatment of wastewater from pharmaceutical, brewery, paper and amino acid producing industries
This study concerned the anaerobic treatment of five different industrial wastewaters with a diverse and complex chemical composition. The kinetics of biotransformation of this wastewater at different chemical oxygen demand (COD) were studied in a batch reactor. Wastewater from an amino acid producing industry (Fermex) and from a tank that received several types of wastewaters (collector) contained 0.83 g l−1 and 0.085 g l−1 sulfate, respectively. During the study period of 20 days, methane formation was observed in all types of wastewaters. Studies on COD biodegradation showed the reaction velocity was higher for Fermex wastewater and lower for collector wastewater, with values of 0.0022 h−1 and 0.0011 h−1, respectively. A lower methanogenic activity of 0.163 g CH4 day−1 g−1 volatile suspended solids (VSS) and 0.20 g CH4 day−1 g−1 VSS, respectively, was observed for paper producing and brewery wastewater. Adapted granular sludge showed the best biodegradation of COD during the 20-day period. The sulfate-reducing activity in pharmaceutical and collector wastewater was studied. A positive effect of sulfate-reducing activity on methanogenic activity was noted for both types of wastewaters, both of which contained sulfate ions. All reactions of methane generation for the tested industrial wastewaters were first-order. The results of this study suggest that the tested wastewaters are amenable to anaerobic treatment.
- 4 June 2005
- Published by Oxford University Press (OUP) in Journal of Industrial Microbiology and Biotechnology
- Vol. 32 (11-12) , 691-696
Comparative anaerobic treatment of wastewater from pharmaceutical, brewery, paper and amino acid producing industries
This study concerned the anaerobic treatment of five different industrial wastewaters with a diverse and complex chemical composition. The kinetics of biotransformation of this wastewater at different chemical oxygen demand (COD) were studied in a batch reactor. Wastewater from an amino acid producing industry (Fermex) and from a tank that received several types of wastewaters (collector) contained 0.83 g l−1 and 0.085 g l−1 sulfate, respectively. During the study period of 20 days, methane formation was observed in all types of wastewaters. Studies on COD biodegradation showed the reaction velocity was higher for Fermex wastewater and lower for collector wastewater, with values of 0.0022 h−1 and 0.0011 h−1, respectively. A lower methanogenic activity of 0.163 g CH4 day−1 g−1 volatile suspended solids (VSS) and 0.20 g CH4 day−1 g−1 VSS, respectively, was observed for paper producing and brewery wastewater. Adapted granular sludge showed the best biodegradation of COD during the 20-day period. The sulfate-reducing activity in pharmaceutical and collector wastewater was studied. A positive effect of sulfate-reducing activity on methanogenic activity was noted for both types of wastewaters, both of which contained sulfate ions. All reactions of methane generation for the tested industrial wastewaters were first-order. The results of this study suggest that the tested wastewaters are amenable to anaerobic treatment.