Ivan Lopez

Summary

Country: Uruguay

Publications

  1. ncbi request reprint Co-digestion of ruminal content and blood from slaughterhouse industries: influence of solid concentration and ammonium generation
    I Lopez
    Engineering Faculty, University of the Republic, Montevideo, Uruguay
    Water Sci Technol 54:231-6. 2006
  2. doi request reprint Assessment on the performance of a series of two UASB reactors compared against one of the same total volume using Anaerobic Digestion Model No 1 (ADM1)
    Ivan Lopez
    Facultad de Ingenieria, Universidad de la Republica, Montevideo, Uruguay
    Water Sci Technol 59:647-52. 2009
  3. doi request reprint Modelling of slaughterhouse solid waste anaerobic digestion: determination of parameters and continuous reactor simulation
    Ivan Lopez
    Engineering Faculty, Universidad de la Republica, J Herrera y Reissig 565, Montevideo, Uruguay
    Waste Manag 30:1813-21. 2010
  4. doi request reprint UASB reactor hydrodynamics: residence time distribution and proposed modelling tools
    I Lopez
    Engineering Faculty, Universidad de la Republica, Montevideo, Uruguay
    Environ Technol 31:591-600. 2010
  5. doi request reprint Modelling of an EGSB treating sugarcane vinasse using first-order variable kinetics
    Ivan Lopez
    Facultad de Ingenieria, Universidad de la Republica, Uruguay
    Water Sci Technol 64:2080-8. 2011
  6. doi request reprint Integrated anaerobic treatment of dairy industrial wastewater and sludge
    Mauricio Passeggi
    Engineering Faculty, University of the Republic, Montevideo, Uruguay
    Water Sci Technol 59:501-6. 2009

Collaborators

Detail Information

Publications6

  1. ncbi request reprint Co-digestion of ruminal content and blood from slaughterhouse industries: influence of solid concentration and ammonium generation
    I Lopez
    Engineering Faculty, University of the Republic, Montevideo, Uruguay
    Water Sci Technol 54:231-6. 2006
    ..5 m3/d. The VS stabilisation with a solid retention time of 20 days was of 43%. The pilot reactor working at steady state had a TS concentration of 3-4% with a ratio of RC/blood of 10:1 at the entrance...
  2. doi request reprint Assessment on the performance of a series of two UASB reactors compared against one of the same total volume using Anaerobic Digestion Model No 1 (ADM1)
    Ivan Lopez
    Facultad de Ingenieria, Universidad de la Republica, Montevideo, Uruguay
    Water Sci Technol 59:647-52. 2009
    ..Furthermore, for the same total conversion the volume required by the series is 43% of that of the single reactor...
  3. doi request reprint Modelling of slaughterhouse solid waste anaerobic digestion: determination of parameters and continuous reactor simulation
    Ivan Lopez
    Engineering Faculty, Universidad de la Republica, J Herrera y Reissig 565, Montevideo, Uruguay
    Waste Manag 30:1813-21. 2010
    ..The simulations showed that methane flow peaked at a flow rate of 0.5-0.8 Nm(3)/d/m(reactor)(3) at a residence time of 10-20 days. Simulations allow the adequate selection of operating conditions of a continuous reactor...
  4. doi request reprint UASB reactor hydrodynamics: residence time distribution and proposed modelling tools
    I Lopez
    Engineering Faculty, Universidad de la Republica, Montevideo, Uruguay
    Environ Technol 31:591-600. 2010
    ..Experimental data from a 250 m3 UASB reactor treating malting wastewater are used to calibrate and validate the proposed model...
  5. doi request reprint Modelling of an EGSB treating sugarcane vinasse using first-order variable kinetics
    Ivan Lopez
    Facultad de Ingenieria, Universidad de la Republica, Uruguay
    Water Sci Technol 64:2080-8. 2011
    ..Variation of specific kinetic constants reflects the influence of the fraction of raw vinasse in the feed. High salt concentrations in the reactor may have inhibited the process...
  6. doi request reprint Integrated anaerobic treatment of dairy industrial wastewater and sludge
    Mauricio Passeggi
    Engineering Faculty, University of the Republic, Montevideo, Uruguay
    Water Sci Technol 59:501-6. 2009
    ..LCFA inhibition as assayed using palmitate was found to depend not only on the palmitate concentration but also on the palmitate-to-biomass concentration ratio...