Filtros : "Alemanha" "Bioprocess Engineering" "EP" Removidos: "IQ011" "ENGENHARIA NAVAL E OCEÂNICA" "ug" "Financiamento FAPERGS" "International Mineral Processing Congress" Limpar

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  • Source: Bioprocess Engineering. Unidade: EP

    Subjects: BIOTECNOLOGIA, FERMENTAÇÃO

    Acesso à fonteDOIHow to cite
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    • ABNT

      VILAÇA, Patrícia Ribeiro et al. Determination of power consumption and volumetric oxygen transfer coefficient in bioreactors. Bioprocess Engineering, v. 22, p. 261-265, 2000Tradução . . Disponível em: https://doi.org/10.1007/s004490050730. Acesso em: 08 out. 2024.
    • APA

      Vilaça, P. R., Badino Junior, A. C., Facciotti, M. C. R., & Schmidell Netto, W. (2000). Determination of power consumption and volumetric oxygen transfer coefficient in bioreactors. Bioprocess Engineering, 22, 261-265. doi:10.1007/s004490050730
    • NLM

      Vilaça PR, Badino Junior AC, Facciotti MCR, Schmidell Netto W. Determination of power consumption and volumetric oxygen transfer coefficient in bioreactors [Internet]. Bioprocess Engineering. 2000 ; 22 261-265.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/s004490050730
    • Vancouver

      Vilaça PR, Badino Junior AC, Facciotti MCR, Schmidell Netto W. Determination of power consumption and volumetric oxygen transfer coefficient in bioreactors [Internet]. Bioprocess Engineering. 2000 ; 22 261-265.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/s004490050730
  • Source: Bioprocess Engineering. Unidade: EP

    Subjects: FERMENTAÇÃO ALCOÓLICA, REATORES QUÍMICOS

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    • ABNT

      OLIVEIRA, Samuel Conceição de et al. Continuous ethanol fermentation in a tower reactor with flocculating yeast recycle: scale-up effects on process performance, kinetic parameters and model predictions. Bioprocess Engineering, v. 20, n. 6, p. 525-530, 1999Tradução . . Disponível em: https://doi.org/10.1007/s004490050624. Acesso em: 08 out. 2024.
    • APA

      Oliveira, S. C. de, De Castro, H. F., Visconti, A. E. S., & Giudici, R. (1999). Continuous ethanol fermentation in a tower reactor with flocculating yeast recycle: scale-up effects on process performance, kinetic parameters and model predictions. Bioprocess Engineering, 20( 6), 525-530. doi:10.1007/s004490050624
    • NLM

      Oliveira SC de, De Castro HF, Visconti AES, Giudici R. Continuous ethanol fermentation in a tower reactor with flocculating yeast recycle: scale-up effects on process performance, kinetic parameters and model predictions [Internet]. Bioprocess Engineering. 1999 ; 20( 6): 525-530.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/s004490050624
    • Vancouver

      Oliveira SC de, De Castro HF, Visconti AES, Giudici R. Continuous ethanol fermentation in a tower reactor with flocculating yeast recycle: scale-up effects on process performance, kinetic parameters and model predictions [Internet]. Bioprocess Engineering. 1999 ; 20( 6): 525-530.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/s004490050624
  • Source: Bioprocess Engineering. Unidade: EP

    Subjects: FERMENTAÇÃO ALCOÓLICA, BIOTECNOLOGIA

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    • ABNT

      OLIVEIRA, S. C. et al. Continuous alcoholic fermentation process: model considering loss of cell viability. Bioprocess Engineering, v. 20, p. 157-160, 1999Tradução . . Disponível em: https://doi.org/10.1007/s004490050574. Acesso em: 08 out. 2024.
    • APA

      Oliveira, S. C., Paiva, T. C. B., Visconti, A. E. S., & Giudici, R. (1999). Continuous alcoholic fermentation process: model considering loss of cell viability. Bioprocess Engineering, 20, 157-160. doi:10.1007/s004490050574
    • NLM

      Oliveira SC, Paiva TCB, Visconti AES, Giudici R. Continuous alcoholic fermentation process: model considering loss of cell viability [Internet]. Bioprocess Engineering. 1999 ; 20 157-160.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/s004490050574
    • Vancouver

      Oliveira SC, Paiva TCB, Visconti AES, Giudici R. Continuous alcoholic fermentation process: model considering loss of cell viability [Internet]. Bioprocess Engineering. 1999 ; 20 157-160.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/s004490050574
  • Source: Bioprocess Engineering. Unidade: EP

    Subjects: PROCESSOS QUÍMICOS, CINÉTICA QUÍMICA

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    • ABNT

      RAMON-PORTUGAL, Felipe et al. Kinetic study and mathematical modelling of killer and sensitive S. Cerevisiae strains growing in mixed culture. Bioprocess Engineering, v. 17, n. 6, p. 375-381, 1997Tradução . . Disponível em: https://doi.org/10.1007/pl00008970. Acesso em: 08 out. 2024.
    • APA

      Ramon-Portugal, F., Délia-Dupuy, M. L., Pingaud, H., Carrillo Le Roux, G. A., & Riba, J. P. (1997). Kinetic study and mathematical modelling of killer and sensitive S. Cerevisiae strains growing in mixed culture. Bioprocess Engineering, 17( 6), 375-381. doi:10.1007/pl00008970
    • NLM

      Ramon-Portugal F, Délia-Dupuy ML, Pingaud H, Carrillo Le Roux GA, Riba JP. Kinetic study and mathematical modelling of killer and sensitive S. Cerevisiae strains growing in mixed culture [Internet]. Bioprocess Engineering. 1997 ; 17( 6): 375-381.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/pl00008970
    • Vancouver

      Ramon-Portugal F, Délia-Dupuy ML, Pingaud H, Carrillo Le Roux GA, Riba JP. Kinetic study and mathematical modelling of killer and sensitive S. Cerevisiae strains growing in mixed culture [Internet]. Bioprocess Engineering. 1997 ; 17( 6): 375-381.[citado 2024 out. 08 ] Available from: https://doi.org/10.1007/pl00008970

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