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Artigo de periodico
An original procedure for physical simulation of upflow anaerobic sludge lanket reactors (2000)
Pires, Eduardo Cleto ; Hanisch, Werner Siegfried; Andrade, Marcio Antonio Nogueira
Source: Bioprocess Engineering. Unidade: EESC
Subjects: LODO DE ESGOTO, REATORES ANAERÓBIOS, ENGENHARIA HIDRÁULICA
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
ABNT
PIRES, Eduardo Cleto e HANISCH, Werner Siegfried e ANDRADE, Marcio Antonio Nogueira. An original procedure for physical simulation of upflow anaerobic sludge lanket reactors. Bioprocess Engineering, n. 23, p. 389-395, 2000Tradução . . Disponível em: https://doi.org/10.1007/s004499900180. Acesso em: 10 jun. 2024.
APA
Pires, E. C., Hanisch, W. S., & Andrade, M. A. N. (2000). An original procedure for physical simulation of upflow anaerobic sludge lanket reactors. Bioprocess Engineering, ( 23), 389-395. doi:10.1007/s004499900180
NLM
Pires EC, Hanisch WS, Andrade MAN. An original procedure for physical simulation of upflow anaerobic sludge lanket reactors [Internet]. Bioprocess Engineering. 2000 ;( 23): 389-395.[citado 2024 jun. 10 ] Available from: https://doi.org/10.1007/s004499900180
Vancouver
Pires EC, Hanisch WS, Andrade MAN. An original procedure for physical simulation of upflow anaerobic sludge lanket reactors [Internet]. Bioprocess Engineering. 2000 ;( 23): 389-395.[citado 2024 jun. 10 ] Available from: https://doi.org/10.1007/s004499900180
Artigo de periodico
Scale-up effects on kinetic parameters and on predictions of a yeast recycle continuous ethanol fermentation model incorporating loss of cell viability (2000)
Oliveira, Samuel Conceição de ; Castro, Heizir Ferreira de ; Visconti, Alexandre Eliseu Stourdze ; Giudici, Reinaldo
Source: Bioprocess Engineering. Unidade: EP
Subjects: PROCESSOS QUÍMICOS, FERMENTAÇÃO ALCOÓLICA
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
ABNT
OLIVEIRA, Samuel Conceição de et al. Scale-up effects on kinetic parameters and on predictions of a yeast recycle continuous ethanol fermentation model incorporating loss of cell viability. Bioprocess Engineering, v. 23, n. 1, p. 51-55, 2000Tradução . . Disponível em: https://doi.org/10.1007/s004499900120. Acesso em: 10 jun. 2024.
APA
Oliveira, S. C. de, Castro, H. F. de, Visconti, A. E. S., & Giudici, R. (2000). Scale-up effects on kinetic parameters and on predictions of a yeast recycle continuous ethanol fermentation model incorporating loss of cell viability. Bioprocess Engineering, 23( 1), 51-55. doi:10.1007/s004499900120
NLM
Oliveira SC de, Castro HF de, Visconti AES, Giudici R. Scale-up effects on kinetic parameters and on predictions of a yeast recycle continuous ethanol fermentation model incorporating loss of cell viability [Internet]. Bioprocess Engineering. 2000 ; 23( 1): 51-55.[citado 2024 jun. 10 ] Available from: https://doi.org/10.1007/s004499900120
Vancouver
Oliveira SC de, Castro HF de, Visconti AES, Giudici R. Scale-up effects on kinetic parameters and on predictions of a yeast recycle continuous ethanol fermentation model incorporating loss of cell viability [Internet]. Bioprocess Engineering. 2000 ; 23( 1): 51-55.[citado 2024 jun. 10 ] Available from: https://doi.org/10.1007/s004499900120
Artigo de periodico
General relationship for volumetric oxygen transfer coefficient - ('K IND.L A') prediction in tower bioreactors utilizing immobilezed cells (2000)
Barboza, M.; Zaiat, Marcelo; Hokka, C. O.
Source: Bioprocess Engineering. Unidade: EESC
Assunto: BIOTECNOLOGIA
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ABNT
BARBOZA, M. e ZAIAT, Marcelo e HOKKA, C. O. General relationship for volumetric oxygen transfer coefficient - ('K IND.L A') prediction in tower bioreactors utilizing immobilezed cells. Bioprocess Engineering, v. 22, p. 181-184, 2000Tradução . . Disponível em: https://repositorio.usp.br/directbitstream/c75b7d7e-6855-41fa-81c7-7d7db2ed6f97/PROD_000628_SYSNO_1195540.pdf. Acesso em: 10 jun. 2024.
APA
Barboza, M., Zaiat, M., & Hokka, C. O. (2000). General relationship for volumetric oxygen transfer coefficient - ('K IND.L A') prediction in tower bioreactors utilizing immobilezed cells. Bioprocess Engineering, 22, 181-184. Recuperado de https://repositorio.usp.br/directbitstream/c75b7d7e-6855-41fa-81c7-7d7db2ed6f97/PROD_000628_SYSNO_1195540.pdf
NLM
Barboza M, Zaiat M, Hokka CO. General relationship for volumetric oxygen transfer coefficient - ('K IND.L A') prediction in tower bioreactors utilizing immobilezed cells [Internet]. Bioprocess Engineering. 2000 ; 22 181-184.[citado 2024 jun. 10 ] Available from: https://repositorio.usp.br/directbitstream/c75b7d7e-6855-41fa-81c7-7d7db2ed6f97/PROD_000628_SYSNO_1195540.pdf
Vancouver
Barboza M, Zaiat M, Hokka CO. General relationship for volumetric oxygen transfer coefficient - ('K IND.L A') prediction in tower bioreactors utilizing immobilezed cells [Internet]. Bioprocess Engineering. 2000 ; 22 181-184.[citado 2024 jun. 10 ] Available from: https://repositorio.usp.br/directbitstream/c75b7d7e-6855-41fa-81c7-7d7db2ed6f97/PROD_000628_SYSNO_1195540.pdf
Artigo de periodico
Determination of power consumption and volumetric oxygen transfer coefficient in bioreactors (2000)
Vilaça, Patrícia Ribeiro; Badino Junior, Alberto Colli; Facciotti, Maria Cândida Reginato; Schmidell Netto, Willibaldo
Source: Bioprocess Engineering. Unidade: EP
Subjects: BIOTECNOLOGIA, FERMENTAÇÃO
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
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: 10 jun. 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 jun. 10 ] 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 jun. 10 ] Available from: https://doi.org/10.1007/s004490050730
Artigo de periodico
Continuous ethanol fermentation in a tower reactor with flocculating yeast recycle: scale-up effects on process performance, kinetic parameters and model predictions (1999)
Oliveira, Samuel Conceição de ; De Castro, H. F.; Visconti, Alexandre Eliseu Stourdze ; Giudici, Reinaldo
Source: Bioprocess Engineering. Unidade: EP
Subjects: FERMENTAÇÃO ALCOÓLICA, REATORES QUÍMICOS
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
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: 10 jun. 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 jun. 10 ] 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 jun. 10 ] Available from: https://doi.org/10.1007/s004490050624
Artigo de periodico
Continuous alcoholic fermentation process: model considering loss of cell viability (1999)
Oliveira, S. C.; Paiva, T. C. B.; Visconti, A. E. S.; Giudici, Reinaldo
Source: Bioprocess Engineering. Unidade: EP
Subjects: FERMENTAÇÃO ALCOÓLICA, BIOTECNOLOGIA
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
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: 10 jun. 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 jun. 10 ] 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 jun. 10 ] Available from: https://doi.org/10.1007/s004490050574
Artigo de periodico
Influence of the tracer characteristics on hydrodynamic models packed-bed bioreactors (1999)
De Nardi, I. R.; Zaiat, Marcelo; Foresti, Eugênio
Source: Bioprocess Engineering. Unidade: EESC
Assunto: TRATAMENTO DE ÁGUAS RESIDUÁRIAS
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
ABNT
DE NARDI, I. R. e ZAIAT, Marcelo e FORESTI, Eugênio. Influence of the tracer characteristics on hydrodynamic models packed-bed bioreactors. Bioprocess Engineering, v. 2, p. 469-476, 1999Tradução . . Disponível em: https://doi.org/10.1007/s004490050704. Acesso em: 10 jun. 2024.
APA
De Nardi, I. R., Zaiat, M., & Foresti, E. (1999). Influence of the tracer characteristics on hydrodynamic models packed-bed bioreactors. Bioprocess Engineering, 2, 469-476. doi:10.1007/s004490050704
NLM
De Nardi IR, Zaiat M, Foresti E. Influence of the tracer characteristics on hydrodynamic models packed-bed bioreactors [Internet]. Bioprocess Engineering. 1999 ; 2 469-476.[citado 2024 jun. 10 ] Available from: https://doi.org/10.1007/s004490050704
Vancouver
De Nardi IR, Zaiat M, Foresti E. Influence of the tracer characteristics on hydrodynamic models packed-bed bioreactors [Internet]. Bioprocess Engineering. 1999 ; 2 469-476.[citado 2024 jun. 10 ] Available from: https://doi.org/10.1007/s004490050704
Artigo de periodico
Kinetic study and mathematical modelling of killer and sensitive S. Cerevisiae strains growing in mixed culture (1997)
Ramon-Portugal, Felipe; Délia-Dupuy, M. L.; Pingaud, Herve; Carrillo Le Roux, Galo Antonio ; Riba, Jean Pierre
Source: Bioprocess Engineering. Unidade: EP
Subjects: PROCESSOS QUÍMICOS, CINÉTICA QUÍMICA
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
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: 10 jun. 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 jun. 10 ] 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 jun. 10 ] Available from: https://doi.org/10.1007/pl00008970

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