Source: Process Biochemistry. Unidade: FCF
Subjects: BIOQUÍMICA, CANDIDA, FERMENTAÇÃO
A citação é gerada automaticamente e pode não estar totalmente de acordo com as normas
ABNT
SILVA, Silvio Silvério da et al. Use of a fluidized bed reactor operated in semi-continuous mode for xylose-to-xylitol conversion by Candida guilliermondii immobilized on porous glass. Process Biochemistry, v. 38, n. 6, p. 903-907, 2003Tradução . . Disponível em: https://doi.org/10.1016/s0032-9592(02)00177-2. Acesso em: 12 nov. 2024.APA
Silva, S. S. da, Santos, J. C., Carvalho, W., Aracava, K. K., & Vitolo, M. (2003). Use of a fluidized bed reactor operated in semi-continuous mode for xylose-to-xylitol conversion by Candida guilliermondii immobilized on porous glass. Process Biochemistry, 38( 6), 903-907. doi:10.1016/s0032-9592(02)00177-2NLM
Silva SS da, Santos JC, Carvalho W, Aracava KK, Vitolo M. Use of a fluidized bed reactor operated in semi-continuous mode for xylose-to-xylitol conversion by Candida guilliermondii immobilized on porous glass [Internet]. Process Biochemistry. 2003 ; 38( 6): 903-907.[citado 2024 nov. 12 ] Available from: https://doi.org/10.1016/s0032-9592(02)00177-2Vancouver
Silva SS da, Santos JC, Carvalho W, Aracava KK, Vitolo M. Use of a fluidized bed reactor operated in semi-continuous mode for xylose-to-xylitol conversion by Candida guilliermondii immobilized on porous glass [Internet]. Process Biochemistry. 2003 ; 38( 6): 903-907.[citado 2024 nov. 12 ] Available from: https://doi.org/10.1016/s0032-9592(02)00177-2