1988
DOI: 10.1080/00021369.1988.10869171
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Construction of a Bioreactor with Immobilized Yeast Cells for Production of a Low-phenylalanine Peptide Mixture as a Phenylketonuria Foodstuff

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Cited by 3 publications
(3 citation statements)
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“…This contrasts to the design of marine photobioreactors, which have been the subject of extensive and innovative work (for example, see Contreras et al, 1998;Hu et al, 1998;Matsunaga and Burgess, 1994). Many marine bac- (Karamanev and Nikolov, 1991) High biomass concentrations Little loss of cells through washout (Godia et al, 1987) Improved mass transfer Reduced media viscosity, increased differential velocity between media and cells (Wang et al, 1984) Advantageous partitioning effects Support can decrease inhibitory product concentration near cells (Wada et al, 1981) Increased product yield Energy is channelled away from biomass synthesis, into product synthesis (Sayles and Ollis, 1989) Increased product stability Liquid throughput reduces a product's residence time and therefore possibility of degradation (Okada et al, 1987) Integration with downstream processing Cells easily separated from media and products (Furusaki, 1988) Increased reaction selectivity Immobilization can affect membrane permeability (Watanabae et al, 1988) Flexibility in terms of fermentation protocol…”
Section: Bioreactor Considerationsmentioning
confidence: 99%
“…This contrasts to the design of marine photobioreactors, which have been the subject of extensive and innovative work (for example, see Contreras et al, 1998;Hu et al, 1998;Matsunaga and Burgess, 1994). Many marine bac- (Karamanev and Nikolov, 1991) High biomass concentrations Little loss of cells through washout (Godia et al, 1987) Improved mass transfer Reduced media viscosity, increased differential velocity between media and cells (Wang et al, 1984) Advantageous partitioning effects Support can decrease inhibitory product concentration near cells (Wada et al, 1981) Increased product yield Energy is channelled away from biomass synthesis, into product synthesis (Sayles and Ollis, 1989) Increased product stability Liquid throughput reduces a product's residence time and therefore possibility of degradation (Okada et al, 1987) Integration with downstream processing Cells easily separated from media and products (Furusaki, 1988) Increased reaction selectivity Immobilization can affect membrane permeability (Watanabae et al, 1988) Flexibility in terms of fermentation protocol…”
Section: Bioreactor Considerationsmentioning
confidence: 99%
“…A escolha do procedimento deve considerar a relação custos vs eficiência. 3,4,50,56,57,74 Se o hidrolisado protéico assim obtido ainda apresentar características organoléticas indesejáveis, recomenda-se a realização da reação de plasteína, que consiste na condensação peptídeo-peptídeo, útil para a remoção do paladar amargo e para a incorporação de tirosina e triptofano, parcialmente perdidos durante a hidrólise enzimática. [25][26][27]56,77,78 Esses dois aminoácidos, liberados juntamente com a Phe, são importantes, pois são aminoácidos essenciais.…”
Section: Hidrolisados Protéicos Com Baixo Teor De Pheunclassified
“…The different permeabilities of various substances in a complex reaction medium may be exploited in such a way that the selectivity of a particular reaction is increased. Intact cells of Rhodotorula rubra indiscriminately consumed all the constituents of an enzymic hydrolysate of a whey protein preparation, but cells entrapped in a polypyrrole membrane matrix consumed only low-molecular-weight components to give a low-phenylalanine peptide mixture in a high yield (Watanabe et al, 1988).…”
Section: The Increase In Reaction Selectivitymentioning
confidence: 99%