2008
DOI: 10.1590/s0100-40422008000800004
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Biossíntese de goma xantana a partir da fermentação de soro de leite: rendimento e viscosidade

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Cited by 20 publications
(21 citation statements)
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“…A fermentação aeróbica transcorreu em agitador rotativo (Shaker Tecnal, TE-424) a 28 °C, 250 rpm por 120 h [4] . Os caldos fermentativos contendo GX foram centrifugados a 5 °C e 9625 xg (Eppendorf, 5702R) por 30 min.…”
Section: Produção E Extração Da Gxunclassified
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“…A fermentação aeróbica transcorreu em agitador rotativo (Shaker Tecnal, TE-424) a 28 °C, 250 rpm por 120 h [4] . Os caldos fermentativos contendo GX foram centrifugados a 5 °C e 9625 xg (Eppendorf, 5702R) por 30 min.…”
Section: Produção E Extração Da Gxunclassified
“…A relação C:N foi duas vezes maior no RLS quando comparado a GRB (Tabela 1). Nery et al [4] relatam 1,5:1 para soro de leite, Brandão et al [29] relatam 22:1 para caldo de cana e Brandão et al…”
Section: Composição Centesimal Dos Substratos Alternativos E Produçãounclassified
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“…The commercial fermentation media used in the production of xanthan gum contains glucose as the carbon source, and the conventional media used in research contains both this source and sucrose. If xanthan were produced commercially in Brazil as from sucrose, this source would represent a relatively small percentage of the production costs, but since the imported polymer is obtained from glucose, the cost of the carbon source represents a critical factor in the fermentation from a commercial point of view [2][3][4][5] . This reality makes it feasible to use xanthan for food and pharmaceutical ends, but not in the petroleum area, where large amounts would be required for the oil exploration process.…”
Section: Introductionmentioning
confidence: 99%