1990
DOI: 10.3168/jds.s0022-0302(90)78708-5
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Rheological Characterization of Dulce de Leche, a Confectionery Dairy Product

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Cited by 19 publications
(15 citation statements)
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“…In dulce de leche industrial production, the presence of the exhauster is mandatory, primarily becau se it increases the evaporation rate, consistent with the present results. Simulations of the evaporation process should investigate the exhaust system or pressure reduction (vacuum evaporation), as demonstrated by Silva et al (2015), Silveira et al (2013), Rovedo et al (1991), Martinez et al (1990), andPauletti et al (1990). Silveira et al (2015) compared the efficacy of a pilot scale single stage evaporator in the evaporation of water and skim milk.…”
Section: Resultsmentioning
confidence: 99%
“…In dulce de leche industrial production, the presence of the exhauster is mandatory, primarily becau se it increases the evaporation rate, consistent with the present results. Simulations of the evaporation process should investigate the exhaust system or pressure reduction (vacuum evaporation), as demonstrated by Silva et al (2015), Silveira et al (2013), Rovedo et al (1991), Martinez et al (1990), andPauletti et al (1990). Silveira et al (2015) compared the efficacy of a pilot scale single stage evaporator in the evaporation of water and skim milk.…”
Section: Resultsmentioning
confidence: 99%
“…pueden utilizar como fuente de carbono y energía para producir biomasa [8]. Utilizando K. fragilis se puede obtener biomasa siguiendo el procedimiento descrito por Pauletti et al [61] o el recomendado por [5]. Con [60] dan a conocer la metodología para obtener biomasa a partir de K. marxianus var.…”
Section: Biomasaunclassified
“…En cuanto a su textura, el dulce de leche se caracteriza por ser un fluido no newtoniano de carácter pseudoplástico, cuya consistencia está en función de los grados Brix que posee (Pauletti et al 1990). Se ha observado que su viscosidad se ve afectada principalmente por el contenido de sólidos solubles, la acidez de la mezcla inicial y el porcentaje de sacarosa, explicando estas tres variables el 73-85% de las variaciones en la viscosidad final (Casals y de Hombre 1995).…”
Section: Introductionunclassified