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Residence time distribution of liquids in a continuous tubular thermal processing system part I: Relating RTD to processing conditions

dc.contributor.authorTorres, A. Pinheiro
dc.contributor.authorOliveira, F. A. R.
dc.date.accessioned2011-10-21T13:50:15Z
dc.date.available2011-10-21T13:50:15Z
dc.date.issued1998
dc.description.abstractA systematic experimental study on residence time distribution (RTD) in tubular flow was performed, covering a wide range of processing conditions. The flow of water in various sections of a tubular continuous thermal processing system was analysed using the classical Danckwerts approach. Methylene blue was used as tracer and different constant temperatures (25–80 °C) and flow rates (80–380 l/ h) were tested. These conditions yielded mean residence times up to 6 min and Reynolds numbers between 1350 and 9700. Various models were fitted to the experimental data, and the dispersion model showed to yield the best fit. Peak analysis led to both accurate and precise as well as conservative parameters, when compared to other methods of parameter estimation. Results revealed that fluid dispersion in tubular flow (Peclet number) can be related to processing conditions (Reynolds number) by a power law model. Results were compared to published correlations.por
dc.identifier.citationTORRES, A. Pinheiro; OLIVEIRA, F. A. R. - Residence time distribution of liquids in a continuous tubular thermal processing system part I: Relating RTD to processing conditions. Journal of Food Engineering. ISSN 0260-8774. Vol. 35 n.º 2 (1998), p. 147-163por
dc.identifier.urihttp://hdl.handle.net/10400.14/6678
dc.language.isoengpor
dc.peerreviewedyespor
dc.publisherElsevierpor
dc.relation.publisherversionDOI 10.1016/S0260-8774(98)00008-9por
dc.titleResidence time distribution of liquids in a continuous tubular thermal processing system part I: Relating RTD to processing conditionspor
dc.typejournal article
dspace.entity.typePublication
rcaap.rightsopenAccesspor
rcaap.typearticlepor

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