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Modelling the Transport of Metalaxyl in Gerbera Plants grown in a Closed-loop Hydroponic System

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dc.contributor.author Karras, G en
dc.contributor.author Savvas, D en
dc.contributor.author Patakioutas, G en
dc.contributor.author Pomonis, T en
dc.contributor.author Albanis, T en
dc.contributor.author Pomonis, P en
dc.date.accessioned 2014-06-06T06:47:53Z
dc.date.available 2014-06-06T06:47:53Z
dc.date.issued 2007 en
dc.identifier.issn 15375110 en
dc.identifier.uri http://dx.doi.org/10.1016/j.biosystemseng.2006.10.007 en
dc.identifier.uri http://62.217.125.90/xmlui/handle/123456789/3841
dc.subject.other Computer simulation en
dc.subject.other Concentration (process) en
dc.subject.other Fungicides en
dc.subject.other Nutrition en
dc.subject.other Rate constants en
dc.subject.other Transport properties en
dc.subject.other Closed hydroponic systems en
dc.subject.other Drainage water en
dc.subject.other Gerbera plants en
dc.subject.other Reactor systems en
dc.subject.other Plants (botany) en
dc.subject.other Gerbera en
dc.subject.other Gerbera jamesonii en
dc.title Modelling the Transport of Metalaxyl in Gerbera Plants grown in a Closed-loop Hydroponic System en
heal.type journalArticle en
heal.identifier.primary 10.1016/j.biosystemseng.2006.10.007 en
heal.publicationDate 2007 en
heal.abstract The transport and the kinetics of the fungicide metalaxyl were followed in various parts of gerbera plants (Gerbera jamesonii) grown in a closed hydroponic system. The pesticide was applied into the nutrient solution and supplied to the plants in the mode of a pulse at two concentrations, 112·5 and 225 mg l-1. Its fate was then followed regularly for a period of 121 days, by collecting and analysing samples of irrigation solution, drainage water, roots, leaves and flowers of the plants by means of gas chromatography. The dimensionless parameter D/uL, where D is the diffusion coefficient, u is the linear velocity and L is the length of flow, for the movement of the tracer metalaxyl in the whole plant was found to be about 0·15-0·30 for both concentration treatments. These relatively high values support the statement that the plant operates as a well mixed reactor system. Next, the variation of analytical data in the solution, the roots, the leaves, and flowers were simulated using a model of four reactor vessels connected in series. From the results, it was possible to estimate the values for the apparent rate constant kapp of elimination in each compartment. The values for kapp appear similar for both treatments, but differ strongly in the various parts of the plants as follows: kleaves>kflowers>kroots. These variations of the apparent rate constants in the different parts of the plant are explained based on differences in the mode of long-distance transport to each of them. © 2006 IAgrE. en
heal.journalName Biosystems Engineering en
dc.identifier.issue 2 en
dc.identifier.volume 96 en
dc.identifier.doi 10.1016/j.biosystemseng.2006.10.007 en
dc.identifier.spage 279 en
dc.identifier.epage 292 en


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