Optimization criteria for a single bead-string reactor in flow injection analysis based on consecutive kinetic reactions
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Cited by (12)
Theoretical framework for mixer design for noise reduction and gradient fidelity
2021, Journal of Chromatography ACitation Excerpt :Axial mixing of a sequence of liquids along the length of a channel has not received an equal amount of attention in literature. Idealized flow injection models for simplified geometries such as single bead string reactors [10–12] and coiled tubes [13,14] have been previously described. However, their implications on the aforementioned demands on LC systems have not been discussed.
Chapter 3 Theoretical Basis of Flow Injection Analysis
2008, Comprehensive Analytical ChemistryCitation Excerpt :The model has been validated by experiments performed with an FIA system incorporating a single-bead string reactor. Van Veen et al. [148] have extended the model of Reijn et al. [147] to two consecutive (pseudo) first-order reactions (i.e., Analyte→Intermediate→Product), and have derived equations for the maxima of the RTD curves of the intermediate and the product. Rules for choosing the optimal reactor length have been formulated and experimentally confirmed using an FIA manifold with a single-bead string reactor.
Monosegmented flow-analysis of serum cholesterol
1999, FarmacoMathematical modelling of flow-injection systems
1995, Analytica Chimica ActaSimple model of flow-injection sample transport for prediction of peak heights
1992, Analytica Chimica ActaDispersion phenomena in flow-injection systems
1992, Analytica Chimica Acta