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Modelling of Binary Nucleation in Laminar Co-Flow Tube.
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SYSNO ASEP 0508932 Document Type C - Proceedings Paper (int. conf.) R&D Document Type The record was not marked in the RIV Title Modelling of Binary Nucleation in Laminar Co-Flow Tube. Author(s) Trávníčková, Tereza (UCHP-M) RID, ORCID, SAI
Havlica, Jaromír (UCHP-M) RID, ORCID, SAI
Hrubý, Jan (UT-L) RID, ORCID
Ždímal, Vladimír (UCHP-M) RID, ORCID, SAISource Title Conference Guide. - Florence : Italian Association of Chemical Engineering, 2019 - ISBN N Number of pages 2 s. Publication form Online - E Action European Congress of Chemical Enginewering /12./ Event date 15.09.2019 - 19.09.2019 VEvent location Florence Country IT - Italy Event type EUR Language eng - English Country IT - Italy Keywords mathematical modeling ; laminar co-flow tube ; partial pressure profiles Subject RIV CI - Industrial Chemistry, Chemical Engineering OECD category Chemical process engineering Subject RIV - cooperation Institute of Thermomechanics - Thermodynamics R&D Projects GA17-19798S GA ČR - Czech Science Foundation (CSF) Institutional support UCHP-M - RVO:67985858 ; UT-L - RVO:61388998 Annotation Particle nucleation is one of the important phenomena encountered in both chemical engineering and environmental studies. The Laminar Co-Flow Tube (LCFT) was designed for experimental measurement of binary and ternary nucleation of mixtures of atmospheric aerosols at laboratory conditions, most often H2SO4 + H2O + amines (MEA, TEA)/terpenes (α-pinene, limonene). When nucleating components are entrained co-currently with H2S04 in the axial flow, a clearly defined nucleation zone can be formed in the axial region of the chamber. As a result, the losses of the formed particles on the device walls are minimized. Laminar flow allows mathematical modeling of velocity and partial pressure profiles in the chamber. From these, it is then possible to predict the shape and size of the nucleation zone and subsequently the nucleation rate. Two models were used for mathematical modeling of momentum and mass transfer in the LFDC. 2D axisymmetric CFD model and simplified 1D analytical model. A parametric study was carried out using both models and the influence of the individual simplifications of analytical model on overall behavior of the system was discussed.
Workplace Institute of Chemical Process Fundamentals Contact Eva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227 Year of Publishing 2020
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