Number of the records: 1  

Modelling of Binary Nucleation in Laminar Co-Flow Tube.

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    SYSNO ASEP0508932
    Document TypeC - Proceedings Paper (int. conf.)
    R&D Document TypeThe record was not marked in the RIV
    TitleModelling 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, SAI
    Source TitleConference Guide. - Florence : Italian Association of Chemical Engineering, 2019 - ISBN N
    Number of pages2 s.
    Publication formOnline - E
    ActionEuropean Congress of Chemical Enginewering /12./
    Event date15.09.2019 - 19.09.2019
    VEvent locationFlorence
    CountryIT - Italy
    Event typeEUR
    Languageeng - English
    CountryIT - Italy
    Keywordsmathematical modeling ; laminar co-flow tube ; partial pressure profiles
    Subject RIVCI - Industrial Chemistry, Chemical Engineering
    OECD categoryChemical process engineering
    Subject RIV - cooperationInstitute of Thermomechanics - Thermodynamics
    R&D ProjectsGA17-19798S GA ČR - Czech Science Foundation (CSF)
    Institutional supportUCHP-M - RVO:67985858 ; UT-L - RVO:61388998
    AnnotationParticle 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.
    WorkplaceInstitute of Chemical Process Fundamentals
    ContactEva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227
    Year of Publishing2020
Number of the records: 1  

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