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Overview of calculation methods for determining the heat transfer coefficient for condensation of flue gas from biomass boilers in vertical tube condensers

The result's identifiers

  • Result code in IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F68407700%3A21220%2F25%3A00384127" target="_blank" >RIV/68407700:21220/25:00384127 - isvavai.cz</a>

  • Result on the web

    <a href="https://doi.org/10.1007/s00231-025-03577-1" target="_blank" >https://doi.org/10.1007/s00231-025-03577-1</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1007/s00231-025-03577-1" target="_blank" >10.1007/s00231-025-03577-1</a>

Alternative languages

  • Result language

    angličtina

  • Original language name

    Overview of calculation methods for determining the heat transfer coefficient for condensation of flue gas from biomass boilers in vertical tube condensers

  • Original language description

    The condensation of water vapor from flue gas in the energy cycles of power and heating plants is an important issue to increase the efficiency of the boiler or to separate water vapor from flue gas. A theoretical study of flue gas condensation from biomass boilers in vertical tube condensers was conducted. An overview of the methods available for determining the condensation heat transfer coefficient was compiled. Three approaches were identified to determine the heat transfer coefficient and condenser heat output according to the foundation of each method: experimental foundation (Empirical correlations), semi-theoretical foundation (Heat and mass transfer analogy, Diffusion layer model) and theoretical foundation (Boundary layer model). Empirical correlations represent the simplest way to predict the condensation heat transfer coefficient. However, the deviation of the predicted results from the experimental results is quite high, and since the equations usually lack some important driving parameters or are developed for a slightly different geometry of operating conditions, they are not reliable enough for the considered application. The Boundary layer model is very complex and impractical. Therefore, the use of the Heat and mass transfer analogy or the Diffusion layer model is the most effective for the mentioned application

  • Czech name

  • Czech description

Classification

  • Type

    J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database

  • CEP classification

  • OECD FORD branch

    20303 - Thermodynamics

Result continuities

  • Project

    <a href="/en/project/EF16_019%2F0000753" target="_blank" >EF16_019/0000753: Research centre for low-carbon energy technologies</a><br>

  • Continuities

    P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Others

  • Publication year

    2025

  • Confidentiality

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Data specific for result type

  • Name of the periodical

    Heat and Mass Transfer

  • ISSN

    0947-7411

  • e-ISSN

    1432-1181

  • Volume of the periodical

    61

  • Issue of the periodical within the volume

    7

  • Country of publishing house

    CH - SWITZERLAND

  • Number of pages

    14

  • Pages from-to

  • UT code for WoS article

    001507915900002

  • EID of the result in the Scopus database

    2-s2.0-105008003906