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
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Czech description
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Classification
Type
J<sub>imp</sub> - Article in a specialist periodical, which is included in the Web of Science database
CEP classification
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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
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UT code for WoS article
001507915900002
EID of the result in the Scopus database
2-s2.0-105008003906