The Effect of Plate Corrugations Geometry on Performance of Plate Heat Exchangers Subjected to Fouling
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00216305%3A26210%2F19%3APU135970" target="_blank" >RIV/00216305:26210/19:PU135970 - isvavai.cz</a>
Výsledek na webu
<a href="https://www.aidic.it/cet/19/76/047.pdf" target="_blank" >https://www.aidic.it/cet/19/76/047.pdf</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.3303/CET1976047" target="_blank" >10.3303/CET1976047</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
The Effect of Plate Corrugations Geometry on Performance of Plate Heat Exchangers Subjected to Fouling
Popis výsledku v původním jazyce
The novel approach of estimating the influence of plate corrugations geometry on plate heat exchanger (PHE) operation in conditions of fouling is proposed. It is based on the presented mathematical model of the PHE with commercially produced plates. To account for fouling on the heat transfer surface, the fouling model of reaction and transport type presented in dimensionless form is employed. The influence of plate corrugations geometry on PHE performance is discussed on results of modelling PHE installed for thin juice heating at evaporation station of the sugar factory. The corrugations inclination angle to the main flow direction is considered as the main influencing parameter. The effect of this parameter on fouling intensity is shown for the cases when the plates with different corrugations angle are used in one PHE. The measures to mitigate fouling in PHE by optimal selection of plate corrugations geometry are discussed.
Název v anglickém jazyce
The Effect of Plate Corrugations Geometry on Performance of Plate Heat Exchangers Subjected to Fouling
Popis výsledku anglicky
The novel approach of estimating the influence of plate corrugations geometry on plate heat exchanger (PHE) operation in conditions of fouling is proposed. It is based on the presented mathematical model of the PHE with commercially produced plates. To account for fouling on the heat transfer surface, the fouling model of reaction and transport type presented in dimensionless form is employed. The influence of plate corrugations geometry on PHE performance is discussed on results of modelling PHE installed for thin juice heating at evaporation station of the sugar factory. The corrugations inclination angle to the main flow direction is considered as the main influencing parameter. The effect of this parameter on fouling intensity is shown for the cases when the plates with different corrugations angle are used in one PHE. The measures to mitigate fouling in PHE by optimal selection of plate corrugations geometry are discussed.
Klasifikace
Druh
J<sub>SC</sub> - Článek v periodiku v databázi SCOPUS
CEP obor
—
OECD FORD obor
20402 - Chemical process engineering
Návaznosti výsledku
Projekt
<a href="/cs/project/EF15_003%2F0000456" target="_blank" >EF15_003/0000456: Laboratoř integrace procesů pro trvalou udržitelnost</a><br>
Návaznosti
P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)
Ostatní
Rok uplatnění
2019
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Chemical Engineering Transactions
ISSN
2283-9216
e-ISSN
—
Svazek periodika
neuveden
Číslo periodika v rámci svazku
76
Stát vydavatele periodika
IT - Italská republika
Počet stran výsledku
6
Strana od-do
277-282
Kód UT WoS článku
—
EID výsledku v databázi Scopus
2-s2.0-85076278452