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Wyszukujesz frazę "Ciżmiński, P." wg kryterium: Autor


Wyświetlanie 1-2 z 2
Tytuł:
Prediction of coking dynamics for wet coal charge
Autorzy:
Kardaś, D.
Polesek-Karczewska, S.
Ciżmiński, P.
Stelmach, S.
Powiązania:
https://bibliotekanauki.pl/articles/185719.pdf
Data publikacji:
2015
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
pyrolysis
devolatilisation
vaporisation
internal gas pressure
piroliza
odparowanie
wewnętrzne ciśnienie gazu
Opis:
A one-dimensional transient mathematical model describing thermal and flow phenomena during coal coking in an oven chamber was studied in the paper. It also accounts for heat conduction in the ceramic oven wall when assuming a constant temperature at the heating channel side. The model was solved numerically using partly implicit methods for gas flow and heat transfer problems. The histories of temperature, gas evolution and internal pressure were presented and analysed. The theoretical predictions of temperature change in the centre plane of the coke oven were compared with industrialscale measurements. Both, the experimental data and obtained numerical results show that moisture content determines the coking process dynamics, lagging the temperature increase above the water steam evaporation temperature and in consequence the total coking time. The phenomenon of internal pressure generation in the context of overlapping effects of simultaneously occurring coal transitions – devolatilisation and coal permeability decrease under plastic stage – was also discussed.
Źródło:
Chemical and Process Engineering; 2015, 36, 3; 291-303
0208-6425
2300-1925
Pojawia się w:
Chemical and Process Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Modeling of drying and pyrolysis in a gasifier during the startup phase
Autorzy:
Ciżmiński, P.
Polesek-Karczewska, S.
Kardaś, D.
Powiązania:
https://bibliotekanauki.pl/articles/175590.pdf
Data publikacji:
2015
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
moisture
evaporation
condensation
pyrolysis
Opis:
An appropriate arrangement of particular zones in the gasifier is of practical importance for the gasification process effectiveness. One of the parameters that affects the optimum reactor operation and has to be taken into account is the speed of bed movement. The transient one-dimensional model describing the heat and mass transfer in the upper section of the biomass fixed bed gasifier that covers the zones of evaporation and pyrolysis, was introduced. To study the effect of packed bed settling resulted from the wood particles’ volume change due to their devolatilization, the simulations for various bed movement speeds were performed. The computation results indicated, as expected, on the different distribution of pyrolysis and drying zones, depending on the speed value. The clear tendency towards the reduction of pyrolysis zone, and on the other hand, towards the expansion of drying zone, with an increasing movement speed was observed.
Źródło:
Transactions of the Institute of Fluid-Flow Machinery; 2015, 128; 73-83
0079-3205
Pojawia się w:
Transactions of the Institute of Fluid-Flow Machinery
Dostawca treści:
Biblioteka Nauki
Artykuł
    Wyświetlanie 1-2 z 2

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