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


Wyświetlanie 1-5 z 5
Tytuł:
Statistical Analysis of Emotions and Opinions at Digg Website
Autorzy:
Pohorecki, P.
Sienkiewicz, J.
Mitrović, M.
Paltoglou, G.
Hołyst, J.
Powiązania:
https://bibliotekanauki.pl/articles/1400182.pdf
Data publikacji:
2013-03
Wydawca:
Polska Akademia Nauk. Instytut Fizyki PAN
Tematy:
02.50.-r
07.05.Hd
89.20.Hh
89.70.Cf
Opis:
We performed statistical analysis on data from the Digg.com website, which enables its users to express their opinion on news stories by taking part in forum-like discussions as well as to directly evaluate previous posts and stories by assigning so called "diggs". Owing to fact that the content of each post has been annotated with its emotional value, apart from the strictly structural properties, the study also includes an analysis of the average emotional response of the comments about the main story. While analysing correlations at the story level, an interesting relationship between the number of diggs and the number of comments that a story received was found. The correlation between the two quantities is high for data where small threads dominate and consistently decreases for longer threads. However, while the correlation of the number of diggs and the average emotional response tends to grow for longer threads, correlations between numbers of comments and the average emotional response are almost zero. We also suggest presence of two different mechanisms governing the evolution of the discussion and, consequently, its length.
Źródło:
Acta Physica Polonica A; 2013, 123, 3; 604-615
0587-4246
1898-794X
Pojawia się w:
Acta Physica Polonica A
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Pressure drop in two-phase gas-liquid (Taylor) flow in microreactors
Autorzy:
Cygański, P.
Sobieszuk, P.
Pohorecki, R.
Powiązania:
https://bibliotekanauki.pl/articles/185780.pdf
Data publikacji:
2012
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
przepływ Taylora
przepływ gaz-ciecz
spadek ciśnienia
mikroreaktor
gas-liquid Taylor flow
microreactor
pressure drop
Opis:
The pressure drop in microreactors for the gas - liquid Taylor flow was measured for 4 different microreactor geometries and 3 different gas - liquid systems. The results have been compared with the existing literature correlations. A selection of the best correlations has been made.
Źródło:
Chemical and Process Engineering; 2012, 33, 3; 369-384
0208-6425
2300-1925
Pojawia się w:
Chemical and Process Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Correction methods for pulsed neutron source reactivity measurement in accelerator driven systems
Autorzy:
Gajda, P.
Janczyszyn, J.
Pohorecki, W.
Powiązania:
https://bibliotekanauki.pl/articles/148199.pdf
Data publikacji:
2013
Wydawca:
Instytut Chemii i Techniki Jądrowej
Tematy:
accelerator driven systems (ADS)
EUROTRANS
measurement
reactivity
YALINA
Opis:
Important issue in the perspective of nuclear energy development in the near future is the partitioning and transmutation (P&T) of spent nuclear fuel. For years the European Commission (EC) has sponsored this scientific activity through the Framework Programmes (FP). One of the milestones for P&T is the development of accelerator driven systems (ADS). Extensive research in this field was carried out within the EUROTRANS project of 6th FP of EURATOM. Part of this research was devoted to testing and development of reactivity monitoring techniques in ADS. This paper concerns the methods of the reactivity measurement using the pulsed neutron source (PNS). Due to the fact that basic methods devoted to determine the core reactivity are derived from point kinetics, while real subcritical core kinetics differs from this model, there is a need to improve these methods in order to deal with the observed spatial effects. There are several ways to make these methods work properly and finally it should be possible to achieve this. However, they still need a validation which is supposed to be done within next FP project FREYA.
Źródło:
Nukleonika; 2013, 58, 2; 287-293
0029-5922
1508-5791
Pojawia się w:
Nukleonika
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Carbon dioxide absorption into aqueous blends of N-methyldiethanolamine and 2-ethylaminoethanol
Autorzy:
Moniuk, W.
Pohorecki, R.
Machniewski, P.
Powiązania:
https://bibliotekanauki.pl/articles/184865.pdf
Data publikacji:
2012
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
alkanoloamines
carbon dioxide
absorption
simulation
packed column
alkanoloaminy
dwutlenek węgla
absorpcja
symulacja
kolumna z wypełnieniem
Opis:
Measurements of the absorption rate of carbon dioxide into aqueous solutions of N-methyldiethanoloamine (MDEA) and 2-ethylaminoethanol (EAE) have been carried out. On this basis a mathematical model of the performance of an absorption column operated with aqueous solution of a blend of the above amines at elevated temperatures and pressures have been proposed. The results of simulations obtained by means of this model are described. The work is a part of a wider program, aimed at the development of a new process.
Źródło:
Chemical and Process Engineering; 2012, 33, 4; 547-561
0208-6425
2300-1925
Pojawia się w:
Chemical and Process Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
Tytuł:
Contribution of liquid-and gas-side mass transfer coefficients to overall mass transfer coefficient in Taylor flow in a microreactor
Autorzy:
Sobieszuk, P.
Ilnicki, F.
Pohorecki, R.
Powiązania:
https://bibliotekanauki.pl/articles/185639.pdf
Data publikacji:
2014
Wydawca:
Polska Akademia Nauk. Czytelnia Czasopism PAN
Tematy:
Taylor flow
mass transfer coefficients
microreactor
CFD simulations
przepływ Taylora
współczynnik przenikania masy
mikroreaktor
symulacje CFD
Opis:
Gas-liquid microreactors find an increasing range of applications both in production, and for chemical analysis. The most often employed flow regime in these microreactors is Taylor flow. The rate of absorption of gases in liquids depends on gas-side and liquid-side resistances. There are several publications about liquid-side mass transfer coefficients in Taylor flow, but the data about gas-side mass transfer coefficients are practically non existent. We analysed the problem of gas-side mass transfer resistance in Taylor flow and determined conditions, in which it may influence the overall mass transfer rate. Investigations were performed using numerical simulations. The influence of the gas diffusivity, gas viscosity, channel diameter, bubble length and gas bubble velocity has been determined. It was found that in some case the mass transfer resistances in both phases are comparable and the gas-side resistance may be significant. In such cases, neglecting the gas-side coefficient may lead to errors in the experimental data interpretation.
Źródło:
Chemical and Process Engineering; 2014, 35, 1; 35-45
0208-6425
2300-1925
Pojawia się w:
Chemical and Process Engineering
Dostawca treści:
Biblioteka Nauki
Artykuł
    Wyświetlanie 1-5 z 5

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