| 1 |
Formation of dead zone in catalytic particles in catalysis and biocatalysis-new alternative method of determination
Krol G, Szukiewicz M, Chutkowski M
Canadian Journal of Chemical Engineering, 97, 1525, 2019 |
| 2 |
Deactivation of nickel catalyst for benzene hydrogenation in an industrial bed
Szukiewicz M, Kaczmarski K, Stolecki K, Golebiowski A, Borowiecki T, Sylwestrowicz R
Przemysl Chemiczny, 88(12), 1302, 2009 |
| 3 |
Modeling the commercial catalyst bed for hydrogenation of benzene
Szukiewicz M, Kaczmarski K, Stolecki K, Szarlik S
Przemysl Chemiczny, 87(4), 384, 2008 |
| 4 |
Approximate models for diffusion with non-isothermal or multicomponent reaction in a porous pellet
Szukiewicz M
Inzynieria Chemiczna i Procesowa, 27(4), 1377, 2006 |
| 5 |
An improved approximate model for diffusion and diffusion-with-reaction processes occurring in a porous pellet
Szukiewicz M
Przemysl Chemiczny, 85(8-9), 1157, 2006 |
| 6 |
Approximate model for diffusion and reaction in a porous pellet and an effectiveness factor
Szukiewicz M, Petrus R
Chemical Engineering Science, 59(2), 479, 2004 |
| 7 |
An improved approximate model for diffusion processes with or without chemical reaction
Szukiewicz M
Inzynieria Chemiczna i Procesowa, 25(3), 1671, 2004 |
| 8 |
Testing the relative importance of mass and heat resistances in solid catalysts
Petrus R, Szukiewicz M
AIChE Journal, 49(9), 2419, 2003 |
| 9 |
Approximate models application for modelling of fixed bed reactors
Szukiewicz M
Inzynieria Chemiczna i Procesowa, 22(3E), 1363, 2001 |
| 10 |
Selective hydrogenation of an acetylene process: An example of modeling an industrial reactor process
Szukiewicz M, Petrus R
Chemical Engineering & Technology, 22(12), 1059, 1999 |
