1 |
Effect of process parameters on optimum working conditions for catalyst carriers and packings Krajewski W, Kalinowski K Przemysl Chemiczny, 91(12), 2447, 2012 |
2 |
Kinetic model for selective oxidation of o-xylene to phthalic anhydride in terms of catalyst deactivation Krajewski W, Najzarek Z Inzynieria Chemiczna i Procesowa, 28(4), 899, 2007 |
3 |
A method for selecting metal catalyst carriers for exotherma. selective oxidation of volatile organic compounds Krajewski W, Najzarek Z Przemysl Chemiczny, 85(8-9), 1128, 2006 |
4 |
Structured catalyst carrier for selective oxidation of hydrocarbons: modelling and testing Kolodziej A, Krajewski W, Lojewska J Catalysis Today, 91-92, 59, 2004 |
5 |
Selective oxidation using structured catalysts - The way to process intensification Kolodziej A, Krajewski W Inzynieria Chemiczna i Procesowa, 25(2), 217, 2004 |
6 |
Structured metal catalysts - A way to intensify chemical processes Kolodziej A, Lojewska J, Krajewski W Inzynieria Chemiczna i Procesowa, 25(3), 1121, 2004 |
7 |
Evaluation of the efficiency of heat transfer intensification by use of entropic criterion Krajewski W, Kolodziej A Inzynieria Chemiczna i Procesowa, 25(3), 1189, 2004 |
8 |
Intensification of industrial processes by combinatorial techniques of heterogeneous catalysis Krajewski W, Najzarek Z Przemysl Chemiczny, 82(8-9), 728, 2003 |
9 |
Possibilities of selective oxidation of hydrocarbons on structured carrier-supported catalysts Krajewski W, Kolodiej A, Dubis A Przemysl Chemiczny, 82(8-9), 1218, 2003 |
10 |
Analytic stability margin design for unstable and nomninimum-phase plants Ferrante A, Krajewski W, Lepschy A, Viaro U IEEE Transactions on Automatic Control, 47(12), 2117, 2002 |