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Staff

dr hab. inż. Krzysztof Gosiewski

Research Group on Adsorption and Membrane Separation

Phone number: +4832 2310811 w. 126; kom. 601 546535
Email: k.gosiewski@iich.gliwice.pl
Room number: 315

Publications

  1. Mathematical simulation of WGS membrane reactor for gas from coal gasification
    Catalysis Today, doi:10.101 (2010)
  2. A study on thermal combustion of lean methane-air mixtures: Simplified reaction mechanism and kinetic equations
    Chemical Engineering Journal, 154 , 9-16 (2009)
  3. Estimation of kinetic parameters for the homogeneous oxidation of lean methane-air mixtures based on experimental temperature profiles
    Chemical and Process Engineering, 30 , 139 (2009)

  4. Prace Naukowe Instytutu Inżynierii Chemicznej Polskiej Akademii Nauk, 11 , 87 (2008)
  5. Homogeneous vs. catalytic combustion of lean methane-air gas mixtures In reverse flow reactors
    Chem. Eng. Sci., 63 (2008)
  6. Membrane reactors for syngas and hydrogen production
    CZYSTA ENERGIA Produkty chemiczne i paliwa z węgla - ocena potencjału rozwojowego, Rozdz. 5.2 , 227 - 234 (2008)

  7. Chem. Proc. Eng., 28 , 335-345 (2007)
  8. Effect of the mode of heat withdrawal on the asymmetry of temperature profiles in reverse-flow reactors. Catalytic combustion of methane as a test case
    Chem.Eng.Sci, 62 , 2679-2689 (2007)
  9. Homogeneous coal mine ventilation air methane combustion
    Polish Academy of Sciences. Annual Report, 68-69 (2007)
  10. Effective approach to cyclic steady state in the catalytic reverse-flow
    Chemical Engineering Science, 59 , 4095 ̵ (2004)
  11. Efficiency of heat recovery versus maximum catalyst temperature in a reverse-flow combustion of methane
    Chemical Engineering Journal, 107 , 19–2 (2004)
  12. Analysis of the techniques for the utilization of coal bed methane from polish coal mines
    Polityka Energetyczna, 6 , 407-422 (2003)
  13. Cyclic steady state in simulations of the catalytic reverse-flow combustion of methane
    Inżynieria Chemiczna i Procesowa, 24 , 391-409 (2003)
  14. Efficient recovery of heat from the catalytic combustion of methane in reverse-flow reactors
    Inżynieria Chemiczna i Procesowa, 23 , 397-413 (2002)
  15. Kinetics of catalytic combustion of dilute methane– air mixtures
    Inżynieria Chemiczna i Procesowa , 22 , 599-612 (2001)
  16. Simulations of non-stationary reactors for catalytic conversion of methane to synthesis gas
    Chemical Engineering Science, 56 , 1501 - 151 (2001)
  17. Mathematical simulations of reactors for catalytic conversion of methane to syngas with forced concentration cycling
    Chemical Engineering & Processing, 39 , 459-469 (2000)
  18. Effect of the intraparticle mass transport limitations on temperature profiles and catalytic performance of the Reverse-Flow Reactors for the partial oxidation of methane to synthesis gas
    Chemical Engineering Science, 54 , 4589-4602 (1999)
  19. Influence of Some Phenomena Occurring on the Surface and in Active Phase of the Vanadium Catalyst on the Reactor Dynamics
    Studies in Surface Science and Catalysis - Proceedings of the International Symposium, Antwerp, Belgium, 15-17 September 1997, 109 Editor , 511- 516 (1997)
  20. Unsteady States in Metallurgical Sulphuric Acid Plants after SO2 Concentration Drop in the Feed Gas
    Canadian Journal of Chemical Engineering , 74 , 621-625 (1996)
  21. Studies of multitubular reactors with internal heat recovery. Experiments with SO2 oxidation
    Chemical Engineering & Processing , 35 , 75-85 (1995)
  22. Dynamic Modelling of Industrial SO2 Oxidation Reactors - Part I Model of "hot" and "cold" start-ups of the plant
    Chemical Engineering & Processing , 32 , 111 ÷ 129 (1993)
  23. Dynamic modelling of industrial SO2 oxidation reactors - Part II Model of a reverse - flow reactor
    Chemical Engineering & Processing , 32 , 233 ÷ 244 (1993)
  24. A simplified design of reverse flow nonstationary reactor for low reactant concentration
    USPC-1 "Unsteady state processes in catalysis" - Proceedings of the Int. Conference , Editor:VSP , 629-636 (1990)

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