Development of a kinetic model for light alkane aromatisation over zeolite catalysts

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Mục lục

R Universal gas constant
X1’ Mass fractional conversion over a real catalyst with HT activity
X2’ Mass fractional conversion over a pseudo-catalyst without HT activity
yi Mole fraction of component i in the feed (moli molF-1)
Z Zeolite acid site
( Fraction of non-deactivated zeolite acid sites (nTOTAL n0-1)
- Subscripts
- Abbreviations
  - CONCEN Subfunctions to describe the transformation rates of hydrocarbons and
  - hydrogen involved in the reaction
  - SEM Scanning electron microscopy
    - SBR Styrene-butadiene rubber
    - STP Standard temperature and pressure
      - TEM Transmission electron microscopy
      - TOS Time-on-stream
        TPR Temperature-programmed reduction
        XAS X-ray absorption spectroscopy
        XPS X-ray photoelectron spectroscopy
        2.8. COKING IN THE AROMATISATION OF LIGHT ALKANES
        DB Lukyanov, LH Nguyen, T Vazhnova, and ST Kolaczkowski

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