The regeneration by coke combustion of a catalyst based on a SAPO-34 used in the transformation of methanol into ole®ns (ethene and propene) has been studied. It has been observed that coke combustion kinetics are strongly dependent on the nature of the coke (H/C ratio), which in turn is a consequen
Deactivation by coke of a catalyst based on a SAPO-34 in the transformation of methanol into olefins
✍ Scribed by Andrés T Aguayo; Ana E Sánchez del Campo; Ana G Gayubo; Ana Tarrío; Javier Bilbao
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 1999
- Tongue
- English
- Weight
- 207 KB
- Volume
- 74
- Category
- Article
- ISSN
- 0268-2575
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✦ Synopsis
When methanol is converted to oleüns on a SAPO-34 catalyst between 350 and 425ÄC, there is a rapid initial formation of coke, followed by a slower rate of coke deposition. The rate of coke formation decreases with increasing temperature, and with progression through the catalyst bed. The coke completely blocks the internal channels of the SAPO-34 crystals and subsequently blocks the mesopores (intercrystalline and those of the bentonite). Coke deposition mainly blocks sites of acidic strength above 175 kJ mol-1. The presence of water in the feed lessens coke formation, either by converting Lewis to sites or by competing for surface sites with coke precursors.
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