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In addition, the channel system of SSZ-35 prevents the formation of coke precursors.
Hydrogen and syngas formation was observed and quantified under the current conditions without significant formation of coke in the reactor.
The formation of coke occurs via chemical kinetic pathways that are largely dependent on poly aromatic hydrocarbons (PAHs).
The formation of coke during the steam reforming of light hydrocarbons results mainly from catalytic reactions.
The formation of coke, also favoured under these conditions, is a major problem.
High coke yield, low aromatic yields, and low oxygenate yields were observed with large pore zeolites, suggesting that the large pores facilitate the formation of coke.
The reduced chromia/zirconia catalysts were active in the dehydrogenation of isobutane but deactivated due to formation of coke.
The primary reaction competing with aromatic hydrocarbon production was the formation of coke which was negligible even at low catalytic temperatures.
This coupling of transport and reaction would enhance the formation of coke by increasing the rate of recombination reactions.
The occurrence of swelling, disruptive boiling, splashing and the formation of coke were clearly identified by three characteristic combustion times.
Platinum improved catalyst stability by preventing formation of coke precursors on strong acid site of sulfated zirconium.
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