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Mass-transport characteristics of zeolite cracking catalysts. Final report

Technical Report ·
OSTI ID:6537860

Three series of experiments were undertaken in this investigation. In the first study we attempted to measure the intracrystalline diffusivities of a variety of alkanes and naphthenic hydrocarbons in zeolite NaY by the gas chromatography technique. The results were only partially successful. In the second investigation mixtures of two-, three-, and four-ring (naphthalene, phenanthrene, and pyrene) structures were hydrocracked over a nickel-tungsten sulfide ultrastable zeolite Y catalyst. The catalyst was very active in hydrocracking all three structures. At 371/sup 0/C and 10,440 kPa the pseudo first order rate constants (gm/hr/gm) for hydrocracking the two-, three- and four-ring mixtures were 14/6.2/2.8 respectively. In the third experimental investigation three molecular species (n-heptane, decalin, and 1-methyldecalin) of varying critical diameter were cracked over several acid faujasites (LaNaY, LaHY, MgHY, USY) of varying catalytic activity. For comparison purposes the hydrocarbons were also cracked over an amorphous silica-alumina catalyst. The experiments were carried out in a flow reactor in the presence of inert carrier (helium) at near atmospheric pressure and consequently the conditions more nearly approximate catalytic cracking conditions in contrast to the catalytic hydrocracking study described above. The naphthenic hydrocarbons were chosen for this study because it was demonstrated during preliminary work that the cracking kinetics was first order. Detailed reports of the three experiments are included in this final report.

Research Organization:
Mississippi Univ., University (USA). Dept. of Chemical Engineering
DOE Contract Number:
AC22-77ET10651
OSTI ID:
6537860
Report Number(s):
DOE/ET/10651-1; FE-0651-1; ON: DE83003995
Country of Publication:
United States
Language:
English

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