FIELD: carbon materials.
SUBSTANCE: powderlike catalyst is continuously fed into tubular reactor and displaced along reactor axis. Following composition of catalyst can be used: 70-90% Ni and 10-30% MgO or 40-60% Co and 40-60% Al2O3, or Mo, Co, and Mg at molar ratio 1:5:94, respectively. Process is carried out continuously at countercurrent catalyst-hydrocarbon contact. In the first zone(s) catalyst is activated by gases leaving hydrocarbon pyrolysis at 450-600°C. Residence time of catalyst ranges from 5 to 180 min. Activated catalyst is passed into pyrolysis zone(s) at 550-1000°C. Into the same zone(s), hydrocarbons, e.g. methane, are countercurrently passed. Residence time of catalyst in pyrolysis zone(s) ranges from 0.5 to 180 min. Invention can be used in sorbent, catalyst, and composite manufacturing processes.
EFFECT: enabled continuous manufacture of layered nanotubes or bent hollows fibers, reduced number of stages and consumption of reagents.
4 cl, 2 dwg, 7 ex
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Authors
Dates
2005-08-10—Published
2004-02-10—Filed