β Scribed by Niels Bech; Morten Boberg Larsen; Peter Arendt Jensen; Kim Dam-Johansen
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
A fluidized bed reactor was used to study the production of gases from the thermal and catalytic pyrolysis of high-density polyethylene (HDPE). The effect of the bed temperature and type of catalyst was evaluated. The range of operating temperature was from 400 to 800 8C. The catalysts used in this
Isobutane pyrolysis is studied in an unpacked Pyrex reactor at 20-100 torr initial pressures and Results are interpreted in terms of a long chain radical mechanism 750-793 K. and the reaction is modeled. The reaction selectivity or ratio of the initial production rate of isobutene (or hydrogen) to t
Isobutane pyrolysis has been studied in the presence of oxygen at about in 773 K unpacked and in PbO-coated packed Pyrex reactors. The reaction is shown to be accelerated by oxygen in reactors of low surface-to-volume ratio and strongly inhibited in packed PbOcoated reactors. These oxygen effects ar