| 摘要 |
The mixts. consisting of hydrocarbon and hydrogen were circulated in a reactor contg. granular catalysts which gradually pass through a reactor, then move to a regenerative reactor. The hydrocarbons were regenerated by a combustion, oxychlorination and final treatment. Above three treatments were carried out at 350-550 C under 1-15KG/cm2, and with oxygen content 0.01-1, 1-3 and 3-20wt.%, resp.
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