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Although the space ratefor a feed rate of coal through a full-volume reactor wasapproximately the same as that of half the flow ratethrough a half reactor, the ratio of coal to catalystvolume was significantly decreased.Interstage Vent Separator Used. The notation ¡°Vent¡±is designated as the qualitative variable (0 or 1) indicatingthe use of an interstage separator to vent gases andlow-boiling liquids from the bulk stream between thefirst and second reactors. If the separator was notoperated, all products from the first stage were feddirectly into the second stage.Catalyst Specification. The following catalysts wereused: Shell 317, Shell 324, Amoco EXP-AO-60, and acombination of AMOCAT 1A catalyst in the first stageand AMOCAT 1C in the second (designated asAmocat1a). The properties of each of the catalysts arepresented in Table 1.

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