MASS TRANSFER EFFECTS IN LIQUEFACTION OF COAL BY SRC-II PROCESS PART II STUDY OF BUBBLE COLUMN REACTORS
作者:
CHANDRAP.P. SINGH,
NORMANL. CARR,
期刊:
Chemical Engineering Communications
(Taylor Available online 1986)
卷期:
Volume 42,
issue 1-3
页码: 87-110
ISSN:0098-6445
年代: 1986
DOI:10.1080/00986448608911738
出版商: Taylor & Francis Group
关键词: Coal;Liquefaction;Mass transfer;Reactor;SRC-II;Bubble Columns
数据来源: Taylor
摘要:
The effects of hydrogen mass transfer resistance in large-scale SRC-II bubble column reactors (BCR), over large ranges of process variables, are studied. Due to the interactive effects of mass transfer resistance and gas hold up, the hydrogen consumption or liquid yield in a BCR has a maximum with respect to the specific mixing power. Under normal SRC-II process conditions a superficial gas velocity of about 0.01 m/s represents the optimum with respect to the hydrogen consumption or liquid yield. In general, the product quality requirement rather than the rate of hydrogen consumption determines the minimum specific mixing power requirement. Increase in hydrogen partial pressure can be used to reduce the level of mixing power required to maintain the desired product quality. Interrelations between mass transfer and gas hold effects and the variations in hydrogen concentration in slurry over large ranges of process conditions are also illustrated. This work provides some bases for the selection of reactor dimensions and process conditions for an SRC-II bubble column reactor (BCR).
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