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DOI: 10.31274/rtd-180813-109
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Gas holdup in a gas-liquid-fiber semi-batch bubble column

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Cited by 1 publication
(7 citation statements)
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“…On the basis of the above analysis, the gas holdup model for this flow regime can be assumed to be where g ( C , L ) represents the terminal bubble rise velocity V 0j . It is assumed that g ( C , L ) can be described by a functional relationship involving N and N f , i.e …”
Section: Resultsmentioning
confidence: 99%
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“…On the basis of the above analysis, the gas holdup model for this flow regime can be assumed to be where g ( C , L ) represents the terminal bubble rise velocity V 0j . It is assumed that g ( C , L ) can be described by a functional relationship involving N and N f , i.e …”
Section: Resultsmentioning
confidence: 99%
“…semibatch bubble column with a perforated plate gas distributor with A = 0.49% . Su 15 showed that the models work very well provided that the coefficients are altered to account for column diameter effects; more details are provided elsewhere …”
Section: Resultsmentioning
confidence: 99%
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