Process intensification in a model trickle-bed reactor

Industrial and Engineering Chemistry Research

Volumn 41, Issue 13, 2002, Pages 3139-3144

  Sivalingam, G ^a   Radhika, M ^a   Rao, D P ^a   Rao, M S ^a  

^a INDIAN INSTITUTE OF TECHNOLOGY KANPUR   (India)

Author keywords

[No Author keywords available]

Indexed keywords

ACCELERATION; CENTRIFUGATION; FLOW CONTROL; INTERFACES (MATERIALS); PACKED BEDS; PROCESS ENGINEERING; RATE CONSTANTS; ROTATION;

TRICKLE-BED REACTORS;

CHEMICAL REACTIONS;

INTENSIFIER; MODEL; TRICKLE BED REACTOR;

ACCELERATION; ARTICLE; GRAVITY; MODEL; REACTION ANALYSIS; REACTOR;

EID: 0037178102     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0107237     Document Type: Article

References (12)

1. Trickle-bed reactors: State of art and perspectives
2. Mass transfer in rotating packed bed - I. Development of gas-liquid and liquid-solid mass-transfer correlations
3. Liquid holdup in rotating packed beds: Examination of film flow assumption
4. Characteristics of a rotating packed bed
5. Mass transfer limitation in a trickle bed reactor
6. Experimental study of reaction in a partially wetted catalytic pellet
7. Effectiveness factors and mass transfer in trickle-bed reactors
8. A model for sulphur dioxide oxidation in trickle-bed reactors
9. Oxidation of sulfur dioxide in a trickle-bed reactor