Liquid-continuous distillation

Industrial and Engineering Chemistry Research

Volumn 47, Issue 12, 2008, Pages 4290-4294

  Seibert, A Frank ^a   Lewis, J Christopher ^a   Fair, James R ^a  

^a UNIVERSITY OF TEXAS AT AUSTIN   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

AMERICAN CHEMICAL SOCIETY (ACS); CONTINUOUS DISTILLATION; CONTINUOUS OPERATIONS; GAS RATES; OPERATING CONDITIONS; SIEVE TRAYS; STRUCTURED PACKINGS; SUPERFICIAL GAS VELOCITIES;

BUBBLE COLUMNS; COLUMNS (STRUCTURAL); DISTILLATION; GASES; LEAD;

DISTILLATION COLUMNS;

EID: 47249136515     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0709133     Document Type: Article

References (5)

1. Shah, Y. T.; Kelkar, B. G.; Godbole, S. P.; Deckwer, W.-D. Design Parameters Estimations for Bubble Column Reactors. AIChE J. 1982, 28 (3), 353.
2. Fair, J. R. Designing Gas-Sparged Reactors. Part I. Chem. Eng. 1967, 74 (14), 67.
3. Fair, J. R. Designing Gas-Sparged Reactors. Part II. Chem. Eng. 1967, 74 (15), 207.
4. Fair, J. R.; Lambright, A. J; Andersen, J. W. Heat Transfer and Gas Holdup in a Sparged Contactor. Ind. Eng. Chem. Process Des. Dev. 1962, 1 (1), 33.
5. Garcia, J. A.; Fair, J. R. A Fundamental Model for the Prediction of Distillation Sieve Tray Efficiency. Ind. Eng. Chem. Res. 2000, 39, 1809.