A complete model for oxidation air-lift reactors

Computers and Chemical Engineering

Volumn 25, Issue 4-6, 2001, Pages 577-584

  Camarasa, E ^a   Meleiro, L A C ^b   Carvalho, E ^b   Domingues, A ^a   Maciel Filho, R ^b   Wild, G ^c   Poncin, S ^c   Midoux, N ^c   Bouillard, J ^d  

^a Rhodia Brasil Ltda CPP   (Brazil)

^b UNIVERSITY OF CAMPINAS   (Brazil)

^c UNIVERSITÉ DE LORRAINE   (France)

^d SANOFI   (France)

Author keywords

Airlift reactor; Gas hold up; Hydrodynamics; Mass transfer; Modeling

Indexed keywords

HYDRODYNAMICS; MASS TRANSFER; OXIDATION; REACTION KINETICS;

AIR-LIFT REACTORS;

CHEMICAL REACTORS;

AIRLIFT REACTOR; OXIDATION; PERFORMANCE PREDICTION;

CALCULATION; CELL; CONFERENCE PAPER; HYDRODYNAMICS; MASS; MATHEMATICAL ANALYSIS; MATHEMATICAL MODEL; OXIDATION; PREDICTION; REACTOR;

EID: 0035340110     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0098-1354(01)00637-8     Document Type: Conference Paper

References (13)

1. Phenol-acetone process: Cumene oxidation kinetics and industrial plant simulation
2. Liquid circulation in airlift reactors
3. A reassessment of relationship between riser and gas hold-ups in airlift reactors
4. Prediction of gas hold-up and liquid velocity in airlift reactors using two-phase flow friction coefficients
5. Gas-holdup and liquid circulation in gas-liquid reactors
6. Sparged loop reactors
7. A hydrodynamic model for an airlift-loop reactor
8. Average volumetric concentration in two-phase flow systems