Taking mass transfer limitation into account during ozonation of pollutants reacting fairly quickly

Water Science and Technology

Volumn 49, Issue 4, 2004, Pages 25-30

  Benbelkacem, H ^a   Mathe S ^a   Debellefontaine, H ^a  

^a UMR792 INGÉNIERIE DES SYSTÈMES BIOLOGIQUES ET DES PROCÉDÉS   (France)

Author keywords

Fumaric acid; Kinetic regimes; Mass transfer; Modelling; Ozone

Indexed keywords

CONCENTRATION (PROCESS); DECOMPOSITION; MASS TRANSFER; MATHEMATICAL MODELS; ORGANIC COMPOUNDS; OXIDATION; OZONE; RATE CONSTANTS; REACTION KINETICS;

FUMARIC ACID OZONATION; MASS BALANCES; SEMI-BATCH REACTORS;

WATER POLLUTION CONTROL;

FUMARIC ACID; ORGANIC COMPOUND; OZONE;

KINETICS; MASS TRANSFER; OZONATION; REACTOR;

ARTICLE; BATCH REACTOR; CHEMICAL MODEL; CHEMICAL REACTION KINETICS; CONCENTRATION (PARAMETERS); CONSTANTS AND COEFFICIENTS; CONTROLLED STUDY; DECOMPOSITION; DISSOLUTION; GAS; LIQUID; MATHEMATICAL COMPUTING; OXIDATION; OZONATION; PHASE TRANSITION; POLLUTION CONTROL; PROCESS OPTIMIZATION; REACTION TIME; TIME; WASTE WATER MANAGEMENT;

EID: 1842577553     PISSN: 02731223     EISSN: None     Source Type: Journal    
DOI: 10.2166/wst.2004.0210     Document Type: Article

References (3)

1. Benbelkacem, H. and Debellefontaine, H. (2003). Modelling of a gas-liquid reactor in batch conditions. Study of the intermediate regime when part of the reactions occurs within the film and part within the bulk. Chem. Eng. Proc., 42(10), 723-732.
2. Lewis, W.K and Whitman, G. (1924). Principles of gas absorption. Ind. Eng. Chem., 16(12), 1215-1220.
3. Roizard, C., Wild, G. and Charpentier, J.C. (1996). Absorption avec réaction chimique. Techniques de l'Ingé nieur, J-1079, 1-21.