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Photochemical reactors configurations

Classical chemical reaction engineering provides mathematical concepts to describe the ideal (and real) mass balances and reaction kinetics of commonly used reactor types that include discontinuous batch, mixed flow, plug flow, batch recirculation systems and staged or cascade reactor configurations (Levenspiel, 1996). Mixed flow reactors are sometimes referred to as continuously stirred tank reactors (CSTRs). The different reactor types are shown schematically in Fig. 8-1. All these reactor types and configurations are amenable to photochemical reaction engineering. [Pg.240]

Figure 3.9 Left a photochemical reactor with immersed configuration with the lamp and a power source. Right detail of the immersion well. Reproduced by permission of Ace Glass Inc... Figure 3.9 Left a photochemical reactor with immersed configuration with the lamp and a power source. Right detail of the immersion well. Reproduced by permission of Ace Glass Inc...
Figure 3.10 Rayonet photochemical reactor (external configuration). Reproduced by permission of Southern New England Ultra Violet Company... Figure 3.10 Rayonet photochemical reactor (external configuration). Reproduced by permission of Southern New England Ultra Violet Company...
The ideas described in this section can be easily extended to more complex reacting systems either from the chemistry point of view - for example to include the parallel oxidation reaction with hydrogen peroxide or ozone - or to deal with other lamp-reactor configurations. A comprehensive, tutorial review for homogeneous photochemical reactors has been published (Cassano etai, 1995) that provides most of the required methods. [Pg.147]

Figure 27.18 Common configuration for postcolumn reactors with electrochemical analysis. (A) LC-chemical reaction-EC. Postcolumn addition of a chemical reagent (for example, Cu2+ or an enzyme). (B) LC-enzyme-LC. Electrochemical detection following postcolumn reaction with an immobilized enzyme or other catalyst (for example, dehydrogenase or choline esterase). (C) LC-EC-EC. Electrochemical generation of a derivatizing reagent. The response at the second electrode is proportional to analyte concentration (for example, production of Br2 for detection of thioethers). (D) LC-EC-EC. Electrochemical derivatization of an analyte. In this case a compound of a more favorable redox potential is produced and detected at the second electrode (for example, detection of reduced disulfides by the catalytic oxidation of Hg). (E) LC-hv-EC. Photochemical reaction of an analyte to produce a species that is electrochemically active (for example, detection of nitro compounds and phenylalanine). Various combinations of these five arrangements have also been used. [Reprinted with permission from Bioanalytical Systems, Inc.]... Figure 27.18 Common configuration for postcolumn reactors with electrochemical analysis. (A) LC-chemical reaction-EC. Postcolumn addition of a chemical reagent (for example, Cu2+ or an enzyme). (B) LC-enzyme-LC. Electrochemical detection following postcolumn reaction with an immobilized enzyme or other catalyst (for example, dehydrogenase or choline esterase). (C) LC-EC-EC. Electrochemical generation of a derivatizing reagent. The response at the second electrode is proportional to analyte concentration (for example, production of Br2 for detection of thioethers). (D) LC-EC-EC. Electrochemical derivatization of an analyte. In this case a compound of a more favorable redox potential is produced and detected at the second electrode (for example, detection of reduced disulfides by the catalytic oxidation of Hg). (E) LC-hv-EC. Photochemical reaction of an analyte to produce a species that is electrochemically active (for example, detection of nitro compounds and phenylalanine). Various combinations of these five arrangements have also been used. [Reprinted with permission from Bioanalytical Systems, Inc.]...
Regarding the photocatalyst structural configuration, thin-film powder layer and/or fluidized bed, coated wall-parallel, and honeycomb/foam monolithic reactors are probably the most representative. For photochemical water splitting, batch-type photoreactor is most frequently used configuration in lab-scale investigations. In the case of solar photoreactor systems, there are two of the major design issues (i) whether to use a suspended or a supported photocatalyst and (ii) whether to use concentrated or non-concentrated sunlight. [Pg.212]


See other pages where Photochemical reactors configurations is mentioned: [Pg.51]    [Pg.253]    [Pg.234]    [Pg.83]    [Pg.302]    [Pg.522]    [Pg.292]    [Pg.164]    [Pg.282]    [Pg.332]    [Pg.116]   
See also in sourсe #XX -- [ Pg.819 ]




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Photochemical reactors

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