Effect of kinetics and mass transfer on design of extractive reaction processes

Samant, Ketan D.; Ng, Ka Ming

doi:10.1002/aic.690441010

Cited by 35 publications

(21 citation statements)

References 19 publications

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“…Coupling reaction with a separation unit in an integrated reactor has the potential for enhancing the conversion and selectivity of an equilibrium reaction, and reducing the cost of equipment [27], as is always being used in the industry. Hence, a continuous model of cellulose degradation and product separation in an integrated reactor is proposed based on the above reaction mechanism and process analysis.…”

Section: Continuous Modelmentioning

confidence: 99%

Kinetic analysis and process modeling for cellulose valorization in cooperative ionic liquid pairs

et al. 2016

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Section: Continuous Modelmentioning

confidence: 99%

Kinetic analysis and process modeling for cellulose valorization in cooperative ionic liquid pairs

et al. 2016

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“…The selected reactor type form the starting point for further rigorous design and development. Additional details can be found in [9].…”

Section: Screening Of Reactor Typesmentioning

confidence: 99%

“…The reactions can occur in any one or both the phases. The detailed development of the model is given in [9].…”

Section: Effect Of Kinetics and Mass Transfermentioning

confidence: 99%

Systematic Development of Extractive Reaction Processes

Samant

Ng²

1999

Chem. Eng. Technol.

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A systematic framework for the development of extractive reaction processes is presented. It consists of four steps: synthesis of process flow sheets on the basis of reactive-phase diagrams, evaluation of process trade-offs using geometrical design methods, analysis of kinetics and mass transfer effects, and selection of reactor types for the desired performance. We demonstrate these methods for a five-component system with two reactions in parallel.

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“…Consider a multiphase reactive separator with r reactions. If we write detailed material balance equations at constant temperature and pressure, the approach to reaction equilibrium can be shown to be governed by dimensionless Damkohler numbers ŽVenimadhavan et al, 1994;Nisoli et al, 1997;Samant and . Ng, 1998b Ž .…”

Section: Synthesis Of Prepolymerization Processesmentioning

confidence: 99%