X. Meyer | ENSIACET - Academia.edu (original) (raw)
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Papers by X. Meyer
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Industrial & Engineering Chemistry Research, 2001
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Chemical Engineering Research & Design, 2007
First steps of the development of a catalytic reactive distillation process for the production of... more First steps of the development of a catalytic reactive distillation process for the production of n-propyl acetate based on experiments and simulations are proposed. The kinetics for homogeneously (sulphuric acid) and heterogeneously (Amberlyst 15) catalysed reaction were investigated and the constants for a pseudo-homogeneous model are presented. Pilot plant experiments were performed using a homogeneous strong acid catalyst in a
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Computers & Chemical Engineering, 2004
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Chemical Engineering and Processing: Process Intensification, 2008
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Computers & Chemical Engineering, 1999
The modeling of batch crystallization involves a population balance to get the crystal size distr... more The modeling of batch crystallization involves a population balance to get the crystal size distribution which is one of the most important properties in this process. Thus, this model leads to a system of integral, partial differential and algebraic equations (IPDAE). This system can be easily solved by finite difference methods with uniform discretization. However to increase the calculation efficiency and the crystal size distribution accuracy, an adaptive finite difference method with a non-uniform discretization was developed. Results of both methods are compared in term of efficiency and are confronted to experimental data in term of accuracy.
Bookmarks Related papers MentionsView impact
Bookmarks Related papers MentionsView impact
Industrial & Engineering Chemistry Research, 2001
Bookmarks Related papers MentionsView impact
Chemical Engineering Research & Design, 2007
First steps of the development of a catalytic reactive distillation process for the production of... more First steps of the development of a catalytic reactive distillation process for the production of n-propyl acetate based on experiments and simulations are proposed. The kinetics for homogeneously (sulphuric acid) and heterogeneously (Amberlyst 15) catalysed reaction were investigated and the constants for a pseudo-homogeneous model are presented. Pilot plant experiments were performed using a homogeneous strong acid catalyst in a
Bookmarks Related papers MentionsView impact
Computers & Chemical Engineering, 2004
Bookmarks Related papers MentionsView impact
Chemical Engineering and Processing: Process Intensification, 2008
Bookmarks Related papers MentionsView impact
Computers & Chemical Engineering, 1999
The modeling of batch crystallization involves a population balance to get the crystal size distr... more The modeling of batch crystallization involves a population balance to get the crystal size distribution which is one of the most important properties in this process. Thus, this model leads to a system of integral, partial differential and algebraic equations (IPDAE). This system can be easily solved by finite difference methods with uniform discretization. However to increase the calculation efficiency and the crystal size distribution accuracy, an adaptive finite difference method with a non-uniform discretization was developed. Results of both methods are compared in term of efficiency and are confronted to experimental data in term of accuracy.
Bookmarks Related papers MentionsView impact