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Membrane reactors constitutive equations

In this appendix the constitutive equations used in the modeling of packed bed membrane reactors (either ID or 2D) are listed. Components properties have be evaluated by making use of book The Properties of Gases and Liquids. [Pg.29]

These three parameters (or other equivalent dimensionless groups) must appear in whatever formulation of this type of problem (the esterification reaction in PVRs), possibly together with other parameters which take into account other aspects such as additional phenomena (for example concentration polarization of the membrane), the presence of products in the initial mixture, the concentration of the catalyst and more complex constitutive equations. The dimensionless parameters have a more general validity than the individual dimensional parameters that appear grouped into them and characterize more univocally the behaviour of the system. The adoption of the parameter 5, the ratio of the characteristic rate of permeation to the characteristic rate of reaction, can be extended to any PVR and in general also to any membrane reactor. With this approach the comparison between different studies on PVRs is more direct and meaningful. On the other hand, the less acceptable, though often employed, dimensional parameter A/V, is comprised in the definition of 5. [Pg.132]


See other pages where Membrane reactors constitutive equations is mentioned: [Pg.115]   
See also in sourсe #XX -- [ Pg.29 , Pg.30 , Pg.31 ]

See also in sourсe #XX -- [ Pg.29 , Pg.30 , Pg.31 ]




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