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Plug flow, reactor model space time

In a tubular reactor, the concentration and temperature may vary both in time and space. One speaks about a distributed system. The ideal plug flow reactor (PFR) model is the most used. Because of the flat velocity profile, the concentrations and temperature varies only along the length. Consider for simplification a homogeneous reaction. The unsteady state material balance of the reactive species leads to the following equation ... [Pg.130]

J. M. Castro, S. D. Lipshitz, and C. W. Macosko [AIChE J., 28, 973 (1982)] modeled a thermosetting polymerization reaction in a laminar flow reactor under several different operating conditions. Demonstrate your ability to simulate the performance of a plug flow reactor for this reaction under both isothermal and adiabatic reaction conditions. In particular, determine the reactor space times necessary to achieve 73% conversion for both modes of operation and the following parameter values for a (3/2)-order reaction (r = kc - ). [Pg.330]

Model of ideal desaturation (model with plug flow regime) is the favorable approximation for calculation of reactor parameters [3,4,6] any cross-section normal for flow, weight hour space velocity w and flow s properties (pressure, temperature and reaction mixture structure) are uniform narrow distribution of reagents residence times in reaction zone Xpr diffusion in the axial line (coplanar mixing or turbulence) in comparison with weight hour space velocity is negligible low. [Pg.7]


See other pages where Plug flow, reactor model space time is mentioned: [Pg.443]    [Pg.208]    [Pg.115]    [Pg.91]    [Pg.246]    [Pg.408]    [Pg.200]    [Pg.219]    [Pg.126]    [Pg.331]    [Pg.126]    [Pg.366]    [Pg.368]    [Pg.198]    [Pg.418]    [Pg.346]   
See also in sourсe #XX -- [ Pg.248 ]




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