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Nonadiabatic nonisothermal tubular reactors

Here we consider a nonisothermal, nonadiabatic tubular reactor as a distributed system. Our objective is to find its steady-state concentration and temperature profiles. [Pg.138]

Modeling of Tubular Nonisothermal Nonadiabatic Packed-Bed Reactors with Catalyst Poisoning... [Pg.381]

For noncatalytic homogeneous reactions, a tubular reactor is widely used because it cai handle liquid or vapor feeds, with or without phase change in the reactor. The PFR model i usually adequate for the tubular reactor if the flow is turbulent and if it can be assumed tha when a phase change occurs in the reactor, the reaction takes place predominantly in one o the two phases. The simplest thermal modes are isothermal and adiabatic. The nonadiabatic nonisothermal mode is generally handled by a specified temperature profile or by heat transfer to or from some specified heat source or sink and a corresponding heat-transfer area and overall heat transfer coefficient. Either a fractional conversion of a limiting reactant or a reactoi volume is specified. The calculations require the solution of ordinary differential equations. [Pg.214]

The deactivation process in a tubular nonisothermal nonadiabatic reactor depends on a number of kinetic and operational parameters. There are two major questions which we would like to answer (a) can we use the one-dimensional model for simulation... [Pg.385]


See other pages where Nonadiabatic nonisothermal tubular reactors is mentioned: [Pg.443]    [Pg.443]    [Pg.444]   
See also in sourсe #XX -- [ Pg.443 ]




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