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Residence-time distribution reactive tracer

The time that a molecule spends in a reactive system will affect its probability of reacting and the measurement, interpretation, and modeling of residence time distributions are important aspects of chemical reaction engineering. Part of the inspiration for residence time theory came from the black box analysis techniques used by electrical engineers to study circuits. These are stimulus-response or input-output methods where a system is disturbed and its response to the disturbance is measured. The measured response, when properly interpreted, is used to predict the response of the system to other inputs. For residence time measurements, an inert tracer is injected at the inlet to the reactor, and the tracer concentration is measured at the outlet. The injection is carried out in a standardized way to allow easy interpretation of the results, which can then be used to make predictions. Predictions include the dynamic response of the system to arbitrary tracer inputs. More important, however, are the predictions of the steady-state yield of reactions in continuous-flow systems. All this can be done without opening the black box. [Pg.540]

Reactive Tracer. If the tracer is reactive, the measured concentrations reflect both mixing characteristics and decay of the tracer. Therefore, the data must be adjusted, such that the residence time distribution within the reactor can be obtained. Example 19-3 illustrates how to adjust the data following a step input of a reactive tracer. [Pg.466]

Residence time distributions can be determined in practice by injecting a non-reactive tracer material into the input flow to the reactor and measuring the output response characteristics in a similar manner to that described previously in Section 2.1.1. [Pg.123]

Primarily non-reactive substances that can be easily analyzed for concentration are used as tracers. When making a test, tracer is injected to the inlet of the vessel along with the normal charge of process or carrier fluid, according to some definite time sequence. The progress of both the inlet and outlet concentrations with time is noted. Those data are converted to a residence time distribution, RTD, that tells how much time each fraction of the charge spends in the vessel. [Pg.490]

Figure 8.9 Residence time distribution (RTD) for a pulsed tubular reactor. Average residence time = 60 min, with a pulsation rate of 99 spm. C is a dimensionless concentration of a non-reactive tracer solid line is experimental data dashed line is theoretical laminar-flow RTD. [23]... Figure 8.9 Residence time distribution (RTD) for a pulsed tubular reactor. Average residence time = 60 min, with a pulsation rate of 99 spm. C is a dimensionless concentration of a non-reactive tracer solid line is experimental data dashed line is theoretical laminar-flow RTD. [23]...

See other pages where Residence-time distribution reactive tracer is mentioned: [Pg.160]    [Pg.350]    [Pg.954]    [Pg.3100]    [Pg.687]   
See also in sourсe #XX -- [ Pg.466 , Pg.467 ]




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