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Continuous flow reactor steady state, mixtures with

The experimental programme was mainly concerned with estimating kinetic parameters from isothermal steady state operation of the reactor. For these runs, the reactor was charged with the reactants, in such proportions that the mixture resulting from their complete conversion approximated the expected steady state, as far as total polymer concentrations was concerned. In order to conserve reactants, the reactor was raised to the operating temperature in batch mode. When this temperature had been attained, continuous flow operation commenced. This was... [Pg.284]

Flow reactors are fed continuously at one location with streams of reactants already at the required temperature and pressure. The reaction mixture flows out continuously from the end of the reaction zone. Flow reactors are operated under steady-state conditions, i.e. concentrations, temperature, and pressure at a point of the reaction zone are constant. To be precise, they fluctuate with the quality of raw materials and the accuracy of controllers maintaining flows, temperatures, and pressure. [Pg.259]

Cross-flow reactors are fed continuously with streams of components of the reaction mixture whereby some components are introduced at the inlet, while others are introduced at other locations. The reaction mixture flows out continuously from the end of the reaction zone. A cascade of CSTRs with additional feeds to individual reactors represents a cross-flow reactor system. Cross-flow reactors are also operated at steady-state conditions ... [Pg.260]

Propane aromatization reaction (at 550°C) was carried out at atmospheric pressure in a continuous flow quartz reactor (id 13 mm), using a propane-nitrogen mixture (33.3 mol-% propane) as a feed with a space velocity of 3100 cm g h". The catalytic activity and selectivity were measured as a function of time-on-stream (up to about 6.7 + 0.2 h). The reaction products were analyzed by an on-line GC with FID, using Poropak-Q (3 mm x 3 m) and Benton-34 (5%) and dinonylphthalate (5%) on Chromosorb-W (3 mm x 5 m) columns. The activity and selectivity data at different space velocities in the absence of catalyst deactivation (i.e. initial activity/selectivity) at 550°C were obtained by the square pulse technique by passing the reaction mixture at different space velocities over fresh catalyst for a short period (2-5 min) under steady state and then replacing the reactant mixture by pure Nj during the product analysis by the GC. [Pg.426]


See other pages where Continuous flow reactor steady state, mixtures with is mentioned: [Pg.494]    [Pg.275]    [Pg.2]    [Pg.45]    [Pg.852]    [Pg.26]    [Pg.227]    [Pg.155]    [Pg.257]    [Pg.147]    [Pg.66]    [Pg.295]    [Pg.97]    [Pg.97]   


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Continuous flow

Continuous flow reactors steady state

Continuous mixtures

Continuous steady-state flow

Continuous-flow reactors

Flow state

Mixture continuity

Mixture state

Reactor steady state

State, continuity

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