Calculation of the Methane Pyrolysis Reactor Taking into Account the Non-Isochority of the Process of the Reaction

Based on the results of the analysis of literature sources, the kinetics of the methane pyrolysis process is described. Examples of calculating plug-and-play reactors and mixing reactors for a conversion rate of 0,99 at a methane capacity of 6000 kg/h are given. It is shown that the volume of a plug-flow reactor should be more than 20 times the volume of a plug-flow reactor. Comparison of calculations by kinetic equations for an isochoric process and a process that takes into account the increase in the value of the reaction mass, due to which the formed sample of the reaction of hydrogen. The effect of temperature on the core volume has been performed and the optimum temperature has been chosen 1250°С

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Kinetics of the Conversion of Silicon Tetrachloride into Trichlorosilane Obtained through the Temperature Control along a Plug-Flow Reactor

International Journal of Chemical Kinetics ◽

10.1002/kin.20969 ◽

2015 ◽

Vol 48 (1) ◽

pp. 45-57 ◽

Cited By ~ 5

Author(s):

Nílson Kunioshi ◽

Yu Moriyama ◽

Akio Fuwa

Keyword(s):

Temperature Control ◽

Flow Reactor ◽

Plug Flow ◽

Silicon Tetrachloride ◽

Plug Flow Reactor ◽

Kinetics Of

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Kinetics and Product Selectivity (Yield) of Second Order Competitive Consecutive Reactions in Fed-Batch Reactor and Plug Flow Reactor

ISRN Chemical Engineering ◽

10.1155/2013/591546 ◽

2013 ◽

Vol 2013 ◽

pp. 1-17 ◽

Cited By ~ 2

Author(s):

Subash Chandra Bose Selvamony

Keyword(s):

Flow Reactor ◽

Batch Reactor ◽

Plug Flow ◽

Second Order ◽

Plug Flow Reactor ◽

Effect Of Temperature ◽

Product Selectivity ◽

Fed Batch ◽

Consecutive Reaction ◽

Consecutive Reactions

This literature compares the performance of second order competitive consecutive reaction in Fed-Batch Reactor with that in continuous Plug Flow Reactor. In a kinetic sense, this simulation study aims to develop a case for continuous Plug Flow Reactor in pharmaceutical, fine chemical, and related other chemical industries. MATLAB is used to find solutions for the differential equations. The simulation results show that, for certain cases of nonelementary scenario, product selectivity is higher in Plug Flow Reactor than Fed-Batch Reactor despite the fact that it is the same in both the reactors for elementary reaction. The effect of temperature and concentration gradients is beyond the scope of this literature.

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Kinetics of the selective hydrogenation of cyclopentadiene on a CuAl2O3 aerogel catalyst in an integral plug flow reactor

Applied Catalysis ◽

10.1016/s0166-9834(00)81339-1 ◽

1986 ◽

Vol 21 (1) ◽

pp. 187-199 ◽

Cited By ~ 12

Author(s):

J. Chaouki ◽

C. Chavarie ◽

D. Klvana ◽

G.M. Pajonk

Keyword(s):

Selective Hydrogenation ◽

Flow Reactor ◽

Plug Flow ◽

Plug Flow Reactor ◽

Kinetics Of

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Kinetics of acid hydrolysis of hardwood in a continuous plug flow reactor.

10.1349/ddlp.3201 ◽

1983 ◽

Author(s):

Isaac Kwabena Kwarteng

Keyword(s):

Acid Hydrolysis ◽

Flow Reactor ◽

Plug Flow ◽

Plug Flow Reactor ◽

Kinetics Of ◽

Hydrolysis Of

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PLUG-FLOW REACTOR-BASED ANTIBIOTIC AND NUTRIENT REMOVAL BY VETIVER GRASS (CHRYSOPOGON ZIZANIOIDES)

10.1130/abs/2020am-358630 ◽

2020 ◽

Author(s):

Dibyendu Sarkar ◽

◽

Saumik Panja ◽

Rupali Datta

Keyword(s):

Nutrient Removal ◽

Flow Reactor ◽

Plug Flow ◽

Plug Flow Reactor ◽

Vetiver Grass ◽

Chrysopogon Zizanioides

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Kinetics of the catalytic hydrodesulphurization reaction system; hydrogenolysis of thiophene

Collection of Czechoslovak Chemical Communications ◽

10.1135/cccc19802728 ◽

1980 ◽

Vol 45 (10) ◽

pp. 2728-2741 ◽

Cited By ~ 7

Author(s):

Pavel Fott ◽

Petr Schneider

Keyword(s):

Atmospheric Pressure ◽

Active Sites ◽

Flow Reactor ◽

Kinetic Equations ◽

Reaction System ◽

Reaction Products ◽

Molybdenum Catalyst ◽

Cobalt Molybdenum Catalyst ◽

Kinetics Of ◽

Reaction Schemes

Kinetics have been studied of the reaction system taking place during the reaction of thiophene on the cobalt-molybdenum catalyst in a gradientless circulation flow reactor at 360 °C and atmospheric pressure. Butane has been found present in a small amount in the reaction products even at very low conversion. In view of this, consecutive and parallel-consecutive (triangular) reaction schemes have been proposed. In the former scheme the appearance of butane is accounted for by rate of desorption of butene being comparable with the rate of its hydrogenation. According to the latter scheme part of the butane originates from thiophene via a different route than through hydrogenation of butene. Analysis of the kinetic data has revealed that the reaction of thiophene should be considered to take place on other active sites than that of butene. Kinetic equations derived on this assumption for the consecutive and the triangular reaction schemes correlate experimental data with acceptable accuracy.

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