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ACETYLENE DETONATION IN A CONSTANT-VOLUME REACTOR TO CREATE ENERGY-EFFICIENT CARBON-NEUTRAL CYCLESThis paper is devoted to the study of acetylene thermal decomposition in a flow reactor under
Decomposition of Acetylene into Hydrogen and Carbon: Experiments with Internal Combustion Engines and Experiments with a Flow Reactor combustion engine (ICE) and in a flow-type reactor with external heat supply at a constant temperature (1000
Methane Steam Reforming in a Pd-Ru Membrane Reactor-bed reactor was 57%. The effect of gas flow rate and temperature on the performance of the membrane reactor
Investigation of internal elements impaction on particles circulation in a fluidized bed reactor-dependent processes with heat absorption is considered. The task of incoming heated catalyst granules to the reactor
Dehydrogenation of Methylbutenes to Isoprene: A Comparative Mathematical Analysis of the Dehydrogenation of Methylbutenes to Isoprene in Axial and Radial Reactors upgrading variants: (1) a system of two serially arranged axial fixed-bed reactors and (2) an adiabatic
Numerical simulation of a flow mixer for a radial type chemical reactor to styrene process was studied. A variant of a radial type reactor in which the gas flow is from the bottom
CFD modeling a fluidized bed large scale reactor with various internal elements near the heated particles feeder on the circulation flows of the catalyst particles and heating of the reactor. The analysis of the impact of various
Application of the universal ultrasonic reactor in the processing of rare earth metal ores concentrates. The first method is traditional leaching, but with the use of modern ultrasonic reactors of a through
Effect of the design of a feedstock injection device in a fluidized-bed reactor on the efficiency of the reaction using the dehydrogenation of iso-paraffins in a fluidized chromia–alumina catalyst bed as an example of industrial chemical fluidized-bed reactors with different gas feedstock injection devices, i.e, three
Numerical simulation of heat and mass transfer processes in large-scale fluidized bed complex structure apparatus as an example of the reactor of isoparaffins dehydrogenation. In this paper we consider a fluidized bed reactor block intended for the dehydrogenation of isobutane
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