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We developed a detailed kinetic model for methanol conversion to hydrocarbons over zeolites.
A three-dimensional model for methanol steam reaction in this designed microreactor is developed and numerically analyzed.
A simple lumped kinetic model for methanol conversion to hydrocarbons on a ZSM-5 catalyst over the 302 370°C temperature range is revised and tested, provingthe model to be satisfactory at different conversion levels and catalyst deactivation degrees.
In the preceding section, profiles for fractional formation of FAME with time have been obtained using developed ANN model for methanol to oil molar ratios namely, 9 1, 12 1, and 15:1, and experimental profiles for molar ratio 18 1 and 25:1 are already available at optimum catalyst amount and temperature.
The sub-grid scale (sgs) probability density function (pdf) approach in conjunction with the Eulerian stochastic field method are employed to represent the unknown interaction between turbulence and chemistry at the sub-filter level while a comprehensive kinetics model for methanol oxidation with 18 chemical species and 84 elementary steps is used to account for the gas-phase reaction.
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Three differently detailed kinetic models for methanol synthesis are derived for experimental data measured over a ternary copper catalyst.
Different mathematical model structures for methanol synthesis have been developed and documented in the literature; some of those with applications are introduced in this chapter.
Additionally, it is also a commonly used model organism for methanol assimilation and peroxisomal biogenesis.
For this reason, the generalized overall model for explaining methanol synthesis is still under investigation.
In the present paper new detailed kinetic model for the methanol synthesis from H2, CO2 and/or CO using a Cu/ZnO/Al2O3 catalyst is proposed.
The validity of several kinetic models, available for methanol synthesis, is analysed and modifications are proposed.
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