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The feasibility of using the spherical catalysts NiO/SiO2 and Fe2O3/SiO2 in the process of hydrogenation of polycyclic hydrocarbons model is connected with the chemical activity, which is proportional to the specific surface area and high-dispersing, and the porous structure of these catalytic systems.
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Sulfonation of hydrocarbon model compounds yields completely conjugated and functionalized products.
This work investigates the hydrothermal conversion of hexadecane, as a heavy hydrocarbon model for heavy oil upgrading, and syngas generation.
A newly-developed kinetic model, which was based on a C1‒C4 hydrocarbon model and agent-inhibition sub-models, was used to compare with the measured flame speeds and extinction stretch rates.
We present molecular simulation results for the adsorption of a set of hydrocarbons in model zeolite structures of various pore sizes.
The hydrocarbons are modeled using pseudocompounds, while the organic sulfur compounds are modeled using model compounds, i.e., dibenzothiophene (DBT) and 4,6-dimethyl dibenzothiophene (4,6-DMDBT).
This gives the hydrocarbon system model often used for petroleum reservoir simulations.
A refinery with annual nameplate capacity of 76,000 cubic meters hydrocarbons was modeled.
In the present work VLE data of 3-Methylthiophene with various hydrocarbons were modeled using genetic algorithm.
DED1 is thus a property of Miller Heirs production data and the gas-solid hydrocarbon equilibrium model as Figure 7 so clearly illustrates.
In this paper we introduce a finite volume method for solving the hydrocarbon system model often used for petroleum reservoir simulations.
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