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The shrinking-core model for reaction control was applied to particle size distributions, particularly to the logarithmic normal distribution.
This kinetic hydration model includes three sub-models, i.e. model for hydration of cement, model for reaction of slag, and model for mutual effects between hydration of cement and reaction of slag.
Firstly, we validate our model for reaction against analytical solutions for the bimolecular reaction (A + B → C) in a free fluid.
We have developed a methodology for simulation of thermal reactive flow with fidelity to reaction kinetics without construction of a model for reaction.
Fundamental studies on functional group tolerance and an understanding of the steric and electronic factors crucial to product selectivity have led to the development of an empirical model for reaction design.
The properties of the cross-flow hydrogenation were discussed in connection with a mathematical model for reaction and mass transport in pores and channels of the cross-flow catalyst.
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Experimental data available in the literature are interpreted successfully by the present model for reactions of Ca-sorbents with SO2, H2S and HCl.
A new mechanistic model for reactions involving two liquid phases and a homogeneous phase transfer catalyst (PTC) has been developed based on extraction mechanism considering the equilibrium of catalyst and active catalysts at the interface.
The two-dimensional model is based on a comprehensive description of mass, charge and momentum transport and conservation, and is combined with a global kinetic model for reactions involving vanadium species.
The two-dimensional model is based on a comprehensive description of mass, charge, energy and momentum transport and conservation, and is combined with a global kinetic model for reactions involving vanadium species.
This algorithm is based on the Smoluchowski model for reaction-diffusion systems [ 14].
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