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The measured intracrystalline diffusivity was found to be well represented by the model equations based on the electrostatic field mechanism.
A comparison of the calculated liquid distribution with photographs shows very good qualitative agreement of the real liquid distributions by the model equations.
The results showed that the experimental ethanol conversions and hydrogen yield ratios at varying space times and reaction temperatures could be satisfactorily predicted by the model equations.
It is shown that the oxygen concentration and the decrease in sulfur retention at lower stoichiometric air ratios can readily be described by the model equations.
Experimental measurements of the conductivity of arrays of copper cylinders in acid copper sulphate electrolyte over a range of void fractions and potential gradients under both dc and ac conditions are compared with the conductivities predicted by the model equations.
The eigenvalues associate with the modes (l,m) of the spherical harmonic expansion satisfy characteristic equations determined by the model equations and boundary conditions.
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The heat demand D c,t is calculated by solving the model equations including a simple zone temperature control.
SEM integrates empirical information with mechanistic knowledge by deriving the model equations from known causal relationships, while estimating the model parameters using the available data.
The kinetic parameters of the model were previously estimated by fitting the model equations to experimentally obtained metabolite time course data [ 25].
By integrating the model equations with θ* we generate an exact data set at the same data points as the initial data set.
The experiment using optimized parameters in batch fermenter not only resulted in higher ethanol concentration than the one predicted by the model equation, but also saved fermentation time.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com