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In terms of kinetic energy, these are the most powerful eddies in this region.
Finally, selectivity patterns have been discussed in terms of kinetic rates of vitamin B2 release.
In terms of kinetic equations, pseudo first-order, pseudo second-order and intraparticle diffusion models are expressed as Eqs.
In addition, the transfers of radionuclides between the liquid and solid phases are described in terms of kinetic transfer coefficients.
In this work, a kinetic model (in terms of kinetic parameters) for the HDAs reaction in the TBR is developed.
The obtained spatial gradients can be analyzed in terms of kinetic and mechanistic information about the reaction under study.
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The NO3 N is strongly agree with Pseudo first-order kinetic model by considering both correlation coefficients (R2) and experimental and calculated q e value, but PO4 P agree with second-order kinetics in terms of both kinetic parameters using scoria adsorbent.
An autocatalytic kinetic reaction occurs in these systems, and the kinetic parameters of all systems were reported in terms of generalized kinetic equation that considered the diffusion term.
The removal of copper and cadmium from zeolite as a function of time can be mathematically expressed in terms of different kinetic adsorption models such as: Pseudo-first-order kinetic model supposes that the rate of change of adsorbate uptake with time is directly proportional to the difference in the equilibrium concentration and the amount of adsorbate uptake with time (Ho and McKay 1998).
The observed kinetics are rationalised in terms of a kinetic model in which the rate determining step is the reduction of photocatalyst surface-adsorbed Rz by photo-generated surface electrons, with all photocatalyst surface sites occupied by Rz.
All kinetic parameters of each epoxy resin systems were reported in terms of generalized kinetic equation that considered diffusion term, and the network structure of each epoxy resin systems with different curing agents were analyzed using DiBenedetto equation.
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