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A plug flow model and a model comprising mass and heat dispersion in the reactor are discussed.
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The model comprises mass, energy and momentum equations coupled with a rate equation that describes both the primary and secondary pyrolysis reactions.
Firstly, a flow model comprised of mass, energy and momentum equations is established.
The model comprises dynamic mass balances for water and salt, as well as evaporation calculation based on energy and momentum balances on a daily basis.
A mathematical model comprising conservation of mass, momentum, and ions for a hydrogel subject to alterations of the solution pH is derived, analyzed, validated and presented.
The dynamic behaviour of a reaction system in a continuous-flow stirred tank reactor (CSTR) is described by a model comprising the unsteady mass and heat balances and the kinetics of the reaction system concerned.
A model comprising external and intraparticle mass transfer resistances has been developed to describe ion exchange in microporous materials.
A model comprising differential equations for mass and heat transfer is proposed for the simulation of the continuous thermal processing of a non-Newtonian food in a tubular system.
A twin resistance mass transfer model, comprising a fixed edge resistance and a resistance which increased with frontal depth, was able to describe the sublimation kinetics.
This model comprises a lumped mass denoeing the isolated object and a pair of horizontal springs providing negative stiffness paralleled with a vertical linear spring to bear the load.
Firstly, a mathematical model comprised of the mass conservation equation, momentum balance equation and energy balance equation in the integral joint tubing (IJT) and annuli is proposed for concentric dual-tubing wells (CDTW), and in the main tubing (MT) and auxiliary tubing (AT) for parallel dual-tubing wells (PDTW).
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CEO of Professional Science Editing for Scientists @ prosciediting.com