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The continuous cyclic operation of a packed-bed chemical looping combustion process is described using a basic reactor model.
The process is described using a transfer function and sampled into a discrete model for computer control design.
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The moisture transfer process was described using a serial resistance model, which involves the convective moisture resistance in the channel, the moisture resistance through membrane, and the moisture resistance caused by the air gap.
The process was described using an Auto Regressive Integrated Moving Average eXogenous (ARIMAX) model.
The maintenance process is described using the competing risks framework under imperfect maintenance.
Further, the general design process is described using analysis, synthesis, and evaluation.
However, the kinetics process there is described using a deterministic model.
The overall dissolution process was described using the population balance equation (PBE) coupled with a mass balance equation to account for the evolution of the particle size distribution (PSD) of olivine.
The sorption capacity of the material was measured (83.98 mg/g), and the entire process was described using appropriate kinetic models.
The metabolic process can be described using a dynamic model involving nonlinear differential equations.
The kinetic behavior of the degradation process can be described using a pseudo-first-order kinetic model [42].
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com