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The determination of operating zone is a complex and time-taking process.
The design and commissioning of fed-batch struvite crystallization included the determination of operating supersaturation of struvite crystallization, suitable seed materials and the composition of feed solution.
Determination of operating supersaturation of struvite crystallization was conducted by two steps including thermodynamic simulation using gPROMS2 (process simulation software) along with a set of batch experiments.
The correlation is useful for the design of filtration devices and the determination of operating conditions in filtration processes for both dust aerosols and colloidal suspensions.
Considering the rapid variation of waste composition and the more severe regulation trend of pollutant emission in this country, the importance of the development of a reliable computer program for a full-scale, stoker-type incinerator cannot be emphasized too much especially in the view of proper design and optimal determination of operating condition of existing and future constructed facility.
This kind of problem is commonly found in chemical engineering since process design and operability involve structural and decisional choices as well as the determination of operating conditions.
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Therefore, studies of column adsorption systems are needed, in which the most important parameter to be determined is the column breakthrough curves, that is useful for the determination of the operating life span of the fixed adsorbent bed (Bielicka-Daszkiewicz and Voelkel 2009; Naja and Volesky 2006; Chu 2004).
After theoretical and experimental determination of thermodesorber operating characteristics (temperature profile, losses, removal of desorbed material), examples of applications in several fields are given.
Frequently the design of schemes for correction of aberrations or the determination of possible operating ranges for beamlines and cells in synchrotrons exhibit multitudes of possibilities for their correction, usually appearing in disconnected regions of parameter space which cannot be directly qualified by analytical means.
The present study deals with the determination of optimal values of operating parameters i.e. temperature (60 100 °C), pressure (200 350 bar), particle size (0.5 1.0 mm), flow rate-CO2 (5.0 15 g/min) and co-solvent (0.0 10%) leading to the best cumulative extraction yield (CEY) during a supercritical CO2 extraction of oil from Pongamia pinnata (L).
On the other hand, it is not always economical nor feasible to use the most sophisticated models for a range of different applications, such as process and equipment design, the determination of optimal operating policies, model-based control, etc., and the model complexity has to be adapted to the purpose.
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