A procedure for the optimal determination of process synthesis, design and operation for both batch and continuous separation is presented.
The visualization method was applied to solve two types of problems, one is the determination of optimal operation point or region for a chemical process and the other is optimization of multi-objective problems (Zhang et al. 2010).
The information provided in this study is of great interest for the determination of optimal operation conditions and the design of new gasification concepts or the development of bioenergy carriers via pyrolysis technologies.
In order to obtain basic engineering data, continuous flow system is an effective process suitable for large-scale wastewater volumes and cyclic sorption/desorption: fixed-bed reactor is a simple method for the determination of bed operation life span and regeneration time (Cheknane et al. 2012).
Process synthesis methods enable the determination of unit operations and their interconnection into a process flowsheet, with associated design and operating parameters, and responding to given objectives.
In the sense of causal determination of technical operations, technology exonerates from contingency if it works.
The results of the two approaches lead to the determination of similar optimal operation conditions, which have been implemented for a new experimental phase.
First, a definition and determination of the optimal operation of the storage device is carried out through the formulation and deterministic solution of an optimization problem in GAMS.
However, such systems bring greater managerial complexity, and thus the determination of an appropriate operation strategy to set the recycling ratio of the old product and allocate the capacities of production to the new and remanufactured products is an important issue.
This study mainly focuses on a hybrid production system in which the determination of the optimal operation strategy is based on the consideration of the related costs, the uncertainty about recycling, the demand substitution, the capacity limitation, and the component durability.
