Abstract: The batch distillation model is highly nonlinear due to the influence of mass and composition of the initial material to be separated. It is also caused by the thermodynamics of the system ...
Abstract: Based on theoretical analysis of dynamic mass balance and vapor-liquid phase balance, a state-space model of a methanol/water binary batch distillation pilot plant was developed with an ...
Some results have been hidden because they may be inaccessible to you
Show inaccessible results