Download Advanced Distillation Technologies: Design, Control and by Anton A. Kiss PDF

By Anton A. Kiss

Distillation has traditionally been the most technique for keeping apart combos within the chemical approach undefined. even if, regardless of the pliability and frequent use of distillation approaches, they nonetheless stay tremendous strength inefficient. elevated optimization and novel distillation ideas can carry gigantic merits, not only by way of considerably reduce strength use, but in addition in lowering capital funding and bettering eco-efficiency. whereas prone to stay the separation expertise of selection for the following couple of a long time, there's no doubt that distillation applied sciences want to make radical adjustments for you to meet the calls for of the energy-conscious society.

Advanced Distillation applied sciences: layout, keep an eye on and purposes gives a deep and wide perception into built-in separations utilizing non-conventional preparations, together with either present and upcoming technique intensification applied sciences.

It includes:

  • Key options in distillation technology
  • Principles of layout, keep watch over, sizing and economics of distillation
  • Dividing-wall column (DWC) – layout, configurations, optimum operation and effort effective and complex control
  • DWC purposes in ternary separations, azeotropic, extractive and reactive distillation
  • Heat built-in distillation column (HIDiC) – layout, apparatus and configurations
  • Heat-pump assisted purposes (MVR, TVR, AHP, CHRP, TAHP and others)
  • Cyclic distillation expertise – thoughts, modeling process, layout and keep an eye on issues
  • Reactive distillation – basics, gear, functions, feasibility scheme
  • Results of rigorous simulations in Mathworks Matlab & Simulink, Aspen Plus, Dynamics and customized Modeler

Containing plentiful examples and commercial case reports, it is a distinct source that tackles the main complicated distillation applied sciences – the entire means from the conceptual layout to sensible implementation.

The writer of Advanced Distillation Technologies, Dr. Ir. Anton A. Kiss, has been presented the Hoogewerff Jongerenprijs 2013. discover extra (website in Dutch)...

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Extra resources for Advanced Distillation Technologies: Design, Control and Applications

Sample text

Ternary azeotrope: m (minimum), M (maximum), or S (intermediate). 11b the class is 311-S. The first digit represents the maximumboiling azeotrope acetone/chloroform, the second the minimum-boiling azeotrope chloroform/methanol, the third the minimum-boiling azeotrope acetone/methanol, while the last letter S signifies the ternary saddle azeotrope (Doherty and Malone, 2001; Dimian, 2003). As explained earlier, all residue curves start at the lightest component and move toward the heaviest component.

3 Approximate Multicomponent Methods Several simple approximate methods were developed for analyzing multicomponent systems, long before the availability of computers for rigorous analysis—the best known being the Fenske–Underwood– Gilliland (FUG) shortcut method. , reflux ratios and the corresponding vapor boil-up and reboiler heat input): Fenske equation for minimum number of trays: The minimum number of trays corresponds to total reflux operation (an infinite reflux ratio). 55) N min þ 1 ¼ log aLK;HK where Nmin is the minimum number of stages required, xD,LK is the mole fraction of the light-key (LK) component at the top of the column, xD,HK is the mole fraction of the heavy-key (HK) component at the top of the column, xD,HK is the mole fraction of the heavy-key component at the bottom of the column, xB,LK is the mole fraction of the light-key component at the bottom of the column, and aLK,HK is the relative volatility between the LK and HK components.

Although it is limited to binary systems, the effects of parameters can be extended to multicomponent systems. The basic effects can be summarized as follows:  The easier the separation, the fewer trays are required and the lower the required reflux ratio (also translated into lower energy requirements).  The higher the desired product purities, the more trays are required—but the required reflux ratio does not increase significantly as the product purities increase.  There is an engineering trade-off between the number of trays and the reflux ratio.

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