Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

The Superstructure Approach to Heat Exchanger Network Design

Q = heat exchanger duty U = overall heat transfer coefficient A Tlm = logarithmic mean temperature difference [Pg.417]

Note that the A Tmin for the problem must be fixed in order to remain an MILP problem. Fixing A Tmin fixes the composite curves and the temperatures across each enthalpy interval or block. Unfortunately, this would not necessarily lead to the best network, as the initial superstructure was already simplified with many structural options missing. But this can be allowed for by first carrying out the [Pg.418]

A simplified superstructure is first optimized using MILP. [Pg.418]

The major advantage of the superstructure approach to heat exchanger network design is that, in principle, it is capable [Pg.418]

Any Parallel, Series-parallel or Parallel-series Arrangement [Pg.418]




SEARCH



Approach to Heat-Exchanger Design

Design approach

Heat Exchanger Networks - Network Design

Heat design

Heat exchanger network design

Heat exchanger network design superstructure

Heat exchanger networks

Network design

Superstructure

The heat exchanger network

© 2024 chempedia.info