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This study makes use of a novel methodology for the synthesis of heat exchanger networks, which is aimed at overcoming the shortcomings associated with the use of shortcut models to represent individual exchangers in the synthesis network.
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These correction factors enable the MINLP optimisation of the overall cost of the designed network, which uses only shortcut models of the individual exchangers, to be guided by more detailed models of the individual heat exchangers that comprise the network.
In this paper, we present a nonlinear programming approach to the conceptual design of integrated reaction-separation systems using shortcut models point of operation.
Besides, they provide accessibility through abundant use of shortcut keys for which blind users have to be trained.
This paper presents a numerical study of economics and environmental impact of an integrated steelmaking plant, using surrogate, empirical and shortcut models based on mass and energy balance equations for the unit operations.
Adjustments at the workplace and use of shortcuts are recommended.
Unfortunately, such haste can cause fatigue and the use of shortcuts that result in accidents.
In the first design step, the optimal flowsheet structure of simple columns is identified using a superstructure formulation and shortcut models based on rigorous thermodynamics.
This paper presents retrofit shortcut models for design of both reboiled and steam-stripped distillation columns.
The optimization framework includes shortcut models developed for the simulation of the existing distillation column, and a retrofit shortcut model for the heat exchanger network.
Shortcut models are well established for grassroots design of distillation columns and have been widely applied.
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