Journal ArticleDOI
Design of resilient processing plants—III: A general framework for the assessment of dynamic resilience
TLDR
It is shown that dynamic resilence is determined by characteristics inherent in the system and that it is independent of the imposed controller structure and type.About:
This article is published in Chemical Engineering Science.The article was published on 1983-01-01. It has received 291 citations till now. The article focuses on the topics: Operability.read more
Citations
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Plantwide control: the search for the self-optimizing control structure
TL;DR: A systematic procedure for finding suitable controlled variables based on only steady-state information is presented and important steps are degree of freedom analysis, definition of optimal operation (cost and constraints), and evaluation of the loss when the controlled variables are kept constant rather than optimally adjusted.
Journal ArticleDOI
Survey A review of methods for input/output selection
Marc van de Wal,Bram de Jager +1 more
TL;DR: A set of criteria is proposed that a good IO selection method should possess, which is used to assess and compare the methods and it could be used as a guideline for new methods.
Journal ArticleDOI
A review of recent design procedures for water networks in refineries and process plants
TL;DR: In this paper, a review of the procedures to design and retrofit water networks is presented, and the roadmap towards zero liquid discharge and energy integrated solutions are briefly outlined emphasizing the main trend leaning towards the use of mathematical programming.
Journal ArticleDOI
Applications of multiobjective optimization in Chemical Engineering
TL;DR: The general background of this area is presented, followed by a description of how the results can be described in terms of Pareto sets, and the several methods available for generating optimal solutions.
Journal ArticleDOI
Analyzing the interaction of design and control—1. A multiobjective framework and application to binary distillation synthesis
TL;DR: In this paper, a systematic procedure for incorporating open-loop steady-state controllability measures within the mathematical programming approach of process synthesis is presented, which translates a superstructure of design alternatives into a multiobjective mixed-integer nonlinear (MINLP) optimization problem.
References
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Journal ArticleDOI
Internal model control. A unifying review and some new results
Carlos E. García,Manfred Morari +1 more
Journal ArticleDOI
The pinch design method for heat exchanger networks
B. Linnhoff,E. Hindmarsh +1 more
TL;DR: In this article, a novel method is presented for the design of heat exchanger networks, which combines sufficient simplicity to be used by hand with near certainty to identify "best" designs, even for large problems.
Journal ArticleDOI
Terminal composition control of a binary distillation column
R.K. Wood,M.W. Berry +1 more
TL;DR: In this article, a pilot scale binary distillation column operated under the control of an IBM 1800 digital computer has been studied for disturbances in feed flow rate, and two alternate control systems, namely a noninteracting control system and a ratio control system were evaluated.
Journal ArticleDOI
Optimal process design under uncertainty
TL;DR: In this article, a rigorous mathematical formulation for the problem of optimal design under uncertainty is presented, which involves a nonlinear infinite programming problem in which an optimization is performed on the set of design and control variables, such that the inequality constraints of the chemical plant are satisfied for every parameter value that belongs to a specified polyhedral region.