1993
DOI: 10.1016/0098-1354(93)85011-a
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From nonlinear programming theory to practical optimization algorithms: A process engineering viewpoint

Abstract: As process optimization becomes an established and mature technology for process simulation, analysis and operation, it becomes important to consider larger and more creative problem formulations and applications, as well as the development of efficient algorithms to tackle them. Here, some novel process optimization applications are briefly reviewed in the following areas of process design and analysis:• treatment of constrained and nonsmooth simulation problems, particularly in phase equilibrium • synthesis … Show more

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Cited by 10 publications
(12 citation statements)
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“…Three main variants of this method are direct single shooting, direct multiple shooting, and orthogonal collocation [see, e.g., 27,28]. The focus in this section is on the former approach, also known as direct sequential approach, but the following ideas can be readily extended to the other two approaches.…”
Section: Direct Two-layer Schemementioning
confidence: 99%
See 3 more Smart Citations
“…Three main variants of this method are direct single shooting, direct multiple shooting, and orthogonal collocation [see, e.g., 27,28]. The focus in this section is on the former approach, also known as direct sequential approach, but the following ideas can be readily extended to the other two approaches.…”
Section: Direct Two-layer Schemementioning
confidence: 99%
“…Moreover, in using derivative-based NLP techniques such as SQP, the first-order derivatives-and the second-order derivatives too if necessary-can be obtained from the numerical integration of the associated state-sensitivity or adjoint equations [28].…”
Section: Direct Two-layer Schemementioning
confidence: 99%
See 2 more Smart Citations
“…If a plant model is available, numerical optimization techniques can be used to compute a local [1] or even the global [2] solution. The problem to be solved then reads: u * (θ ) := arg min u φ (u, θ ) subject to g (u, θ ) ≤ 0, (1.2) where φ is the modeled cost function, g is the n g -dimensional vector of modeled plant constraints, and θ is an n θ -dimensional vector of model parameters.…”
Section: Introductionmentioning
confidence: 99%