The two decomposition methods Dulmage-Mendelsohn (DM) decomposition and bordered block transformation (BBTF) have been examined on their capabilities to eliminate convergence problems during the iteration of large, nonlinear equation systems as they occur frequently in process modeling. They both divide the overall system into lower dimensional subsystems, which can be solved separately in sequence. Exemplarily these methods were applied on the model of a reactive distillation column, where the decomposed systems show a higher robustness with respect to systematically selected initial points compared to the original system. Nevertheless, the improvement in DM seems small since a large subsystem with 576 of the 664 model equations remains. T...
Includes bibliographical references (leaves 146-150)The Newton-Raphson procedure is used to solve th...
This work addresses a number of fundamental problems relevant to the solution of equation systems en...
A nonlinear system of equations is said to be reducible if it can be divided into m blocks (m>1) in ...
The initialization of process models for chemical engineering systems is often a challenge. While de...
To meet the needs of plant wide dynamic process simulation of today's complex, highly interconnected...
For the plantwide dynamic simulations in the chemical process industry, a parallel approach using a ...
AbstractThe decomposition method can be an effective procedure for solution of nonlinear and/or stoc...
The chemical industry has historically favored increasingly larger plant designs to lower production...
AbstractThe concept of treating multicomponent distillation problems as nonlinear boundary value pro...
AbstractThe author's decomposition method [1] provides a new, efficient computational procedure for ...
Abstract The aim of this work is to improve the overall robustness in equation-oriented chemical eng...
In this article we consider iterative operator-splitting methods for nonlinear differential equation...
AbstractNonlinear dynamical systems are shown to represent severe difficulties in modeling. When in ...
Application of the Hammerstein Block-oriented Exact Solution Technique (H-BEST) to a real industrial...
The design of chemical engineering process equipment routinely necessitates the solution of large sy...
Includes bibliographical references (leaves 146-150)The Newton-Raphson procedure is used to solve th...
This work addresses a number of fundamental problems relevant to the solution of equation systems en...
A nonlinear system of equations is said to be reducible if it can be divided into m blocks (m>1) in ...
The initialization of process models for chemical engineering systems is often a challenge. While de...
To meet the needs of plant wide dynamic process simulation of today's complex, highly interconnected...
For the plantwide dynamic simulations in the chemical process industry, a parallel approach using a ...
AbstractThe decomposition method can be an effective procedure for solution of nonlinear and/or stoc...
The chemical industry has historically favored increasingly larger plant designs to lower production...
AbstractThe concept of treating multicomponent distillation problems as nonlinear boundary value pro...
AbstractThe author's decomposition method [1] provides a new, efficient computational procedure for ...
Abstract The aim of this work is to improve the overall robustness in equation-oriented chemical eng...
In this article we consider iterative operator-splitting methods for nonlinear differential equation...
AbstractNonlinear dynamical systems are shown to represent severe difficulties in modeling. When in ...
Application of the Hammerstein Block-oriented Exact Solution Technique (H-BEST) to a real industrial...
The design of chemical engineering process equipment routinely necessitates the solution of large sy...
Includes bibliographical references (leaves 146-150)The Newton-Raphson procedure is used to solve th...
This work addresses a number of fundamental problems relevant to the solution of equation systems en...
A nonlinear system of equations is said to be reducible if it can be divided into m blocks (m>1) in ...