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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/18743
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dc.contributor.advisorCrowe, C. M.-
dc.contributor.authorLord, Stephen-
dc.date.accessioned2016-01-18T19:00:27Z-
dc.date.available2016-01-18T19:00:27Z-
dc.date.issued1970-09-
dc.identifier.urihttp://hdl.handle.net/11375/18743-
dc.description.abstract<p> The various criteria and methods suggested in the literature for choosing the optimum sequence of calculation are compared. They are then analysed using the results of runs on three different simulations. Two techniques of convergence are used, and it is found that Geometric Convergence Promotion will improve the rate of convergence compared to Direct Substitution for any feasible sequence. It is also shown that the optimal sequences of calculation are different for the two techniques. </p> <p> It is concluded that the Minimum Cut Streams criterion is the best to use for Direct Substitution, but that the use of the feasible Set criterion and Convergence Promotion will yield better convergence. The iterative improvement of convergence is discussed, and it is concluded that the available time is best spent on improving the starting point and the Convergence Promotion technique rather than on changing the sequence of calculation. </p>en_US
dc.language.isoenen_US
dc.subjectchemical planten_US
dc.subjectsimulationsen_US
dc.subjectchemical engineeringen_US
dc.subjectconvergenceen_US
dc.titlelmprovement of Convergence in the Simulation of Complex Chemical Plantsen_US
dc.contributor.departmentChemical Engineeringen_US
dc.description.degreetypeThesisen_US
dc.description.degreeMaster of Engineering (MEngr)en_US
Appears in Collections:Open Access Dissertations and Theses

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