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Multisite objective function

In this final chapter, we study the multisite refinery and petrochemical integration problem, explained in Chapter 5, under uncertainty. The randomness considered includes both the objective function and right-hand side parameters of inequality constraints. As pointed out in the previous chapters, considering such strategic planning decisions requires proper handling of uncertainties as they play a maj or role in the final decision making process. [Pg.173]

Alkali Metal Cation-Cavitates Rigid, Macrospheroidal Multidentate, Multisite Zeolate Nanoreaction Chambers We have recently completed an extensive series of quantitative kinetic measurements in zeolite Y, for archetypical CO substitution reactions of Mo (CO) -M5 Y (M = Li, Na, K, Rb and Cs) by PMcj and CO. A key objective of this particular study was to evaluate how the energetics and dynamics of this reaction compared to the situation found in the gas and solution phases. Through such detailed studies of the rates of these reactions as a function of, for example, temperature, pressure, loading and cation type, it was anticipated that one could begin to identify the different ways in which the special environment found within the nanoreaction vessels of a zeolite host could influence the nature of chemical transformations contained therein. [Pg.315]


See other pages where Multisite objective function is mentioned: [Pg.141]    [Pg.142]    [Pg.159]    [Pg.141]    [Pg.142]    [Pg.159]    [Pg.76]    [Pg.455]   
See also in sourсe #XX -- [ Pg.65 ]

See also in sourсe #XX -- [ Pg.65 ]




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