Probabilistic reactor design in the framework of elementary process functions

Achenie, 1990, A superstructure based approach to chemical reactor network synthesis, Comput. Chem. Eng., 14, 23, 10.1016/0098-1354(90)87003-8 Behr, 2002, Temperature-dependent multicomponent solvent systems • an alternative concept for recycling homogeneous catalysts, Chem. Eng. Technol., 25, 143, 10.1002/1521-4125(200202)25:2<143::AID-CEAT143>3.0.CO;2-O Behr, 2008, Advances in thermomorphic liquid/liquid recycling of homogeneous transition metal catalysts, J. Mol. Catal. A: Chem., 285, 20, 10.1016/j.molcata.2008.01.021 Beyer, 2007, Robust optimization • a comprehensive survey, Comput. Methods Appl. Mech. Eng., 196, 3190, 10.1016/j.cma.2007.03.003 Bhaskar, 2000, Applications of multiobjective optimization in chemical engineering, Rev. Chem. Eng., 16, 1, 10.1515/REVCE.2000.16.1.1 Biegler, 1983 Bohnen, 2002, Hydroformylation of alkenes: an industrial view of the status and importance, Adv. Catal., 47, 1 Enevoldsen, 1994, Reliability-based optimization in structural engineering, Struct. Saf., 15, 169, 10.1016/0167-4730(94)90039-6 Flassig, 2012, Optimal design of stimulus experiments for robust discrimination of biochemical reaction networks, Bioinformatics, 28, 3089, 10.1093/bioinformatics/bts585 Freund, 2011, Model-based reactor design based on the optimal reaction route, Chem. Ingen. Tech., 83, 420, 10.1002/cite.201000195 Freund, 2008, Towards a methodology for the systematic analysis and design of efficient chemical processes: Part 1, From unit operations to elementary process functions, Chem. Eng. Process.: Process Intens., 47, 2051, 10.1016/j.cep.2008.07.011 Glasser, 1987, A geometric approach to steady flow reactors: the attainable region and optimization in concentration space, Indus. Eng. Chem. Res., 26, 1803, 10.1021/ie00069a014 Heine, 2006, Robust model predictive control using the unscented transformation, 224 Hentschel, 2015, Model-based identification and experimental validation of the optimal reaction route for the hydroformylation of 1-dodecene, Indus. Eng. Chem. Res., 10.1021/ie504388t Hentschel, 2014, Simultaneous design of the optimal reaction and process concept for multiphase systems, Chem. Eng. Sci., 115, 69, 10.1016/j.ces.2013.09.046 Hillestad, 2010, Systematic staging in chemical reactor design, Chem. Eng. Sci., 65, 3301, 10.1016/j.ces.2010.02.021 Horn, 1964, Attainable regions in chemical reaction techniques, 293 Julier, 2000, A new method for the nonlinear transformation of means and covariances in filters and estimators, IEEE Trans. Autom. Control, 45, 477, 10.1109/9.847726 Julier, 1996 Kiedorf, 2014, Kinetics of 1-dodecene hydroformylation in a thermomorphic solvent system using a rhodium-biphephos catalyst, Chem. Eng. Sci., 115, 31, 10.1016/j.ces.2013.06.027 Kohlpaintner, 2001, Aqueous biphasic catalysis: Ruhrchemie/Rhône-Poulenc oxo process, Appl. Catal. A: Gen., 221, 219, 10.1016/S0926-860X(01)00791-8 Kokossis, 1991, Synthesis of isothermal reactor•separator•recycle systems, Chem. Eng. Sci., 46, 1361, 10.1016/0009-2509(91)85063-4 Li, 2008, Chance constrained programming approach to process optimization under uncertainty, Comput. Chem. Eng., 32, 25, 10.1016/j.compchemeng.2007.05.009 Markert, 2013, Analysis of the reaction network for the Rh-catalyzed hydroformylation of 1-dodecene in a thermomorphic multicomponent solvent system, Appl. Catal. A: Gen., 462, 287, 10.1016/j.apcata.2013.04.005 Marler, 2004, Survey of multi-objective optimization methods for engineering, Struct. Multidiscip. Optim., 26, 369, 10.1007/s00158-003-0368-6 Mulvey, 1995, Robust optimization of large-scale systems, Oper. Res., 43, 264, 10.1287/opre.43.2.264 Peschel, 2010, Methodology for the design of optimal chemical reactors based on the concept of elementary process functions, Indus. Eng. Chem. Res., 49, 10535, 10.1021/ie100476q Peschel, 2011, Analysis and optimal design of an ethylene oxide reactor, Chem. Eng. Sci., 66, 6453, 10.1016/j.ces.2011.08.054 Rossner, 2010, Quality-by-design using a Gaussian mixture density approximation of biological uncertainties, Comput. Appl. Biotechnol., 7 Scähfer, 2012, Hydroformylation of 1-dodecene in the thermomorphic solvent system dimethylformamide/decane. Phase behavior•reaction performance•catalyst recycling, Indus. Eng. Chem. Res., 51, 10296, 10.1021/ie300484q Schenkendorf, 2009, Optimal experimental design with the sigma point method, IET Syst. Biol., 3, 10, 10.1049/iet-syb:20080094 Schuâller, 2008, Computational methods in optimization considering uncertainties • an overview, Comput. Methods Appl. Mech. Eng., 198, 2, 10.1016/j.cma.2008.05.004 Sobol
tm), 2001, Global sensitivity indices for nonlinear mathematical models and their Monte Carlo estimates, Math. Comput. Simul., 55, 271, 10.1016/S0378-4754(00)00270-6 Srinivasan, 2003, Dynamic optimization of batch processes: II. Role of measurements in handling uncertainty, Comp. Chem. Eng., 27, 27, 10.1016/S0098-1354(02)00117-5 Srinivasan, 2003, Dynamic optimization of batch processes: I. Characterization of the nominal solution, Comput. Chem. Eng., 27, 1, 10.1016/S0098-1354(02)00116-3 Telen, 2014, Robustifying optimal experiment design for nonlinear, dynamic (bio) chemical systems, Compu. Chem. Eng., 71, 415, 10.1016/j.compchemeng.2014.09.006 Wiebus, 1994, Die großtechnische Oxosynthese mit immobilisiertem Katalysator, Chem. Ingen. Tech., 66, 916, 10.1002/cite.330660704 Xie, 2013, Enhanced hydroformylation by carbon dioxide-expanded media with soluble Rh complexes in nanofiltration membrane reactors, AIChE J., 59, 4287, 10.1002/aic.14142