Variable density fluid reactor network synthesis—Construction of the attainable region through the IDEAS approach
暂无分享,去创建一个
[1] Vasilios Manousiouthakis,et al. IDEAS approach to the synthesis of globally optimal separation networks: application to chromium recovery from wastewater , 2003 .
[2] L. Biegler,et al. Constructive targeting approaches for the synthesis of chemical reactor networks , 1992 .
[3] J. D. Paynter,et al. Determination of optimal reactor type , 1970 .
[4] Diane Hildebrandt,et al. Choosing optimal control policies using the attainable region approach , 1999 .
[5] Vasilios Manousiouthakis,et al. IDEAS approach to process network synthesis: Application to multicomponent MEN , 2000 .
[6] Lorenz T. Biegler,et al. Developing Targets for the Performance Index of a Chemical Reactor Network: Isothermal Systems , 1988 .
[7] Vasilios Manousiouthakis,et al. IDEAS approach to process network synthesis: minimum utility cost for complex distillation networks , 2002 .
[8] Martin Feinberg. Optimal reactor design from a geometric viewpoint — III. Critical CFSTRs , 2000 .
[9] Vasilios Manousiouthakis,et al. Infinite DimEnsionAl State-space approach to reactor network synthesis: application to attainable region construction , 2002 .
[10] Antonis C. Kokossis,et al. Scoping and screening complex reaction networks using stochastic optimization , 1999 .
[11] R. Jackson. Optimization of chemical reactors with respect to flow configuration , 1968 .
[12] Vasilios Manousiouthakis,et al. IDEAS Approach to Process Network Synthesis: Minimum Plate Area for Complex Distillation Networks with Fixed Utility Cost† , 2002 .
[13] D. Glasser,et al. A geometric approach to steady flow reactors: the attainable region and optimization in concentration space , 1987 .
[14] Vasilios Manousiouthakis,et al. Globally optimal power cycle synthesis via the Infinite-DimEnsionAl State-space (IDEAS) approach featuring minimum area with fixed utility , 2003 .
[15] Magne Hillestad. A systematic generation of reactor designs: II. Non-isothermal conditions , 2005, Comput. Chem. Eng..
[16] Magne Hillestad. A systematic generation of reactor designs: I. Isothermal conditions , 2004, Comput. Chem. Eng..
[17] Christodoulos A. Floudas,et al. Optimization of complex reactor networks—I. Isothermal operation , 1990 .
[18] S L Ong,et al. Optimization of CSTRs in series by dynamic programming , 1986, Biotechnology and bioengineering.
[19] Larry A. Taylor,et al. The Shrink-Wrap algorithm for the construction of the attainable region: an application of the IDEAS framework , 2004, Comput. Chem. Eng..
[20] Lanny D. Schmidt,et al. The engineering of chemical reactions , 1997 .
[21] M. Feinberg,et al. Optimal reactor design from a geometric viewpoint—I. Universal properties of the attainable region , 1997 .
[22] James B. Rawlings,et al. Chemical Reactor Analysis and Design Fundamentals , 2002 .
[23] G. Froment,et al. Chemical Reactor Analysis and Design , 1979 .
[24] Antonis C. Kokossis,et al. Nonisothermal synthesis of homogeneous and multiphase reactor networks , 2000 .
[25] Martin Feinberg. Optimal reactor design from a geometric viewpoint. Part II. Critical sidestream reactors , 2000 .
[26] O. Levenspiel. Chemical Reaction Engineering , 1972 .
[27] L. Biegler,et al. Algorithmic synthesis of chemical reactor networks using mathematical programming , 1986 .
[28] Martin Feinberg. Recent results in optimal reactor synthesis via attainable region theory , 1999 .
[29] A. L. Ravimohan. Optimization of chemical reactor networks with respect to flow configuration , 1971 .
[30] Diane Hildebrandt,et al. Synthesis of chemical reactor networks , 1995 .
[31] Lorenz T. Biegler,et al. A superstructure based approach to chemical reactor network synthesis , 1990 .
[32] Diane Hildebrandt,et al. Linear programming formulations for attainable region analysis , 2002 .
[33] Ernest J. Henley,et al. Separation Process Principles , 1998 .
[34] Diane Hildebrandt,et al. The attainable region for segregated, maximum mixed, and other reactor models , 1994 .
[35] D. Glasser,et al. Geometry of the Attainable Region Generated by Reaction and Mixing: With and without Constraints , 1990 .