Distillation pinch points and more
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Angelo Lucia | Ross Taylor | Amit Amale | A. Lucia | R. Taylor | A. Amale
[1] Arthur W. Westerberg,et al. Homogeneous azeotropic distillation: Analysis of separation feasibility and consequences for entrainer selection and column design , 1994 .
[2] R. Bruce Eldridge,et al. Hybrid Separations/Distillation Technology. Research Opportunities for Energy and Emissions Reduction , 2005 .
[3] Michael F. Malone,et al. Nonideal Multicomponent Distillation: Use of Bifurcation Theory for Design , 1991 .
[4] Michael F. Malone,et al. Conceptual design of distillation systems , 2001 .
[5] S. Skogestad,et al. Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column , 2003 .
[6] Michael F. Malone,et al. Simulation of kinetic effects in reactive distillation , 2000 .
[7] Wolfgang Marquardt,et al. Shortcut methods for nonideal multicomponent distillation: 2. Complex columns , 1998 .
[8] Andreas A. Linninger,et al. Temperature Collocation Algorithm for Fast and Robust Distillation Design , 2004 .
[9] Y. H. Kim. A new fully thermally coupled distillation column with postfractionator , 2006 .
[10] Rafiqul Gani,et al. Simple new algorithm for distillation column design , 2000 .
[11] M. F. Malone,et al. Feasibility of separations for distillation of nonideal ternary mixtures , 1993 .
[12] H. Hausen,et al. Rektifikation von Dreistoffgemischen insbesondere von Sauerstoff-Stickstoff-Argon-Gemischen , 1935 .
[13] Michael F. Doherty,et al. Design and minimum reflux for heterogeneous azeotropic distillation columns , 1989 .
[14] R. D. Gray,et al. A modified Redlich‐Kwong equation of state , 1970 .
[15] A. Underwood,et al. Fractional Distillation of Multicomponent Mixtures , 1949 .
[16] Michael F. Doherty,et al. A simple exact method for calculating tangent pinch points in multicomponent nonideal mixtures by bifurcation theory , 1986 .
[17] Arthur W. Westerberg,et al. Graphical design applied to MTBE and methyl acetate reactive distillation processes , 2001 .
[18] S. Glanz,et al. Calculating minimum reflux of nonideal multicomponent distillation using eigenvalue theory , 1994 .
[19] Angelo Lucia,et al. Geometry of Separation Boundaries: Systems with Reaction , 2006 .
[20] Domingos Barbosa,et al. Design and minimum-reflux calculations for single-feed multicomponent reactive distillation columns , 1988 .
[21] J. Prausnitz. Computer calculations for multicomponent vapor-liquid and liquid-liquid equilibria , 1980 .
[22] Alfons Vogelpohl. Die näherungsweise Berechnung der Rektifikation von Gemischen mit binären Azeotropen , 1974 .
[23] E. Blass,et al. A review on minimum energy calculations for ideal and nonideal distillations , 1995 .
[24] V. Rico-RamOH. Multicomponent Distillation , 2003 .
[25] Angelo Lucia,et al. The geometry of separation boundaries: I. Basic theory and numerical support , 2006 .
[26] Neal R. Amundson,et al. On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade: Part IV. The calculation of the minimum reflux ratio , 1955 .
[27] M. F. Malone,et al. Attainable regions for reaction with separation , 1997 .
[28] C. Gibson,et al. Calculation of Minimum Reflux in Distillation Columns , 1950 .
[29] Angelo Lucia,et al. Energy Efficient Hybrid Separation Processes , 2006 .
[30] Michael F. Doherty,et al. Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns , 1985 .
[31] Wolfgang Marquardt,et al. Minimum energy demand and split feasibility for a class of reactive distillation columns , 2004 .
[32] Michael F. Doherty,et al. Geometric behavior and minimum flows for nonideal multicomponent distillation , 1990 .
[33] E. Blass,et al. Minimum reflux calculations for nonideal mixtures using the reversible distillation model , 1991 .
[34] N. L. Franklin,et al. The interpretation of minimum reflux conditions in multi-component distillation , 1997 .