Understanding Distillation Using Column Profile Maps

Understanding Distillation Using Column Profile Maps

Volumn , Issue , 2012, Pages

  Beneke, Daniel ^a   Peters, Mark ^a   Glasser, David ^a   Hildebrandt, Diane ^a  

^a UNIVERSITY OF THE WITWATERSRAND   (South Africa)

Author keywords

[No Author keywords available]

Indexed keywords

EID: 84891584676     PISSN: None     EISSN: None     Source Type: Book    
DOI: 10.1002/9781118477304     Document Type: Book

References (184)

1. Humphrey, J.L., Separation processes: Playing a critical role. Chemical Engineering Progress, 1995, 91(10):31-41.
2. Soave, G. and J.A. Feliu, Saving energy in distillation towers by feed splitting. Applied Thermal Engineering, 2002, 22(8):889-896.
3. Mix, T.W. and J.S. Dweck, Conserving Energy in Distillation. 1982, Cambridge, MA: MIT Press. p. 104.
4. McCabe, W.L. and E.W. Thiele, Graphical design of fractionating columns. Industrial and Engineering Chemistry, 1925, 17(6):606-611.
5. Underwood, A.J.V., Fractional distillation of multi-component mixtures-Calculation of minimum reflux ratio. Institute of Petroleum-Journal, 1946, 32(274):614-626.
6. Huss, R.S. and A.W. Westerberg, Collocation methods for distillation design. 1. Model description and testing. Industrial & Engineering Chemistry Research, 1996, 35(5):1603-1610.
7. Halvorsen, I.J. and S. Skogestad, Minimum energy consumption in multicomponent distillation. 1. Vmin diagram for a two-product column. Industrial & Engineering Chemistry Research, 2003, 42(3):596-604.
8. Halvorsen, I.J. and S. Skogestad, Minimum energy consumption in multicomponent distillation. 2. Three-product Petlyuk arrangements. Industrial & Engineering Chemistry Research, 2003, 42(3):605-615.
9. Engelien, H.K. and S. Skogestad, Minimum energy diagrams for multieffect distillation arrangements. AIChE Journal, 2005, 51(6):1714-1725.
10. Engelien, H.K. and S. Skogestad, Multi-effect distillation applied to an industrial case study. Chemical Engineering and Processing, 2005, 44(8):819-826.
11. Wolff, E.A. and S. Skogestad, Operation of integrated three-product (Petlyuk) distillation columns. Industrial & Engineering Chemistry Research, 1995, 34(6):2094-2103.
12. Fidkowski, Z. and L.W. Krolikowski, Minimum energy requirements of thermally coupled distillation systems. AIChE Journal, 1987, 33(4):643-653.
13. Alstad, V., I.J. Halvorsen, and S. Skogestad, Optimal operation of a Petlyuk distillation column: Energy savings by over-fractionating, in Computer Aided Chemical Engineering, A. Barbosa-Povoa and H. Matos, editors. 2004, Elsevier. pp. 547-552.
14. Carlberg, N.A. and A.W.Westerberg, Temperature-heat diagrams for complex columns; Underwood's method for side strippers and enrichers. Industrial & Engineering Chemistry Research, 1989, 28(9):1379-1385.
15. Glinos, K. and M.F. Malone, Minimum vapor flows in a distillation column with a sidestream stripper. Industrial & Engineering Chemistry, Process Design and Development, 1985, 24:1087-1090.
16. Glinos, K.N. and M.F. Malone, Design of sidestream distillation columns. Industrial & Engineering Chemistry, Process Design and Development, 1985, 24(3):822-828.
17. Kiva, V.N., E.K. Hilmen, and S. Skogestad, Azeotropic phase equilibrium diagrams: A survey. Chemical Engineering Science, 2003, 58(10):1903-1953.
18. Lucia, A., A. Amale, and R. Taylor, Energy efficient hybrid separation processes. Industrial & Engineering Chemistry Research, 2006, 45(25):8319-8328.
19. Van Dongen, D.B. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 1. Problem formulation for a single column. Industrial & Engineering Chemistry, Fundamentals, 1985, 24(4):454-463.
20. Doherty, M.F. and G.A. Caldarola, Design and synthesis of homogeneous azeotropic distillations. 3. The sequencing of columns for azeotropic and extractive distillations. Industrial & Engineering Chemistry, Fundamentals, 1985, 24(4):474-485.
21. Levy, S.G., D.B.Van Dongen, and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns. Industrial & Engineering Chemistry, Fundamentals, 1985, 24(4):463-474.
22. Levy, S.G. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 4. Minimum reflux calculations for multiple-feed columns. Industrial & Engineering Chemistry, Fundamentals, 1986, 25(2):269-279.
23. Knight, J.R. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 5. Columns with non-negligible heat effects. Industrial & Engineering Chemistry, Fundamentals, 1986, 25(2):279-289.
24. Krishnamurthy, R. and R. Taylor, Simulation of packed distillation and absorption columns. Industrial & Engineering Chemistry, Process Design and Development, 1985, 24(3):513-524.
25. Taylor, R., H.A. Kooijman, and J.S. Hung, A second generation nonequilibrium model for computer simulation of multicomponent separation processes. Computers & Chemical Engineering, 1994, 18(3):205-217.
26. Kooijman, H.A. and R. Taylor, Nonequilibrium model for dynamic simulation of tray distillation columns. AIChE Journal, 1995, 41(8):1852-1863.
27. Kooijman, H., Dynamic nonequilibrium column simulation, in Chemical Engineering. 1995, Potsdam, NY: Clarkson University. p. 144.
28. Taylor, R., R. Krishna, and H. Kooijman, Real-world modeling of distillation. Chemical Engineering Progress, 2003, 99(7):28-39.
29. Holland, S.T., et al., Column profile maps. 2. Singular points and phase diagram behaviour in ideal and nonideal systems. Industrial & Engineering Chemistry Research, 2004, 43(14):3590-3603.
30. Tapp, M., et al., Column profile maps. 1. Derivation and Interpretation. Industrial & Engineering Chemistry Research, 2004, 43(2):364-374.
31. Holland, S.T., et al., Complex column design by application of column profile map techniques: Sharp-split Petlyuk column design. Industrial & Engineering Chemistry Research, 2010, 49(1):327-349.
32. Holland, S.T., et al., Novel separation system design using "moving triangles". Computers & Chemical Engineering, 2004, 29(1):181-189.
33. Mulopo, J.L., D. Hildebrandt, and D. Glasser, Reactive residue curve map topology: Continuous distillation column with non reversible kinetics. Computers & Chemical Engineering, 2008, 32(3):622-629.
34. Peters, M., et al., Derivation and properties of membrane residue curve maps. Industrial & Engineering Chemistry Research, 2006, 45(26):9080-9087.
35. Peters, M., et al., Application of membrane residue curve maps to batch and continuous processes. Industrial & Engineering Chemistry Research, 2008, 47(7):2361-2376.
36. Mulopo, J.L., et al., Experimental simulation of distillation column concentration profiles using a batch apparatus: Columns stripping section. Chemical Engineering Science, 2005, 60(24):6815-6823.
37. Modise, T., et al., Experimental simulation of distillation column section profiles using a batch apparatus. Industrial & Engineering Chemistry Research, 2005, 44:7511-7519.
38. Modise, T., et al., Experimental measurement of the saddle node region in a distillation column profile map by using a batch apparatus. Chemical Engineering Research and Design, 2007, 85(1):24-30.
39. Hömmerich, U. and R. Rautenbach, Design and optimization of combined pervaporation/ distillation processes for the production of MTBE. Journal of Membrane Science, 1998, 146(1):53-64.
40. Tapp, M., et al., Make distillation boundaries work for you! in Computer Aided Chemical Engineering, A. Barbosa-Povoa and H. Matos, editors. 2004, Elsevier. pp. 499-504.
41. Kister, H.Z., Distillation Design. 1992, McGraw-Hill.
42. Kister, H., Distillation Operation. 1990, McGraw-Hill Professional.
43. Doherty, M.F. and M.F. Malone, Conceptual Design of Distillation Systems. 1st ed. 2001, New York, NY: McGraw-Hill. p. 568.
44. Seader, J.D. and E.J. Henley, Separation Process Principles. 2nd ed. 2006, Hoboken, NJ: Wiley. p. 756.
45. Petlyuk, F.B., Distillation Theory and its Application to Optimal Design of Separation Unit. 2004, Cambridge: Cambridge University Press.
46. Agrawal, R. and Z.T. Fidkowski, Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations?. Industrial & Engineering Chemistry Research, 1998, 37(8):3444-3454.
47. Fidkowski, Z.T. and R. Agrawal, Multicomponent thermally coupled systems of distillation columns at minimum reflux. AIChE Journal, 2001, 47(12):2713-2724.
48. Bruggemann, S. and W. Marquardt, Rapid screening of design alternatives for nonideal multiproduct distillation processes. Computers & Chemical Engineering, 2004, 29(1):165-179.
49. Watkins, R.N., Petroleum Refinery Distillation. 1979, Houston: Gulf Pub. Co.
50. Emmrich, G., H. Gehrke, and U. Ranke, The progressive extractive distillation arrangement for the morphylane extractive distillation process. Chemie Ingenieur Technik, 2001, 73(6):715.
51. Schreinemakers, F.A.H., Einige bemerkungen ueber dampfdruecke ternaerer gemische. Journal of Physical Chemistry, 1902, 43:671-685.
52. Rayleigh J.W.S., On the distillation of binary mixtures. Philosophical Magazine, 1902, 6 (4):521-537.
53. Fien, G.-J.A.F. and Y.A. Liu, Heuristic synthesis and shortcut design of separation processes using residue curve maps: A review. Industrial & Engineering Chemistry Research, 1994, 33(11):2505-2522.
54. Kiva, V.N., E.K. Hilmen, and S. Skogestad, Azeotropic phase equilibrium diagrams: A survey. Chemical Engineering Science, 2003, 58(10):1903-1953.
55. Doherty, M.F. and J.D. Perkins, On the dynamics of distillation processes-I: The simple distillation of multicomponent non-reacting, homogeneous liquid mixtures. Chemical Engineering Science, 1978, 33(3):281-301.
56. Doherty, M.F. and J.D. Perkins, On the dynamics of distillation processes-II. The simple distillation of model solutions. Chemical Engineering Science, 1978, 33(5):569-578.
57. Doherty, M.F. and J.D. Perkins, On the dynamics of distillation processes-III: The topological structure of ternary residue curve maps. Chemical Engineering Science, 1979, 34(12):1401-1414.
58. Smith, J.M., H.C.Van Ness, and M.M. Abbott, Introduction to Chemical Engineering Thermodynamics. 7th ed. McGraw-Hill Chemical Engineering Series. 2005, Boston: McGraw-Hill. 18, p. 817.
59. Tapp, M., et al., Column profile maps.1. Derivation and interpretation. Industrial and Engineering Chemistry Research, 2004, 43(2):364-374.
60. Knight, J.R. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 5. Columns with non-negligible heat effects. Industrial and Engineering Chemistry, Fundamentals, 1986, 25(2):279-289.
61. Van Dongen, D.B. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 1. Problem formulation for a single column. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):454-463.
62. Levy, S.G., D.B.Van Dongen, and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):463-474.
63. Doherty, M.F. and G.A. Caldarola, Design and synthesis of homogeneous azeotropic distillations. 3. The sequencing of columns for azeotropic and extractive distillations. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):474-485.
64. Levy, S.G. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 4. Minimum reflux calculations for multiple-feed columns. Industrial and Engineering Chemistry, Fundamentals, 1986, 25(2):269-279.
65. Felbab, N., D. Hildebrandt, and D. Glasser, A new method of locating all pinch points in nonideal distillation systems, and its application to pinch point loci and distillation boundaries. Computers and Chemical Engineering, 2011, 35(6):1072-1087.
66. Ruiz, G.J., et al., Rigorous synthesis and simulation of complex distillation networks. AIChE Journal, 2011, 57(1):136-148.
67. Holland, S.T., et al., Column profile maps. 2. Singular points and phase diagram behaviour in ideal and nonideal systems. Industrial and Engineering Chemistry Research, 2004, 43(14):3590-3603.
68. Doherty, M.F. and J.D. Perkins, On the dynamics of distillation processes III: The topological structure of ternary residue cure maps. Chemical Engineering Science, 1979, 34:1401-1414.
69. Holland, S.T., et al., Novel separation system design using "moving triangles". Computers and Chemical Engineering, 2004, 29(1):181-189.
70. Hildebrandt, D., et al., Column profile maps as a tool for synthesizing complex column configurations. Computers and Chemical Engineering, 2010, 34(9):1487-1496.
71. Tapp, M. and S. Kauchali, et al., An experimental simulation of distillation column concentration profiles using a batch apparatus. 2003, Chemical Engineering Science. 58:479-486.
72. Mulopo, J.L, et al., Experimental simulation of distillation column concentration profiles using a batch apparatus: Columns stripping section. 2005, Chemical Engineering Science, 60(24):6815-6823.
73. Modise, T., et al., Experimental simulation of distillation column section profiles using a batch apparatus. 2005, Industrial and Engineering Chemistry Research, 44:7511-7519.
74. Modise, T., et al., Experimental measurement of the saddle node region in a distillation column profile map by using a batch apparatus. 2007, Chemical Engineering Research and Design, 85(1):24-30.
75. Modise, T. D., Experimental simulation of distillation column profile maps, Chemical and Metallurgical Engineering. 2008, Johannesburg: University of the Witwatersrand.
76. Mulopo, J., A study of vector formulations for distillation processes, Chemical and Metallurgical Engineering. 2008, Johannesburg: University of the Witwatersrand.
77. Furzer, I. A., Critical distillation experiments in a region near the homogeneous ternary azeotrope in the system ethyl acetateéthanoĺwater. 2001. Industrial and Engineering Chemistry Research, 40(3):990-992.
78. Van Dongen, D.B. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 1. Problem formulation for a single column. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):454-463.
79. Levy, S.G., D.B.Van Dongen, and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):463-474.
80. Levy, S.G. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 4. Minimum reflux calculations for multiple-feed columns. Industrial and Engineering Chemistry Fundamentals, 2002, 25(2):269-279.
81. Doherty, M.F. and M.F. Malone, Conceptual Design of Distillation Systems. 1st ed. 2001, New York, NY, USA, McGraw-Hill. p. 568.
82. Kremser, A., Theoretical analysis of absorption process. National Petroleum News, 1930, 22(21):43-49.
83. Knight, J.R. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 5. Columns with non-negligible heat effects. Industrial and Engineering Chemistry, Fundamentals, 1986, 25(2):279-289.
84. Seader, J.D. and E.J. Henley, Separation Process Principles. 2nd ed. 2006, Hoboken, NJ: Wiley. p. 756.
85. Ruiz, G.J., et al., Robust thermodynamically-guided algorithms for synthesis of energy efficient separation networks, in Computer Aided Chemical Engineering. S. Pierucci and G.B. Ferraris, Editors. 2010, The Netherlands: Elsevier. pp. 1117-1122.
86. Ruiz, G.J., et al., Design and optimization of energy efficient complex separation networks, in 7th International Conference on the Foundations of Computer-Aided Process Design. 2009, New York: Taylor & Francis Group.
87. Zhang, L. and A.A., Linninger, Temperature collocation algorithm for fast and robust distillation design. Industrial and Engineering Chemistry Research, 2004, 43(12):3163-3182.
88. Fenske, M.R., Fractionation of straight-run Pennsylvania gasoline. Industrial and Engineering Chemistry, 1932, 24(5):482-485.
89. Underwood, A.J.V., Fractional distillation of multi-component mixtures-Calculation of minimum reflux ratio. Institute of Petroleum-Journal, 1946, 32(274):614-626.
90. Wahnschafft, O.M., et al., The product composition regions of single-feed azeotropic distillation columns. Industrial and Engineering Chemistry Research, 1992, 31 (10):2345-2362.
91. Linninger, A., Industry-Wide Energy Saving by Complex Separation Networks, in FOCAPO, Cambridge, MA, 2008.
92. Zhang, L. and A.A. Linninger, Towards computer-aided separation synthesis. AIChE Journal, 2006, 52(4):1392-1409.
93. Abbas, R., S.T. Holland, and I.J. Halvorsen, Novel minimum reflux calculation using eigenvector maps, in Distillation and Absorption 2010, G.K. de Haan, editor. 2010, Eindhoven, The Netherlands: Eindhoven University of Technology.
94. McCabe, W.L. and E.W. Thiele, Graphical design of fractionating columns. Industrial and Engineering Chemistry, 1925, 17(6):606-611.
95. Akashah, S., J.H. Erbar, and R.N. Maddox, Optimum feed plate location for multicomponent distillation separations. Chemical Engineering Communications, 1979, 3 (6):461-468.
96. Fenske, M.R., Fractionation of straight-run Pennsylvania gasoline. Industrial and Engineering Chemistry, 1932, 24(5):482-485.
97. Doherty, M.F. and M.F. Malone, Conceptual Design of Distillation Systems. 1st ed. 2001, New York, NY: McGraw-Hill. p. 568.
98. Glinos, K.N. and M.F. Malone, Design of sidestream distillation columns. Industrial and Engineering Chemistry, Process Design and Development, 1985, 24(3):822-828.
99. Levy, S.G., D.B.Van Dongen, and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations: 2. Minimum reflux calculations for nonideal and azeotropic columns. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):463-474.
100. Watkins, R.N., Petroleum Refinery Distillation. 1979, Houston, TX: Gulf Pub. Co.
101. Petlyuk, F.B., Distillation Theory and its Application to Optimal Design of Separation Unit. 2004, Cambridge: Cambridge University Press.
102. Emmrich, G., H. Gehrke, and U. Ranke, The progressive extractive distillation arrangement for the morphylane extractive distillation process. Chemie Ingenieur Technik, 2001, 73(6):715.
103. Beneke, D.A. and A.A. Linninger, Graphical design and analysis of thermally coupled sidestream columns using column profile maps and temperature collocation. AIChE Journal, 2010.
104. Wright, R.O., Fractionation Apparatus. 1949: USA Patent no. 2471134.
105. Petlyuk, F.B., V.M. Platonov, and D.M. Slavinskii, Thermodynamically optimal method for separating multicomponent mixtures. International Chemical Engineering, 1965, 5(3):554-561.
106. Kaibel, G., Distillation columns with vertical partitions. Chemical Engineering and Technology, 1987, 10(1):92-98.
107. Wenzel, S. and H.J. Röhm, Auslegung thermisch und stofflich gekoppelter Destillationskolonnen mittels Gesamtkostenoptimierung. Chemie Ingenieur Technik, 2003, 75(5):534-540.
108. Wolff, E.A. and S. Skogestad, Operation of integrated three-product (Petlyuk) distillation columns. Industrial and Engineering Chemistry Research, 1995, 34(6):2094-2103.
109. Stupin, W.J. and F.J. Lockhart, Thermally coupled distillation-a case history. Chemical Engineering Progress, 1972, 68(10):71.
110. Hendry, J.E., D.F. Rudd, and J.D. Seader, Synthesis in the design of chemical processes. AIChE Journal, 1973, 19:1.
111. Doukas, N. and W.L. Luyben, Economics of alternative distillation configurations for separation of ternary mixtures. Industrial and Engineering Chemistry Process Design and Development, 1978, 17:273.
112. Tedder, D.W. and D.F. Rudd, Parametric studies in industrial distillation: Part 1. Design comparisons. AIChE Journal, 1978, 24:303.
113. Fidkowski, Z. and L.W. Krolikowski, Minimum energy requirements of thermally coupled distillation systems. AiChE Journal, 1987, 33(4):643-653.
114. Westerberg, A.W., The synthesis of distillation based separation systems. Computers and Chemical Engineering, 1985, 9(5):421.
115. Glinos, K.N. and M.F. Malone, Design of sidestream distillation columns. Industrial and Engineering Chemistry Process Design and Development, 1985, 24(3):822-828.
116. Rudd, H., Thermal coupling for energy efficiency. The Chemical Engineering, 1992, p. (Supplement) S14.
117. Triantafyllou, C. and R. Smith, The design and optimisation of fully thermally coupled distillation columns: Process design. Transactions of the Institution of Chemical Engineers, 1992, 70:118-132.
118. Westerberg, A.W. and O. Wahnschafft, Synthesis of distillation-based separation systems, in Advances in Chemical Engineering, L.A. John, editor. 1996, New York: Academic Press pp. 63-170.
119. Finn, A.J., Gas Separation and Purification, 1996, 10(3):169.
120. Hernandez, S. and A. Jimenez, Controllability analysis of thermally coupled distillation systems. Industrial and Engineering Chemistry Research, 1999, 38(10):3957-3963.
121. Segovia-Hernández, J.G., S. Hernández, and A. Jiménez, Analysis of dynamic properties of alternative sequences to the Petlyuk column. Computers and Chemical Engineering, 2005, 29(6):1389-1399.
122. Hernández, S., J. Gabriel Segovia-Hernández, and V. Rico-Ramírez, Thermodynamically equivalent distillation schemes to the Petlyuk column for ternary mixtures. Energy, 2006, 31(12):2176-2183.
123. Hernández, S. and A. Jiménez, Design of energy-efficient Petlyuk systems. Computers and Chemical Engineering, 1999, 23(8):1005-1010.
124. Halvorsen, I.J. and S. Skogestad, Minimum energy consumption in multicomponent distillation. 2. Three-product Petlyuk arrangements. Industrial and Engineering Chemistry Research, 2003, 42(3):605-615.
125. Halvorsen, I.J. and S. Skogestad, Optimizing control of Petlyuk distillation: Understanding the steady-state behavior. Computers and Chemical Engineering, 1997. 21(Supplement 1):S249-S254.
126. Abdul Mutalib, M.I. and R. Smith, Transactions of Institute of Chemical Engineering, Part A, 1998. 76:308.
127. Agrawal, R. and Z.T. Fidkowski, Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations?. Industrial and Engineering Chemistry Research, 1998, 37(8):3444-3454.
128. Ling, H. and W.L. Luyben, New control structure for divided-wall columns. Industrial and Engineering Chemistry Research, 2009, 48(13):6034-6049.
129. Holland, S.T., Column profile maps: A tool for the design and analysis of complex distillation systems, in Chemical and Metallurgical Engineering. 2005, Johannesburg: University of the Witwatersrand.
130. Holland, S.T., et al., Complex column design by application of column profile map techniques: Sharp-split Petlyuk column design. Industrial and Engineering Chemistry Research, 2009, 49(1):327-349.
131. Halvorsen, I.J. and S. Skogestad, Optimal operation of Petlyuk distillation: Steady-state behavior. Journal of Process Control, 1999, 9(5):407-424.
132. Halvorsen, I.J. and S. Skogestad, Minimum energy consumption in multicomponent distillation. 1. Vmin diagram for a two-product column. Industrial and Engineering Chemistry Research, 2003, 42(3):596-604.
133. Abbas, R., Utilisation of Column Profile Maps for design and optimisation of complex distillation processes, in Chemical and Metallurgical Engineering. 2011, Johannesburg: University of the Witwatersrand.
134. Backhaus, A.A., Continuous processes for the manufacture of esters, 1921, USA.
135. Backhaus, A.A., Apparatus for producing high grade esters, 1922, USA.
136. Backhaus, A.A., Process for producing high grade esters, 1923, USA.
137. Backhaus, A.A., Process for esterification, 1923, USA.
138. Berman, S., et al., Esterification. Continuous production of dibutyl phthalate in a distillation column. Industrial and Engineering Chemistry, 1948, 40:2139-2148.
139. Taylor, R. and R. Krishna, Modeling reactive distillation. Chemical Engineering Science, 2000, 55:5183-5229.
140. Taylor, R. and R. Krishna, Modelling reactive distillation. Chemical Engineering Science, 2000, 55(22):5183-5229.
141. Venimadhavan, G., et al., Effect of kinetics on residue curve maps for reactive distillation. AIChE Journal, 1994, 40(11):1814.
142. Jiménez, L., O.M.Wanhschafftb, and V. Julka, Analysis of residue curve maps of reactive and extractive distillation units. Computers and Chemical Engineering, 2001, 25(4-6):635-664.
143. Barbosa, D. and M.F. Doherty, The simple distillation of homogeneous reactive mixtures. Chemical Engineering Science, 1988, 43(3):541-550.
144. Barbosa, D. and M.F. Doherty., Synthesis and Analysis of Multicomponent Reactive Distillation Systems. 1986, Miami, FL, USA: AIChE.
145. Barbosa, D. and M.F. Doherty., Design of multicomponent reactive distillation columns. 1987. Brighton, UK: European Federation of Chemical Engineering, Amarousion-Pefki, Greece.
146. Barbosa, D. and M.F. Doherty, Design and minimum reflux calculations for single-feed multicomponent reactive distillation columns. Chemical Engineering Science, 1988, 43:1523-1537.
147. Buzad, G. and M.F. Doherty, Design of three-component kinetically controlled reactive distillation columns using fixed-points methods. Chemical Engineering Science, 1994, 49(12):1947-1963.
148. Chen, F., et al., Multiple steady states in reactive distillation: Kinetic effects. Computers and Chemical Engineering, 2002, 26(1):81-93.
149. Chen, F., et al., Simulation of kinetic effects in reactive distillation. Computers and Chemical Engineering, 2000, 24(11):2457-2472.
150. Okasinski, M.J. and M.F. Doherty, Design method for kinetically controlled, staged reactive distillation columns. Industrial and Engineering Chemistry Research, 1998, 37 (7):2821-2834.
151. Doherty, M.F. and M.F. Malone, Conceptual Design of Distillation Systems, ed. C.E. Series. 2001, New York, NY, USA: McGraw-Hill. 568.
152. Hauan, S. and K.M. Lien, Phenomena based design approach to reactive distillation. Chemical Engineering Research & Design, Transactions of the Institute of Chemical Engineers, Part A, 1998, 76(A3):396-407.
153. Hauan, S., A.W. Westerberg, and K.M. Lien, Phenomena-based analysis of fixed points in reactive separation systems. Chemical Engineering Science, 2000, 55(6):1053-1075.
154. Van Dongen, D.B. and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 1. Problem formulation for a single column. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):454-463.
155. Levy, S.G., D.B.Van Dongen, and M.F. Doherty, Design and synthesis of homogeneous azeotropic distillations. 2. Minimum reflux calculations for nonideal and azeotropic columns. Industrial and Engineering Chemistry, Fundamentals, 1985, 24(4):463-474.
156. Hoffmaster, W.R. and S. Hauan, Using feasible regions to design and optimize reactive distillation columns with ideal VLE. AIChE Journal, 2006, 52(5):1744-1753.
157. Stitt, E.H., Reactive distillation for toluene disproportionation: A technical and economic evaluation. Chemical Engineering Science, 2002, 57(9):1537-1543.
158. Luyben, W.L. and C.-C. Yu, Reactive Distillation Design and Control. 2008, Hoboken, NJ: Wiley: AIChE. 21, 574 p.
159. An, W., K.T. Chuang, and A.R. Sanger, Dehydration of methanol to dimethyl ether by catalytic distillation. The Canadian Journal of Chemical Engineering, 2004, 82(5): 948-955.
160. Peters, M., et al., Membrane Process Design Using Residue Curve Maps 2011, New York: Wiley. p. 224.
161. Rautenbach, R. and R. Albrecht, Membrane Processes. 1st ed. 1989, New York: Wiley. 490.
162. Marriott, J. and E. Sørensen, A general approach to modelling membrane modules. Chemical Engineering Science, 2003, 58(22):4975-4990.
163. Marriott, J. and E. Sørensen, The optimal design of membrane systems. Chemical Engineering Science, 2003, 58(22):4991-5004.
164. Rautenbach, R. and R. Albrecht, The separation potential of pervaporation: Part 2. Process design and economics. Journal of Membrane Science, 1985, 25(1):25-54.
165. McCandless, F.P., A comparison of membrane cascades, some one-compressor recycle permeators, and distillation. Journal of Membrane Science, 1994, 89(1-2):51-72.
166. Seader, J.D. and E.J. Henley, Separation Process Principles. 2nd ed. 2006, Hoboken, NJ: Wiley. p. 756.
167. Hwang, S. and J.M. Thorman, The continuous membrane column. AIChE Journal, 1980, 26.
168. Tsuru, T. and S.-T. Hwang, Permeators and continuous membrane columns with retentate recycle. Journal of Membrane Science, 1995, 98(1-2):57-67.
169. Tapp, M., et al., Column profile maps. 1. Derivation and interpretation. Industrial and Engineering Chemistry Research, 2004, 43(2):364-374.
170. Wijmans, J.G. and R.W. Baker, The solution-diffusion model: A review. Journal of Membrane Science, 1995, 107(1-2):1-21.
171. Huang, Y.-S., et al., Residue curve maps of reactive membrane separation. Chemical Engineering Science, 2004, 59(14):2863-2879.
172. Peters, M., et al., Application of membrane residue curve maps to batch and continuous processes. Industrial and Engineering Chemistry Research, 2008, 47(7):2361-2376.
173. Peters, M., et al., Derivation and properties of membrane residue curve maps. Industrial and Engineering Chemistry Research, 2006, 45(26):9080-9087.
174. Fien, G.-J.A.F. and Y.A. Liu, Heuristic synthesis and shortcut design of separation processes using residue curve maps: A review. Industrial and Engineering Chemistry Research, 1994, 33(11):2505-2522.
175. Lu, Y., et al., Hybrid process of distillation side-connected with pervaporation for separation of methanol/MTBE/C4 mixture. Desalination, 2002, 149(1-3):81-87.
176. Rehfinger, A. and U. Hoffmann, Kinetics of methyl tertiary butyl ether liquid phase synthesis catalyzed by ion exchange resin-I. Intrinsic rate expression in liquid phase activities. Chemical Engineering Science, 1990, 45(6):1605-1617.
177. Bausa, J. and W. Marquardt, Shortcut design methods for hybrid membrane/distillation processes for the separation of nonideal multicomponent mixtures. Industrial and Engineering Chemistry Research, 2000, 39(6):1658-1672.
178. Hömmerich, U. and R. Rautenbach, Design and optimization of combined pervaporation/ distillation processes for the production of MTBE. Journal of Membrane Science, 1998, 146(1):53-64.
179. Kim, S.B. and A.A. Linninger, Rigorous separation design. 2. Network design solutions for mixtures with various volatility differences and feed compositions. Industrial and Engineering Chemistry Research, 2010, 49(18):8670-8684.
180. Kim, S.B., G.J. Ruiz, and A.A. Linninger, Rigorous separation design. 1. Multicomponent mixtures, nonideal mixtures, and prefractionating column networks. Industrial and Engineering Chemistry Research, 2010, 49(14):6499-6513.
181. Ruiz, G.J., et al., Design and optimization of energy efficient complex separation networks, in 7th International Conference on the Foundations of Computer-Aided Process Design. 2009, New York: Taylor & Francis Group.
182. Ruiz, G.J., et al., Robust thermodynamically-guided algorithms for synthesis of energy efficient separation networks, in Computer Aided Chemical Engineering, S. Pierucci and G.B. Ferraris, Editors. 2010, Amsterdam, The Netherlands: Elsevier. pp. 1117-1122.
183. Zhang, L. and A.A. Linninger, Towards computer-aided separation synthesis. AIChE Journal, 2006, 52(4):1392-1409.
184. Zhang, L. and A.A. Linninger, Temperature collocation algorithm for fast and robust distillation design. Industrial and Engineering Chemistry Research, 2004, 43(12):3163-3182.