Page 236 - Applied Process Design For Chemical And Petrochemical Plants Volume II

Distillation

62. Sherwood, T. K., Absoqtion and Extraction, McGraw-Hill 91. Wichterle, I., R., Kobayashi, and P. S. Chappelear, “Caution1
Book Co., Inc., KewYork, N.Y. (1937). Pinch Point inY-X Curve” Hydro. Roc. Nov. (1971), p. 233.
63. Shiras, R N., D. N. Hansen, C. H. Gibson, ‘Calculation of 92. Wagle, M. P., “Estimate Relative Volatility Quickly,” C k
Minimum Reflux in Distillation Columns,” Ind. Eng. Chm Eng. V. 92, No. 9 (1985), p. 85.
V. 42, p. 871 (1950). 93. Reid, R. C., J. M. Prausnitz, and T. K. Sherwood, “Them
64. Simkin, I3. J., C. P. Strand and R. B. Olnep “Entrainment erties of Gases and Liquids,” 3rd Ed., McGraw-Hill, New York,
from Bubble Caps,” Chm. Eng. Bvg, V. 50, p. 565 (1954). (1977), p. 214.
65. Smith, B. D., Design ofEquaZibrium Stage Processes, McGraw- 94. Kister, H. Z., “Distillation Design,” McGraw-Hill, Inc. (1992).
Hill (1963). 95. Kister, H. Z., “Complex Binary Distillation,” Ch. Eng. IT.
66. Smoker, E. H., “Nomographs for Minimum Reflux Ratio 92, No. 2 (1985), p. 9‘7.
and Theoretical Plates for Separation of Binary Mixtures,” 96. Chou, SM. and C. L. Yaws, “Minimum Reflux for Complex
Ind. Eng. Chem. V. 34, p. 509 (1942). Distillations,” Chem. Eng. V. 96, No. 6 (1988), p. 79.
67. Souders, .M., Jr.? G. G. Brown, “Fundamental Design of 97. McCormick, J. E., “A Correlation for Distillation Stages and
absorbing and Stripping Columns for Complex Vapors,” Reflux,” Chm. Eng. V. 95, No. 13 (1988) p. 75.
Id. Eng. Ch. V. 24, p. 519 (1932). 98. Venkateswara, Rao R, and A. Raviprasad, “Quickly Deter-
68. Souders, M., Jr., G. G. Brown, “Design of Fractionating mine Multicomponent Minimum Reflux Rates,” Chem. Eng.
Columns,” Ind. Eng. Chem. V. 26, p. 98 (1934). V. 14 (1987), p. 137.
69. Sutherland, S., Jr.: “Characteristics of Countercurrent Vapor 99. Winn, F. W., “New Relative Volatility Method for Distillation
Liquid Flow at a Perforated Plate. M. S. Thesis, Jan. 1938. Calculations,” Pet. Refiner (now Hjdro. Pmc.) I? 37, No. 6
Texas A8AM College. (1958), p. 216.
70. Teller, A. J., ‘Binary Distillation,” Chem. E%. p. 168, Sept. 100. Frank, O., “Shortcuts for Distillation Design,” Ch. Eng.
(1954). Mar. 14, (1977), p. 109.
71. Umholtz, C. L. and M. Van Winkle, “Effect of Hole Free 101. Kessler, D. P. and P. C. Wankat, “Correlations for Column
Area, Hole Diameter, Hole Spacing Weir Height, and Down- Parameters,” Chem. Eng. V. 95, KO. 13 (1988) p. 71.
comer Area,” Pet. Ref. V. 34, p. 114 (1965). 102. Two, Fu-hfing, C. L. Yam and JS. Cheng, “Minimum Reflux
72. Underwood, k J. V., “Fractional Distillation of Multicom- for Sidestream Columns,” Ch. Eng. July 21, (1986), p. 49.
ponent Mixtures,” Chem. E%. hg. V. 44, p. 603 (1948). 103. Chou, SM. and C. L. Yaws, “Reflux for Multifeed Distilla-
73. Underwood, A. J. V., Zhs. Inst. Ch. E. (London) V. 10 p. tion,” Hydro. Proc. Dec. (1986), p. 41.
112 (1932). 104. Scheiman, A. D., “Find Minimum Reflux by Heat Balance,”
74. Van Winkle, M., DistiZZation, McGraw-Hill, Inc. (1967). Hjidro. Pmc. Sept. (1969), p. 187.
75. Van Winkle, M., “Multicomponent Distillation,” OiZ and Gas 105. Lessi, A, “New Way to Figure Minimum Reflux,” Hydro. BOC.
Journal, p. 182, Mar. 23, (1953). V. 45, No. 3 (1966), p. 1‘73.
76. Wang, J. C. and G. E. Henke, “Tridiagonal Matrix for Distil- 106. Hengstebeck, R. J., ”DistiZlabion-principipEes and Design Proce
lation,” Hydrocarbon Processing, V. 43, No. 8, (1966) p. 155. dures,” Reinhold. Pub. Co. NewYork, (1961), p. 120.
7‘7. Wilson, G. M.,J Am. Chem. SOC., V. 86, (1964) p. 127. 107. Eduljee, H. E., “Easy Way to Remember Reflux vs. Trays,”
78. Zenx, F. A., “Calculate Capacity of Perforated Plates,” Pet Ref: Hydro. Roc. V, 42, No. 3 (1963), p. 183.
V. 33, p. 99 (1934). 108. Maas, J. H., “Optimum-Feed Stage Locations in Multicom-
79. Gas Processors Suppliers Association; Engineerkng Data Book, ponent Distillations,” Ch. Eng. Apr. 16 (1973), p. 96.
V. 1 and 2, 3rd, Rev., 9th Ed. (1977), produced in coopera- 109. Dechman, D. A., “Correcting the McCabe-Thiele Method for
tion with the Gas Processors Association. Unequal Molal Overffow,” Ch. Eng. Dec. 21 (1964) p. 79.
80. DePriester, C. L., The American Institute of Chemical Engi- 110. Torres-Marchal, C., “Graphical Design for Ternary Distilla-
neers; Chem. Eng. Pmg. Sym. Sm V. 49, No. 7 (1933) p. 1. tion Systems,” Chem. Eng. V. 88, No. 21 (1981) p. 134.
81. Nelson, W. L., “Petroleum Refinery Enginem-nf 1st Ed 11 1. Torres-Marchal, C., “Calculating Vapor-Liquid Equilibria for
McGraw-Hill Co., Jnc. (1936), p. 244. Ternary Systems,” Chena. E%. V. 88, No. 21 (1981), p. 141.
82. Carrol1,J. J., What Is Henry’s Law?” Chm Eng. hg. V. 87, 112. Maddox, R. N., “Calculations for Multicomponent Distilla-
Sept. (1991), p. 48. tion,” Chem. En6 Dec. 11 (1961), p. 127.
83. Carroll, J. J., “Use Henry’s Law for Multicomponent Mix- 113. Erbar, R. C., R. S. Joynet-, and R. N. Maddox, “For Multi-
tures,” Chem. Eng. Prog. V. 88, No. 8 (1992) p. 53. component Columns, How to Calculate Minimum Reflux,”
84. Eduljee, H. E., “Equations Replace Gilliland Plot,” Hydro. Petro/Cidern Engr Mar. (1961), p. G19.
A.oc. V. 54, No. 9 (1973), p. 120. 114. Lyster, W. N., S. L. Sullivan, D. S. Billingsley, and C. D. Hol-
85. Murphree, E. V., Ind. Eng. ChemV. 17, (1925), p. 747. land, “Digital Computer Used to Figure Distillation This
86. MacFarland, S. A.: P. M., Sigmund, and M. Van Winkle, “Pre- New Way,” Pet. &J (now, Hjdro. Roc.), June (1959), p. 221.
dict Distillation Efficiency,” Hjdro. hc. V. 51, No. 7 (1972), 115. Maddox, R. K., and J. H. Erbar, “Programming Plate to Plate
p. 111. Distillation Calculations,” Rey5ningEnp: Sept. (1959), p. G35.
87. Biddulph, M. W., “When Distillation Can Be Unstable,” 116. Maddox, R N., and W. A, Jr., Fling, “Try the Pseudo-K
Hydro. hc. V. 94, No. 9 (1979), p. 123. Method for Shortcut Multicomponent Distillation
88. Fair, J. R., “Tray Hydraulics-Perforated Trays,” Chap. 15 in Columns,” Petro/Chm Eng.1: Mar. (1961) p. G37.
Design of Equilibrium Stage Processes, Smith, B. D., McGraw- 117. Kister, H. Z., “DistiZZution Operntion,” McGrawHill, Inc. (1990).
Hill, New York, (1963), p. 552. 118. Forman, E. R., “Control Systems for Distillation,” Chem. Eng.
89. Leva, M., “Film Tray Equipment for Vacuum Distillation,” Nov. 8 (1965). p. 213.
Cha. Erg. V. 67, No. 3 (1971), p. 65. 119. Hoffman, H. L., “HP/PR Special Report, Automatic Con-
90. Biddulph, M. W., ”Tray Efficiency Is Not Constant,” Hydro. trol for Distillation,” Hydro. hc. and Pet. Ref: ?l. 42, No. 2
Proc. Oct. (1977), p. 145. (1963), p. 107.