Page 237 - Applied Process Design For Chemical And Petrochemical Plants Volume II
P. 237
226 Applied Process Design for Chemical and Petrochemical Plants
120. Shinskey, F. G. “Process-Control Sjn-tem,’’ McGraw-Hill Book 149. HenIy, E. J. and L. D., Seader, “Equilibriumstage Separation
Co., 2nd Ed. (1979). Operations in Chemical Engineenkg,” J. Wiley and Sons, Inc.
121. Trigueros, D., Coronado-Velasco, C. and A. Gornez-Munoz, (1981).
“Synthesize Simple Distillation the Thermodynamic Way,” 150. Eckles, A., P., Benz, and S., Fine, “When to Use High Vacu-
Chem. Eng. V. 96, No. 8 (1989), p. 129. um Distillation,” Chem. Eng. V. 98, No. 5 (1991), p. 201.
122. Mapstone, G. E., “Reflux versus Trays By Chart,” HydmProc. 151. Elsby, K., et al., “Packing Performance in Vacuum Distilla-
V. 47, No. 5 (1968), p. 169. tion,” A.I.Ch.E. Symposium Series No. 104 Distillation and
123. Zanker, A, “Nomograph Replaces Gilliland Plot,” Hydro. Adsmpion, (1987), pp. 143-148.
Proc. May (1977), p. 263. 152. “VacEum Technology fw Chual Engineering” Leybold, AG.,
124. Yaws, C. L., P. M. Patel, F. H. Pitts, and C. S. Fang, “Estimate p. 11.
Multicomponent Recovery,” Hydro. Aoc. V. 68, No. 2 (1979), 153. Holland, C. D., S. E., Gallun, and M. J., hckett, “Modelling
p. 99. Azeotropic and Extractive Distillation,” Ch. Eng. Mar. 23
125. Hengstebeck, R. J. Trans. A.I.Ch.E. V. 42 (1946) p. 309. (1981), p. 185.
126. Geddes, R. L., A.I.Ch.E.Jour: 17. 4 (1958), p. 389. 154. Luyben, W. L., “Azeotropic Tower Design by Graph,” Hydro.
127. Ellerbee, R .W., “Steam-Distillation Basics,” Chem. Eng. Mar. hoc. Jan. (1973), p. 109.
4 (1974), p. 105. 155. Stichlmair, J., J. R, Fair, and J. L., Bravo, “Separation of
Azeotropic Mixtures via Enhanced Distillation,” Ch. Eng.
128. Ellerbee, R W., Section 1.4 in Schweitzer, P. A. (editor), Prog. V. 85, No. 1 (1989), p. 63.
Handbook of Separation Techniques for Chemical Enginem, 156. Gerster, J. A, “Azeotropic and Extractive Distillation,” Chem
McGraw-Hill Book Co. (1979). Eng. Prog. V. 65, No. 9 (1969), p. 43.
129. Treybal, R E., “A Simple Method for Batch Distillation,” 167. Holland, C. D., et al., “Solve More Distillation Problems,” 13
Chem Erg. Oct. 5 (1970), p. 96. Parts; Hydrocarbon Proctssiing, Part 1, V. 53, No. 7 (1974) ; Part
130. Ellerbee, R. W., “Batch Distillation Basics,” Chem. E%. May 2, V. 53, No. 11 (1974); Part 3, V- 54, No. 1 (1975); Part 4,
28 (1973), p. 110. V. 54, No. 7 (1975); Part 5, V. 55, 0.1 (1976); Part 6, V. 55,
131. Schweitzer, P. A. “Handbook of Separation for Chemical En& No. 6 (1976); Part 7, V. 56 No. 5 (1977); Part 8, V. 56, No. 6
nem,” McGraw-Hill Book Co. (1979). (1977); Part 9, V. 59, No. 4 No. (1980); Part 10, V. 59, KO. 7
132. Perry, R H., and Green, D. “PerryS Chemical Engineers Han& (1980); Part 11, V. 60, No. 1 (1981); Part 12, V. 60, No. 7
book,” 6th Ed. McGraw-Hill Book Co. (1984). (1981), Part 13, V. 83, No. 11, (1983).
133. Block, B., “Batch Distillation of Binary Mixtures Provides 158. Tru-Tec Division of Koch Engineering Co. Inc. Bulbtin
Versatile Process Operations,” Chem. Eng. Feb. 6 (1961) p. 87. TPD-1 and TCS-1; Koch Engineering Co. Inc. Wichita, Kn.
134. Block, B., “Control of Batch Distillations,” Ch Eng. Jan. 16 67208-0127.
(1967) p. 147. 159. Harrison, M. E., and J. J. Frana, “Trouble-Shooting Distilla-
135. Brasens, J. R, “For Quicker Distillation Estimates,” Hydro. tion Columns,“ C k Eng. V. 96, No. 3 (1989) p. 116.
Proc. Oct (1969), p. 102. 160. Kister, H. Z., R F., Larson and P. E., Madsen, “Vapor Cross
136. Liddle, C. J., “Improved Shortcut Method for Distillation Flow Channeling on Sieve Trays: Fact or Myth?” Chem Eng.
Calculations,” Chem. Eng. Oct. 21 (1968), p. 137. hog. V. 88, No. 11 (1992), p. 86.
137. Hengstebeck, R. J., “An Improved Shortcut for Calculating 161. Niesenfeld, A. E., “Reflux or Distillate: Which to Control?’
Difficult Multicomponent Distillations,” Chem. Eng Jan. 13 Chem. Eng. Oct. 6 (1969), p. 169.
(1969), p. 115. 162. Ludwig, E. E., “Applied Pryect Engineering and Management,”
138. Guy, J. L., “Modeling Batch Distillation in Multitray 2nd Ed., Gulf Publishing Co. (1988), p. 453.
Columns,” Chem Eng. Jan. 10 (1983), p. 99. 163. Rys, R A, “Advanced Control Techniques for Distillation
139. Van Winkle, M. and W. G. Todd, “Optimum Fractionation Columns,” Chesn. ERg. Dec. 10 (1984), p. 75.
Design by Simple Graphical Methods,” Chem. Eng. Sept 20 164. Kister, H. Z., “Distilhti~m Ojmahn,’’ McGraw-Hill Publishing
(1971), p. 136. Co., Inc. (1990).
140. Koppel, P. M., “Fast Way to Solve Problems for Batch Distil- 165. Kister, H. Z., “How to Prepare and Test Columns Before
lation,’’ Chem. Eng. Oct. 16 (1972), p. 109. Start-up,” Ch. Eng. Apr. 6 (1981) p. 97.
141. Yaws, C. L., CS. Fang, and P. M. Patel, “Estimating Recover- 166. Chin, T. G., “Guide to Distillation Pressure Control Meth-
ods,’’ Hydro. Proc. V. 59, No. 10 (1979), p. 145.
ies in Multicomponent Distillation,” Chem. Eng. Jan. 29 167. Thurston, C. W., “Computer Aided Design of Distillation
(1979), p. 101. Column Controls,” Hydro. Froc. V. 60, No. 8 (1981), p. 135.
142. Kumana, J. D., “Run Batch Distillation Processes with 168. Holland, C. D., “Fundamentals of Multicomponent Distallation,”
Spreadsheet Software,” Chem. Eng. Prog. Dec. (1990), p. 53. McGraw-Hill Book Co. Inc. (1981).
143. Li, K Y and K J. Hsiao, “How to Optimize an Air Stripper,” 169. Holland, C. D. and k I., Liapis, “Computer Methods for Solu-
Chem. Erg... 98, No. 7 (1991), p. 114. ing Qmmic separation Robk,” McGrawHill, Inc. (1983).
144. Salmon, R, “New Method for V/L Flash Calculations,” Pet. 170. Haring, H. G., B. J., Grootenhuis, and H. W., Kn01, ‘‘P~~~IxuI-
Ref, (now Hydro. But.) V. 36, No. 12 (1957), p- 133. ming Batch Distillation,” them. E%. Mar. 16 (1964), p- 159.
145. Lockhart, F. J., and R J., McHenry, “Figure Flash Equilibria 171. Nisenfeld, A. E. and C. A., Stravinski, “Feed Forward Con-
Quicker This Way” Pet. Re$ V. 37, No. 3 (1958), p. 209. trol for Azeotropic Distillation,” cha. Eng. Sept. 23 (1968),
146. Gallagher, J. L., “New Short-cut for Flash Calculations,” p. 227.
Hydro. Proc. V. 42, No. 2 (1963), p. 157. 172. Othmer, D. F., “Azeotropic Separation,” Ch. Eng. Frog. V.
147. Holland, C. D. and P. R., Davidson, “Simplify Flash Distilla- 59, No. 6 (1963), p. 67.
tion Calculations,” Pet. Re$ V. 36, No. 3 (1957), p. 183. 173. Fair, J. R. and W. L., Bolles, “Modern Design of Distillation
148. Deam, J. R. and R. N., Maddox, “How to Figure Three-phase Columns,” Chma. Eng. Apr. 22 (1968) p. 156.
Flash,” Hydro. Roc. V. 51, No. 10 (1969), p. 163. 174. Kirkbride, C. G., Petm. ReJiner; V. 23, No. 9 (1944) p. 87.