Page 323 - Applied Process Design For Chemical And Petrochemical Plants Volume III
P. 323
66131_Ludwig_CH10H-J 5/30/2001 4:47 PM Page 282
282 Applied Process Design for Chemical and Petrochemical Plants
120. Vachon, R. I., G. H. Nix, G. E. Tanger, and R. O. Cobb, “Pool 142. Chenoweth, J. M., “Final Report of the HTR/TEMA Joint
Boiling Heat Transfer from Teflon-Coated Stainless Steel,” Committee to Review the Fouling Section of the TEMA Stan-
ASME, Jour. Heat Trans., V. 91, p. 364, Aug. (1969). dards,” Heat Transfer Eng., V. 11, No.1, pp. 73—107 (1990).
121. Volta, F., Jr., “Computer Program for Condenser Design for 143. Zanker, A., “Predict Fouling by Nomograph,” Hydro Proc., V.
Gas Vapor Mixtures,” Dept. of Chemical Engineering, Uni- 53, No. 3, p. 145 (1978).
versity of Rhode Island, Kingston, RI. 144. Ganapathy, V., “Monitor Fouling Graphically,” Chem. Eng., p.
122. Volta, F., Jr., private communication, Dept. of Chemical Engi- 94, Aug. 6, (1984).
th
neering, University of Rhode Island, Kingston, RI. 145. Epstein, N., “Fouling in Heat Exchangers,” Proc. 6 Interna-
123. Volta F., Jr. and C. A. Walker, “Condensation of Vapor in the tional Heat Transfer Conference Keynote Papers, V. 6, p. 235,
Presence of Noncondensing Gas,” AIChE Jour., V. 4, p. 413 Toronto, Canada, Hemisphere Publishing Co., New York, NY
(1958). (1978).
124. Whitley, D. L. and E. E. Ludwig, “Effective Tube Lengths for 146. Mukherjee, R., “Conquer Heat Exchanger Fouling,” Hydro
U-Tubes,” Chem. Eng., V. 67, June 27, (1960). Proc., V. 71, No. 1, p. 121 (1996).
125. Whitley, D. L. and E. E. Ludwig, “Heat Exchanger Design with 147. Turakhia, M. and W. G. Characklis, “Fouling of Heat
a Digital Computer,” Pet. Ref., V. 40, No. 1, p. 147 (1961). Exchanger Surface: Measurement and Diagnosis,” Heat Trans-
126. Williams, R. B. and D. L. Katz, “Performance of Finned Tubes fer Eng., V. 5, No.1—2, p. 93 (1984).
in Shell and Tube Heat Exchangers,” Project M592, Engi- 148. Bott, T. R. and C. R. Bemrose, “Particulate Fouling on the Gas
neering Research Institute, University of Michigan, Ann Side of Finned Tube Heat Exchangers,” Trans of ASME, V.
Arbor, MI, Jan. (1951). 105, p. 178, Feb. (1983).
127. Young, E. H. and D. J. Ward, “How To Design Finned Tube 149. Cooper, A., J. W. Suitor, and J. D. Usher, “Cooling Water Foul-
Shell and Tube Heat Exchangers,” The Refining Engr., p. C-32, ing in Plate Heat Exchangers,” Heat Transfer Eng., V. 1, No. 3,
Nov. (1957). p. 50 (1980).
128. Zuber, N., Trans. ASME, V. 80, No. 37 (1958). 150. Characklis, W. G., M. J. Nimmons, and B. F. Picologlou,
129. Gully, D. L., “How to Figure True Temperature Difference in “Influence of Fouling Biofilms on Heat Transfer,” Heat Trans-
Shell-and-Tube Exchangers,” Oil and Gas Jour., Sept. 14 (1964). fer Eng., V. 3, No. 1, p. 23 (1981).
130. Plant, C. A., “Evaluate Heat Exchanger Performance” Chem. 151. Webb, R. L., “Performance, Cost Effectiveness, and Water-
Eng., V. 99, No. 6, Part 1 and No. 7, Part 2, pp. 100 and 104, Side Fouling Considerations of Enhanced Tube Heat
respectively (1992). Exchangers for Boiling Service with Tube-Side Water Flow,”
131. Blackwell, W. W. and L. Haydu, “Calculating the Corrected Heat Transfer Eng., V. 3, No. 3—4, p. 84 (1982).
LMTD in Shell-and-Tube Heat Exchangers,” Chem. Eng., p. 152. Fischer, P., J. W. Suitor, and R. B. Ritter, “Fouling Measure-
101, Aug. 24, (1981). ment Techniques and Apparatus,” presented at AIChE, 99 th
132. Murty, K. N., “Quickly Calculate Temperature Cross in 1—2 National Meeting, Houston, Texas, pub. Heat Transfer
Parallel-Counterflow Heat Exchangers,” Chem. Eng., p. 99, Research, Inc., March 16—20, (1975).
Sept. 16 (1985). 153. Wachel, L. J., “Exchanger Simulation: Guide to Less Fouling,”
133. Boyer, J. and G. Trumpfheller, “Specification Tips to Maxi- Hydro. Proc., V. 65, No. 11, p. 107 (1986).
mize Heat Transfer,” Chem. Eng., p. 90, May (1993). 154. Crozier, R. A., Jr., “Increase Glow to Cut Fouling,” Chem Eng.,
134. Ratnam, R. and P. S. Patwardhan, “Analyze Single and Multi- p. 115, Mar. 8, (1982).
Pass Heat Exchangers,” Chem. Eng. Prog., V. 88, No. 6, p. 85 155. Crittenden, B. D. and S. T. Kolaczkowski, “Reduce Exchanger
(1993). Fouling,” Hydro. Proc., V. 66, No. 8, p. 45, Gulf Publishing Co.
135. Turton, R., D. Ferguson, and O. Levenspiel, “Charts for the (1987).
Performance and Design of Heat Exchangers,” Chem. Eng., p. 156. Gilmour, C. H., “Design Fouling Out of Your Heat Exchang-
81, Aug. 18, (1986). ers,” abstracted from remarks at AIChE meeting, Houston,
136. Whitley, D. L., “Calculating Heat Exchanger Shell-Side Pres- Texas, (1965), pub. Oil and Gas Jour., July 26, p. 177 (1965).
sure Drop,” Chem. Eng. Prog., V. 57, No. 9, p. 59 (1961). 157. Buecker, B., “Beware of Condenser Fouling,” Chem. Eng., V.
137. Sanatgar, H. and E. F. C. Somerscales, “Account for Fouling in 102, No. 4, p. 108 (1965).
Heat Exchanger Design,” Chem. Eng. Prog., V. 87, No. 2, p. 53 158. Martin, J. F., “Reduce Olefin Plant Fouling,” Hydro. Proc., V.
(1991). 67, No. 11, p. 63 (1988).
138. Frenier, W. W. and S. J. Barber, “Choose the Best Heat 159. Hedrick, R. H., “Calculate Heat Transfer for Tubes in the
Exchanger Cleaning Method,” Chem. Eng. Prog., V. 94, No. 7, Transition Region,” Chem. Eng., V. 97, No. 6, p. 147 (1989).
p. 37 (1998). 160. Sinek, J. R. and E. H. Young, “Heat Transfer in Falling-Film
139. Perry, R. H. and D. W. Green, Perry’s Chemical Engineers’ Hand- Long-Tube Vertical Evaporators,” Chem. Eng. Prog., V. 58, No.
th
book, 6 Ed. McGraw-Hill, Inc. (1984) . 12, p. 74 (1962).
140. Knudsen, J. G., “Conquer Cooling-Water Fouling,” Chem. Eng. 161. Ganapathy, V., “Tube-Wall Temperature Figured Quickly,” Oil
Prog., V. 87, No. 4, p. 42 (1991). and Gas Jour., p. 93, Jan. 1, (1979).
141. Konings, A. M., “Guide Values for the Fouling Resistance of 162. Najjar, M. S., K. J. Bell, and R. N. Maddox, “The Influence of
Cooling Water with Different Types of Treatment for Design Improved Physical Property Data on Calculated Heat Trans-
of Shell and Tube Heat Exchangers,” Heat Transfer Eng., V. 10, fer Coefficients,” Heat Transfer Eng., V. 2, No. 3—4, p. 27
No. 4., p. 54 (1989). (1981).

