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288 Applied Process Design for Chemical and Petrochemical Plants

Rothenberg, D. H. and R. L. Nicholson, “Interacting Controls for Taborek, J., G. F. Hewitt, and N. Afgan, Heat Exchangers, Theory and
Air Coolers,” Chem. Eng. Prog., V. 77, No. 1 (1981) p. 80. Practice, Hemisphere Publishing Co./McGraw-Hill Book Co.
Rubin, F. L., “How to Specify Heat Exchangers,” Chem. Eng., April (1983).
8, (1968) p. 130. Tarrec, A. R., H. C. Lim, and L. B. Koppel, “Finding the Economi-
Scaccia, C., G. Theoclitus, A. Devore, G. J. Bargo, and G. J. Picozzi, cally Optimum Heat Exchanger,” Chem. Eng., Oct. 4, (1971)
“Heat Exchangers,” Chem. Eng., Oct. 6, (1980) p. 120. p. 79.
Schwieger, R. G., “Heat Exchangers,” Power, June (1970) p. 33. Thompson, J. C., “Evaluating Heat Tracing,” Hydrocarbon Processing,
Shah, G. C., “Troubleshooting Reboiler Systems,” Chem. Eng. Prog., V. 76, No. 9, (1997) p.75,
July (1979) p. 53. The Tubular Exchanger Manufacturers Assoc., Inc., Standards; 6 th
Shah, M. M., “A General Predictive Technique for Heat Transfer Ed., TEMA, Inc. Tarrytown, N.Y. (1978).
During Saturated Film Boiling in Tubes,” Heat Trans. Eng., V. Turissini, R. L., T. V. Bruno, E. P. Dahlberg, and R. B. Setterlund,
2, Oct.—Dec. (1980) p. 51. “Prevent Corrosion Failures in Plate Heat Exchangers,” Chem.
Shoot, B. E., “Better Method to Find Pressure Drop,” Heat Eng. Progress, V. 93, No. 9 (1997) p. 44.
Exchanger Design Handbook, Gulf Publishing Company, (1968) Usher, J. D., “Evaluating Plate Heat-Exchangers,” Chem. Eng., Feb.
p. 20. 23, (1970) p. 90.
Short, B. E., “Flow Geometry and Heat Exchanger Performance,” Vachon, R. I., G. H. Nix, G. E. Tanger, and R. O. Cobb, “Pool Boil-
Chem. Eng. Prog., V. 61, No. 7 (1965) p. 63. ing Heat Transfer from Teflon-Coated Stainless Steel,” ASME
Silvestrini, R., “Heat Exchanger Fouling and Corrosion,” Chem. Journal Heat Trans., V. 91, Aug. (1969) p. 364.
Eng. Prog., Dec. (1979) p. 29. Van Stralen, S. J. D., “Heat Transfer to Boiling Binary Liquid Mix-
Singh, J., “Selecting Heat-Transfer Fluids for High-Temperature tures, Part 1,” British Chem. Eng., Jan. (1959) p. 8.
Service,” Chem. Eng., June 1 (1981) p. 53. Wales, R. E., “Mean Temperature Difference in Heat Exchangers,”
Sloan, M., “Designing and Troubleshooting Plate Heat Exchang- Chem. Eng., Feb. 23, (1981) p. 77.
ers,” Chem. Eng., V. 105, No. 5 (1998) p. 78. Walker, R. A. and T. A. Bott, “An Approach to the Prediction of
Sloley, A. W., “Properly Design Thermosyphon Reboilers,” Chem. Fouling in Heat Exchanger Tubes from Existing Data,” Trans.
Eng. Prog., V. 93, No. 3 (1997) p.52. Instn. Chem. Eng., London, V. 51 (1977) pp. 165—167.
Small, W. M., “Not Enough Fouling? You’re Fooling!” Chem. Eng. Wayne, H. P., “How to Keep Outdoor Lines from Freezing,” Power,
Prog., V. 64, No. 3, March (1968) p. 82. March (1955) p. 142.
Small, W. M. and R. K. Young, “The Rod-Baffled Heat Eachanger,” Webb, R. L., “Air-Side Heat Transfer in Finned Tube Heat
Heat Trans. Eng., V. 1, No. 2, Oct.—Dec. (1979) p. 3. Exchangers,” Heat Trans. Eng., V. 1, No. 3, Jan.—March (1980)
Smittle, D., “Maximize Heat Recovery from Hot Flue Gases with p. 33.
Finned Tubing,” Power, V. 124, No. 8 (1980) p.76. Webb, R. L., “The Evolution of Enhanced Surface Geometrics for
Spalding, D. B. and S. Kakac, Turbulent Forced Convection in Channels Nucleate Boiling,” Heat Trans. Eng., V. 2, No. 3—4 (1981) p. 46.
and Bundles, Hemisphere Publishing Corp. Wett, T., “High Flux Heat-Exchange Surface Allows Area to Be Cut
Spencer, R. A., Jr., “Predicting Heat-Excahnger Performance by by Over 80%,” Oil and Gas Journal, Dec. 27 (1971) p. 118.
Successive Summation,” Chem. Eng., Dec. 4, (1978) p. 121. Whitcraft, P. K., “Utilizing Heat Exchanger Tubing Specifications,”
Standiford, F. C., “Effect of Non-Condensables on Condenser Hydrocarbon Processing, V. 78, No. 1 (1999) p. 87.
Design and Heat Transfer,” Chem. Eng. Prog., July (1979) p. 59. Wiebelt, J. A., J. B. Henderson, and J. D. Parker, “Free Convection
Starczewski, J., “Find Tube Side Heat Transfer Coefficient by Heat Transfer from the Outside of Radial Fin Tubes,” Heat
Nomograph,” Hydrocarbon Processing, Nov. (1969) p. 298. Trans. Eng., V. 4, April—June (1980) p. 53.
Starczewski, J., “Graphs Cut Exchanger Design Time,” Heat Willa, J. L., “Improving Cooling Towers,” Chem. Eng., V. 104, No. 11,
Exchanger Design Handbook, Gulf Publishing Company, (1968) (1997) p. 92.
p. 34. Withers, J. G., “Tube-Side Heat Transfer and Pressure Drop for
Starczewski, J., “Short-Cut Method to Exchanger Tube-Side Pres- Tubes Having Helical Internal Ridging and Turbulent/Tran-
sure Drop,” Hydrocarbon Processing, May (1971) p. 122. sitional Flow of Single-Phase Fluid; Part 1 and Part 2 Single
Starczewski, J., “Short-Cut to Tubeside Heat Transfer Coefficient,” Helix Ridging,” Heat Trans. Eng., V. 2, July—Sept., Oct.—Dec.
Hydrocarbon Processing, Feb. (1970) p. 129. (1980) p. 49.
Starczewski, J., “Simplify Design of Parital Condensers,” Hydrocar- Wohl, M. H., “Heat Transfer in Laminar Flow,” Chem. Eng., July 1,
bon Processing, March (1981) p. 131. (1968) p. 81.
Steinmeyer, D. E., “Special Problems in Process Heat Transfer (Fog Wohl, M. H., “Heat Transfer to Non-Newtonian Fluids,” Chem. Eng.,
st
Formation in Partial Condensers),” AIChE 71 Nat’l. Meet- July 15, (1968) p. 127.
ing, Dallas, Feb. (1972). Zanker, A. “Nomograph Determines Heat Flux of Incipient Boil-
Stuhlbarg, D., “How to Find Optimum Exchanger Size for Forced ing,” Heating/Piping/Air Conditioning, May (1978) p. 105.
Circulation,” Hydrocarbon Processing, Jan. (1970) p. 149. Zuber, N., ASME Heat Transfer Transactions, V. 80, (1958).
Sultan, M. and R. L. Judd, “Interaction of the Nucleation Phe-
nomena at Adjacent Sites in Nucleate Boiling,” Journal of Heat
Transfer, V. 105, No. 3 (1983) p. 3.
Taborek, J., “Evolution of Heat Exchanger Design Techniques,”
Heat Trans. Eng., V. 1, No. 1, July—Sept. (1979) p. 15.