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76. Lee, R. P., “Heat Transfer through Coated Metal Surfaces,” 97. Rohsenow, W. and P. Griffith, “Correlation of Maximum
presented at National Association of Corrosion Engineers Heat-Flux Data for Boiling of Saturated Liquids,” presented
13th Annual Conference, March (1957), pub. Corrosion, V. 14, at ASME Meeting, Louisville, Ky., March (1955).
p. 42. 98. Rubin, F. L., “Heat Transfer Rates for Gases,” Pet. Ref., V. 36,
77. Levy, S., “Generalized Correlation of Boiling Heat Transfer,” No. 3, p. 226 (1957).
Paper No. 58-HT-8, presented AIChE—ASME Joint Heat 99. Rubin, F. L., “What’s the Difference between TEMA
Transfer Conference, Chicago, Aug. 1958, pub. ASME Journal Exchanger Classes,” Hydrocarbon Processing, V. 59, p. 92, June
of Heat Transfer (1959). (1980).
78. Linde Div., Union Carbide Corp., bulletins related to high 100. Rubin, F. L. and N. R. Gainsboro, “Latest TEMA Standards for
flux tubing. Shell and Tube Exchnagers,” Chem. Eng., V. 86, p. 11, Sept. 24,
79. Madejski, J., “Design of Cooler Condensers,” British Chem. (1979).
Eng., p. 148, March (1959). 101. Seider, E. N. and G. E. Tate, “Heat Transfer and Pressure
80. Mathews, R. R., “Air Cooling in Chemical Plants,” Chem. Eng. Drop of Liquids in Tubes,” Ind. Eng. Chem., V. 28, p. 1429
Prog., V. 55, No. 5, p. 68 (1959), and as presented at AIChE (1936).
meeting, Cincinnati, OH, December (1958). 102. Short, B. E., “Heat Transfer and Pressure Drop in Heat
81. McAdams, W. H., Heat Transmission, 2 nd Ed., McGraw-Hill Exchangers,” Engineering Research Series No. 37, University
Book Co., Inc. New York, N.Y. (1942). of Texas, Austin, TX, pub. No. 4324, pp. 1—55 (1943).
82. McAdams, W. H., Heat Transmission, 3 rd Ed., McGraw-Hill 103. Skiba, E. J., “Practical Finned Tube Design,” Chem. Eng., p.
Book Co., Inc. New York, N.Y. (1954). 183, Dec. (1954).
83. McAdams, W. H., T. B. Drew, and G. S. Bays, Jr., “Heat Trans- 104. Skrotzki, B. G. A., “Heat Exchangers,” Power, June (1954).
fer to Falling-Water Films,” Trans. ASME, V. 62, p. 627 (1940). 105. Small, W. M. and R. K. Young, “The Rodbaffle Heat
84. McAdams, W. H., W. K. Woods, and R. L. Bryan, “Vaporiza- Exchanger,” Heat Trans. Eng., V. 1, No. 2, p. 21, Oct.—Dec.
tion Inside Horizontal Tubes,” Trans. ASME, V. 63, p. 545 (1979).
(1941). 106. Smith, E. C., “Air Cooled Heat Exchangers,” Chem. Eng., V. 65,
85. McAdams, W. H., W. K. Woods, and L. C. Heroman, Jr., p. 145 (1958).
th
“Vaporization Inside Horizontal Tubes—II, Benzene-Oil Mix- 107. Standards of Tubular Exchanger Manufacturers Association, 6 Ed.
th
tures,” Trans. ASME, V. 61, p. 193 (1942). (1978) and 7 Ed. (1988), The Tubular Exchanger Manufac-
86. Mikic, B. B. and W. M. Rohsenow, “A New Correlation of turers Association, Inc., Tarrytown, N.Y. (also see No. 266).
st
Pool Boiling Data Including the Effect of Heating Surface 108. Stoever, H. J., Applied Heat Transmission, 1 Ed., McGraw-Hill
Characteristics,” ASME Jour. Heat Trans., V. 91, p. 245, May Book Co., Inc., New York, N.Y. (1941).
(1969). 109. Stoever, H. J., “Heat Transfer,” Chem. and Met. Eng., p. 98, May
87. Nakayama, E. V., “Optimum Air Film Cooler Design,” Chem. (1944).
Eng. Prog., V. 55, No. 4, p. 46 (1959). 110. Stuhlbarg, D., “How To Design Tank Heating Coils,” Pet. Ref.,
88. Nauss, V., private discussions, Griscom-Russell Co., Massillon, V. 38, No. 4, p. 143 (1959).
OH (1960). 111. Taborke, J. J., “Organizing Heat Exchanger Programs on Dig-
89. Nelson, W. L., “Fouling Factors—Crude Oil and Water,” Oil ital Computers,” Chem. Eng. Prog., V. 55, No. 10, p. 45 (1959).
and Gas Jour., No 94 in series. 112. Taylor, J. A., “How Solid Deposits Affect Heat Transfer,” Chem.
90. Palen, J. W. and W. M. Small, “A New Way to Design Kettle Eng., V. 60, No. 8, p. 192 (1953).
and Internal Reboilers,” Hydrocarbon Processing, V. 43, No. 11, 113. Test, F. L., A Study of Heat Transfer and Pressure Drop Under
p. 199 (1964). Conditions of Laminar Flow in the Shell Side of Cross Baffled
91. Palen, J. W. and J. J. Taborek, “Refinery Kettle Reboilers,” Heat Exchangers, Paper No. 57-HT-3, ASME—AIChE Heat
AIChE Nat’l. Heat Transfer Conference, Chem. Eng. Prog., V. Transfer Conference, ASME, New York, NY (1957).
58, No. 7, p. 37 (1962). 114. Thomas, J. W., “Air vs. Water Cooling—Cost Comparison,”
92. Peiser, A. M., “Design of Heat Exchangers on Automatic Chem. Eng. Prog., V. 55, No. 4, p. 38 (1959).
Computers,” The Refining Engr., p. C-12, Oct. (1957). 115. Thronton, D. P., “Water Scarce—Natural Gasoline Plant Uses
93. Perkins, B. G., “Heat Removal—with Water or Air,” Chem. Eng. Air for 80% of Required Cooling,” Petroleum Processing, V. 2, p.
Prog., V. 55, No. 4, p. 41 (1959). 52, Jan. (1947).
94. Perry, John H. (Ed), Chemical Engineers Handbook, 3 rd Ed. 116. Tinker T., “Shell-Side Characteristics of Shell-And-Tube Heat
McGraw-Hill Book Co, Inc. (1950). Exchangers,” Paper No. 56A-123, presented at ASME Meet-
94A. Green, D. W. (Ed) and J. O. Maloney, Perry’s Chemical Engineers’ ing, New York, Nov. (1956).
th
Handbook, 6 Ed., McGraw-Hill, Inc. All rights reserved. (1984). 117. Todd, J. F., “Field Performance Testing of Air Cooled Heat
95. Ramdas, V., V. W. Uhl, M. W. Osborne, and J. R. Ortt, “Heat Transfer Equipment,” presented at A.I.Ch.E meeting, Dec.
Transfer in a Scraped-wall Continuous Unit,” Heat Transfer (1958) .
Eng., V. 1, No. 4, p. 38 (1980). 118. Uhl, V. W., “Heat Transfer to Viscous Materials in Jacketed
96. Revilock, J. F., H. Z. Hurlburt, D. R. Brake, E. G. Lang, and D. Agitated Kettles,” Chem. Eng. Prog., Sym. Series 51, No. 17, p.
Q. Kern, “Heat and Mass Transfer Analogy,” Chem. Eng. Prog., 93, AIChE, New York (1955).
V. 55, No. 10, p. 40 (1959). 119. Unfired Pressure Vessels, Section VIII, ASME Boilers and Pres-
sure Vessel Code (Latest Edition), ASME, 345 E. 47th Street,
New York, N.Y.