Page 320 - Applied Process Design For Chemical And Petrochemical Plants Volume III
P. 320

66131_Ludwig_CH10H-J  5/30/2001 4:47 PM  Page 279










                                                                    Heat Transfer                                          279

                                          Subscripts                         4.  Banchero, J. T., G. E. Barker, and R. H. Boll, “Stable Film Boil-
                                                                               ing of Liquid Oxygen Outside Single Horizontal Tubes and
                                 —
                                      bar over symbol   average value.         Wires,” Chem. Eng. Prog. Sym. Series, No. 17, “Heat Transfer—
                                 1   inlet condition.                          St. Louis,” V. 51, p. 21, (1955).
                                 2   outlet condition.                       5.  Bergelin, O. P., W. L. Lafferty, Jr., M. D. Leighton, R. L. Pigford,
                                 A   point A in flow loop, Figure 10-110.      “Heat Transfer and Pressure Drop during Viscous and Turbu-
                                 B   point B in flow loop, Figure 10-110.      lent Flow across Baffled and Unbaffled Tube Banks,” University
                            A, B, etc.   component identification.             of Delaware, Eng. Exp. Sta., Newark, Del. Bul. No. 4 (1958).
                           A v or avg.   average of limits of function, inside and out-  6.  Boilers, Power, Section I, ASME Boiler and Pressure Vessel Code
                                                              2
                                      side tube area for unit length, ft /ft.  ASME, 345 East 47th Street, New York, N.Y. (1980)
                                 D   dirty or under operating conditions; or,  7.  Bowman, R. A., Misc. Papers, No. 28, p. 75, ASME, New York,
                                      overhead distillate.                     N.Y. (1936).
                                 E   exit reboiler vapor.                    8.  Bowman, R. A., A. C. Mueller, and W. M. Nagle, “Mean Tem-
                                 F   friction.                                 perature Difference in Design,” Trans. ASME, V. 62, pp. 283—
                                 L   liquid.                                   294 (1940).
                                 T   total.                                  9.  Bras, G. A. P., “Shortcut to Cooler Condenser Design,” Chem.
                                 b   boiling condition; or, bottoms material.  Eng., V. 60, No. 4, p. 223, No. 5, p. 230 (1953), and V. 61, No.
                                  c   clean, or cold end; or, correction; or, con-  5, p. 190 (1954).
                                      densing; or, critical condition.      10.  Bras, G. H. P., “How to Design Cooler Condensers,” Pet. Ref.,
                                 d   diffusional.                              V. 35, No. 6, p. 177 (1956).
                                  f   film conditions; or, force.           11.  Bras, G. H. P., “A Graphical Method for the Calculation
                              f p  or f   process-side fouling; or, tube-side fouling.  of Cooler Condensers,”  Chem. Eng. Science (London), V. 6,
                                 g   gas.                                      pp. 277—282 (1957).
                            h or hot   hot end; or, hot fluid; or, heating medium.  12.  Bras, G. H. P., “The Graphical Determination of Changes in
                                  i   inside                                   the Gas Phase Due to Simultaneous Heat and Mass Transfer,”
                              l or L   liquid.                                 Chem. Eng. Science (London), V. 9, pp. 176—181 (1958).
                           lm or Lm   log mean.                             13.  “Braun Heat Exchangers,” Bul. 4901, C. F. Braun & Co.,
                                 m   mass.                                     Alhambra, CA. (1949).
                                 o   outside                                14.  Bromley, L. A., “Heat Transfer in Stable Film Boiling,” Chem.
                                 p   process on boiling side.                  Eng. Prog., V. 46, pp. 221 (1950).
                                 m   mean; or, metal.                       15.  Brooks, G. and Gouq-Jen Su, “Heat Transfer in Agitated Ket-
                               max   maximum.                                  tles,” Chem. Eng. Prog., V. 55, No. 10, p. 55 (1959).
                               min   minimum.                               16.  Bul., “An Opportunity,” Wolverine Tube, Inc.
                                  r   radiation.                            17.  Bul., “Elements of Heat Exchanger Engineering,” C. F. Braun
                                  s   steam; or, shell-side of exchanger; or, sur-  and Co., Alhambra, CA (1957).
                                      face; or, saturation temperature.     18.  Bul. 2401, Griscom-Russell Co., Massillon, OH (1960).
                                 sv   saturated vapor.                      19.  Bul. Dowington Iron Works.
                                  t   tube; or, total.                      20.  Bul. HT-23, Heat Transfer Div. National-U.S. Radiator Corp.,
                                 tp   two phase.                               342 Madison Ave., New York, N. Y.
                                  v   vapor.                                21.  Bul., “Design and Cost Comparison of Heat Exchangers
                                 w   wall or surface.                          Using Wolverine Trufin,” Wolverine Tube, Inc. (1959).
                                air   air side.                             22.  Buthod, A. P., “How to Estimate Heat Exchangers,” Oil and
                               cold   cold side, may   air.                    Gas Jour., V. 58, No. 3, p. 67 (1960).
                                                                            23.  Cairns, R. C., “Approximation Methods for Designing Cooler-
                                              References                       Condensers,” Chem. Eng. Science, V. 3, p. 215 (1954).
                                                                            24.  Chase, J. C. and H. E. Degler, “Economics of the Air-Cooled
                       1.  Akers, W. W., H. A. Deans, and O. K. Crosser, “Condensing  Heat Exchanger,” Pet. Engr., p. C-42, Jan. (1953).
                         Heat Transfer within Horizontal Tubes,” Chem. Eng. Prog. Sym.  25.  Chen, Ning Hsing, “Save Time in Heat Exchanger Design,”
                         55, No. 29, p. 171 (1959). Also abstract in Chem. Eng. Prog.,   Chem. Eng., V. 65, p. 153, Oct. 20, (1958).
                         V. 54, No. 10, p. 89 (1958).                       26.  Chen, Ning Hsing, “Condensing and Boiling Coefficients,”
                       2.  Anderson, E. D. and E. W. Flaxbart, “Economics of Design of  Chem. Eng., V. 66, p. 141, Mar. 9, (1959).
                         Heat Exchangers,” presented at Ninth Annual Pet. Mech.  27.  Cichelli, M. T. and C. F. Bonilla, “Heat Transfer to Liquids Boil-
                         Eng. Conf., ASME, Sept. 1954, Los Angeles, CA.        ing Under Pressure,” Trans. AIChE, V. 41, No. 6, p. 755 (1945).
                       3.  Baker, C. K. and G. H. Waller, “Application of Dynamic Mod-  28.  Chilton, T. H. and R. P. Genereaux, “Pressure Drop across
                         eling Technique to the Analysis and Prediction of Heat Trans-  Tube Banks,” Trans. AIChE, V. 29, p. 161 (1933).
                         fer with Particular Reference to Agitated Vessels,” Heat Trans.  29.  Clements, L. D. and C. P. Colver, “Film Condensation of
                         Eng., V. 2, p. 28, Oct.—Dec. (1979).                  Light Hydrocarbons and Their Mixtures in a Vertical Reflux
   315   316   317   318   319   320   321   322   323   324   325