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They may be able to recommend more compact geometries which have greater heat transfer surface per unit volume than those recommended here Manufacturers often have additional design information which allows selection of a more economical geometry For example, for some situations a second and a third coil (Marshall and Yazdani, 1970; Hicks and Gates, 1975), may be economical, although the heat transfer coef cients will be reduced for the middle and outer coils in a three-coil band to about 60 and 40%, respectively, of the inner coil according to Marshall and Yazdani (1970) 14-333 Baf e Pipes and Plate Coil Baf es The recommended geometries are presented in Figure 14-4 The baf e pipes can be placed either radially across the vessel or at an angle of 45 with the vessel radius.

81 V Fattore, M M Mauri, G Oriani, and G Paret, Hydrocarbon Process, Int Ed 60(8), 101 (1981) 82 A Convers, B Juguin, and B Trock, Hydrocarbon Process, Int Ed 60(3),95 (1981) 83 M Miranda, Hydrocarbon Process, Int Ed 66(8),51 (1987) 84 A Clementi, G Oriani, F Ancillotti, and G Pecci, Hydrocarbon Process 58(12), 109 (1979) 85 K R Masters and E A Prohaska, Hydrocarbon Process, Int Ed 67(8),48 (1988) 86 A Aguila and J D Penrod, in Encyclopedia of Chemical Processing and Design, Vol 1, J J McKetta and W A Cunningham, eds, Marcel Dekker, New York, 1976, p 114 87 H J Hagemeyer, in Kirk-Othmer Encyclopedia of Chemical Technology, 4th ed, Vol 1, J1 Kroschwitz and M Howe-Grant, eds, Wiley-Interscience, New York, 1991, p 94 88 K Weissermel and H-J Arpe, Industrial Organic Chemistry, 2nd ed.

, VCH, Weinheim, 1993, 7, p 161 89 Petrol Refiner 40(11),207 (1961) 90 D F Othmer, K Kon, and T Igarashi, Ind Eng Chem 48, 1258 (1956) 91 C M Sharts and W A Sheppard, Org React (NY) 21, 125 (1974) 92 R C Larock and W W Leong, in Comprehensive Organic Synthesis, B M Trost and 1 Fleming, eds, Vol 4: Additions to and Substitutions at C-C n-Bonds, M F Semmelhack, ed, Pergamon Press, Oxford, 1991, 17, p 269 93 N Yoneda, Tetrahedron 47, 5329 (1991) 94 G A Olah, J T Welch, Y D Vankar, M Nojima, 1 Kerekes, and J A Olah, J Org Chem 44, 3872 (1979) 95 G A Olah, M Nojima, and 1 Kerekes, Synthesis 779 (1973) 96 G A Olah, J G Shih, and G K S Prakash, in Fluorine: The First Hundred Years, R E Banks, D W A.

With radial positioning, four pipes per baf e are recommended; and with angled positioning, ve pipes per baf e are recommended The experimental work discussed later was done with four baf es When using plate coils, more than four baf es are used; in fact, as many as 16 angled plate coils have been installed in agitated vessels Probably six baf es would have little effect on the heat transfer coef cient; however, above some number, perhaps six, the heat transfer coef cient will be reduced as additional plate coils are added For more than six baf es, a manufacturer of plate coils and/or a manufacturer of uid mixing equipment should be consulted..

Object Size: As described earlier in this chapter and in 4, you can type entries in any of the Size palette s six text boxes to change the location and dimensions of the currently selected object in a layout. To display the Size palette (illustrated previously in Figure 6-21), choose View Object Size. FileMaker Pro maintains an invisible grid corresponding to current ruler settings. If the grid is on, objects being moved or resized move in grid increments, snapping to the nearest grid intersection. Choose Arrange Object Grids ( +Y/Ctrl+Y) to toggle the grid on and off. To change the spacing and units for the grid and rulers, choose Layouts Set Rulers and select new settings in the Set Rulers dialog, as shown in Figure 6-34.