Page 112 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
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            AT029-Manual
                        AT029-Manual-v7.cls
                                           June 22, 2007
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  AT029-03
         92 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
















                            FIG. 3.6—A GC for measurement of boiling point of products (courtesy of KISR).

         presented in terms of the temperature versus vol% vaporized.  3.1.1.5 Distillation at Reduced Pressures
         It involves a series of experiments at constant atmospheric  Atmospheric distillation curves present boiling points of
         pressure with total vapor in equilibrium with the unvapor-  products from an atmospheric distillation column. For prod-
         ized liquid. In fact to determine each point on the EFV curve  ucts such as heavy gas oils that contain heavy compounds and
         one experiment is required. To have a full shape of an EFV  may undergo a cracking process during vaporization at atmo-
         curve at least five temperatures at 10, 30, 50, 70, and 90 vol%  spheric pressure, distillation data are measured at reduced
         vaporized are required. EFV distillation curves are useful in  pressures from 1 to 760 mm Hg. The experimental procedure
         the design and operation of overhead partial condensers and  is described in ASTM D 1160 test method (see Fig. 3.7). Distil-
         bottom reboilers since the EFV temperatures represent actual  lation of heavy petroleum fractions is normally presented at
         equilibrium temperatures. In contrast with TBP, the EFV ini-  1, 2, 10, or 50 mm Hg. Both a manual and an automatic
         tial temperature of a mixture is greater than the IBP of ASTM  method are specified. The temperature of the vapor should
         D 86 curve, while the FBP from a EFV curve is lower than the  not exceed 400 C (750 F). ASTM D 1160 distillation data are
                                                                                 ◦
                                                                           ◦
         FBP from the TBP curve for the same mixture. EFV curves at  measured more accurately than ASTM D 86 since it is con-
         pressures above atmospheric up to pressures of 15 bar may  ducted at low pressure. For this reason ASTM D 1160 curves
         also be useful for design and operation of vaporizing or con-  are closer to TBP curves at the same pressure base. Con-
         densing vessels under pressure.                      version of distillation data from low pressure to equivalent


























                                 FIG. 3.7—An apparatus for experimental measurement of boiling point
                                at reduced pressures by ASTM D 1160 test method (courtesy of KISR).











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