Page 174 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
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T1: IML
                            QC: —/—
               P2: KVU/KXT
  P1: KVU/KXT
            AT029-Manual
                        AT029-Manual-v7.cls
  AT029-04
                                           June 22, 2007
                                                        21:30
         154 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
                                          TABLE 4.1—Composition of several reservoir fluids.
                            North Sea gas condensate  North Sea oil  Texas gas condensate  Texas oil
                  Component  mol%   SG     M   mol%    SG    M     mol%    SG    M    mol%    SG    M
                  N 2        0.85               0.69               0                   0
                  CO 2       0.65               3.14               0                   0
                  C 1       83.58              52.81              91.35               52.00
                  C 2        5.95               8.87               4.03                3.81
                  C 3        2.91               6.28               1.53                2.37
                  IC 4       0.45               1.06               0.39                0.76
                  nC 4       1.11               2.48               0.43                0.96
                  IC 5       0.36               0.87               0.15                0.69
                  nC 5       0.48               1.17               0.19                0.51
                  C 6        0.60               1.45               0.39                2.06
                  C 7        0.80  0.7243  95   2.39  0.741  91.7  0.361  0.745  100   2.63  0.749  99
                  C 8        0.76  0.7476  103  2.67  0.767  104.7  0.285  0.753  114  2.34  0.758  110
                  C 9        0.47  0.7764  116  1.83  0.787  119.2  0.222  0.773  128  2.35  0.779  121
                             1.03  0.8120  167  14.29  0.869  259.0  0.672  0.814  179  29.52  0.852  221
                  C 10+
                             3.06  0.7745  124  21.18  0.850  208.6  1.54  0.787  141.1  36.84  0.841  198.9
                  C 7+
            --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
                  Source: North Sea gas condensate and oil samples are taken from Ref. [1]. South West Texas gas condensate and oil samples are
                  taken from Ref. [2]. Data for C 7+ have been obtained from data on C 7 ,C 8 ,C 9 ,andC 10+ components.
         boiling point cannot be measured; only molecular weight and  Generation of such data for molecular weight and den-
         specific gravity are available for the plus fractions. Character-  sity distribution from gas chromatography (GC) analysis for
         istics and properties of SCN groups are given later in this  crude oils is shown by Osjord et al. [3]. Detailed composi-
         chapter (Section 4.3).                               tion of SCN groups for C 6+ or C 7+ fractions can also be ob-
                                                              tained by TBP distillation. Experimental data obtained from
                                                              distillation are the most accurate way of analyzing a reser-
                                                              voir fluid or crude oil, especially when it is combined with
                                                              measuring specific gravity of each cut. However, GC analysis
                                                              requires smaller sample quantity, less time, and less cost than
                                                              does TBP analysis. The ASTM D 2892 procedure is a standard
                                                              method for TBP analysis of crude oils [4]. The apparatus used
                                                              in ASTM D 2892, is shown in Fig. 4.1 [5]. A GC for determining
                                                              SCN distribution in crude oils is shown in Fig. 4.2. The out-
                                                              put from this GC for a Kuwaiti crude oil sample is shown in
                                                              Fig. 4.3. In this figure various SCN from C 5 up to C 40 are iden-
                                                              tified and the retention times for each carbon group are given
                                                              on each pick. A comparison of molecular weight and specific
                                                              gravity distribution of SCN groups obtained from TBP distil-
                                                              lation and GC analysis for the same crude oil is also shown by
                                                              Osjord et al. [3]. Pedersen et al. [6] have also presented com-
                                                              positional data for many gas condensate samples from the
                                                              North Sea. An extended composition of a light waxy crude
                                                              oil is given in Table 4.2 [7]. Distribution of SCN groups for
                                                              the Kuwait crude determined from Fig. 4.3 is also given in
                                                              Table 4.2. Other properties of SCN groups are given in
                                                              Section 4.3. One of the important characteristics of crude oils
                                                              is the cloud point (CPT). This temperature indicates when the
                                                              precipitation of wax components in a crude begins. Calcu-
                                                              lation of CPT requires liquid–solid equilibrium calculations,
                                                              which are discussed in Chapter 9 (Section 9.3.3).


                                                              4.1.2 Crude Oil Assays
                                                              Composition of a crude may be expressed similar to a reser-
                                                              voir fluid as shown in Table 1.1. A crude is produced through
                                                              reducing the pressure of a reservoir fluid to atmospheric
                                                              pressure and separating light gases. Therefore, a crude oil
                                                              is usually free of methane gas and has a higher amount
                                                              of C 7+ than the original reservoir fluid. However, in many
                                                              cases information on characteristics of crude oils are given
          FIG. 4.1—Apparatus to conduct TBP analysis of crude oils  through crude assay. A complete data on crude assay contain
         and reservoir fluids (courtesy of KISR [5]).          information on specification of the whole crude oil as well














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