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Table 1 Properties of Crude Oils Shipped to Refineries

                                                           Range            Average
                  Water in crude, % by volume of crude     0.1–2.0          0.3–0.5
                  Salt content in crude, PTB               10–250           60–130
                  Salt concentration in brine, wt%         0.4–25             —
                  Salt concentration in brine, ppm       4,000–250,000        —
                  Source: Ref. 1.


                  Table 2 Average Values for the PTB for Some
                  Typical Crude Oils

                  Source of oil         Avg. salt content (PTB)
                  Middle East                     8
                  Venezuela                      11
                  United States
                    Pennsylvania                  1
                    Wyoming                       5
                    East Texas                   28
                    Gulf Coast                   35
                    Oklahoma and Kansas          78
                    West Texas                  261
                  Canada                        200


                  The method of reducing the PTB by lowering the quantity of remnant
                  water W R is usually referred to as the treating process of oil dehydration.
                  This was the main theme of the last chapter. The other alternative of
                  reducing the PTB is to substantially decrease the dissolved salt content of
                  the remnant water (i.e., its concentration, S R ). This practice is the one we
                  are dealing with in this chapter and is known as desalting. Desalting of
                  crude oil will eliminate or minimize problems resulting from the presence
                  of mineral salts in crude oil. These salts often deposit chlorides on the heat
                  transfer equipment of the distillation units and cause fouling effects. In
                  addition, some chlorides will decompose under high temperature, forming
                  corrosive hydrochloric acid [3]:
                                 High temp:
                      MgCl ðaq:Þ   !    MgðOHÞ þ HCl                            ð2Þ
                           2                   2
                                   H 2 0
                  The removal of these salts is aimed at providing an economical operating
                  cycle in the refining process of crude oil. The reduction of salt content
                  down to 5 PTB is feasible. Even with this low salt content, it has been






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