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Figure 6  Dual polarity ac/dc field.

                     3.  Variable gradient field for maximum salt reduction. If the field
                         gradient is increased beyond a certain limit (E c ), this will shatter
                         the drops; it is expressed as
                                      
 1=2

                               E c   k
                                      d
                        where k is the dielectric constant, 
 is the interfacial tension, and d
                        is the drop diameter. Thus, the drop size can be controlled by the
                        field gradient. The electric field can be used both to mix and
                        separate the drops.
                       By cycling the field strength, the process can be repeated many times
                 during the retention time of the drops within the electric field. Voltage
                 modulation will create mixing, coalescence, and settling, as shown in
                 Figure 7. The electrostatic field causes the dipolar water molecules to align
                 with the field.
                      In the electrical desalting process, a high potential field (16,500–
                 33,000 V) is applied across the settling vessels to help coalescence, as
                 shown in Figure 8. The chemielectric concept utilizing both chemical
                 agents and electrical field is schematically illustrated in Figure 9.
                      In the desalting process, it is a common practice to apply enough
                 pressure to suppress any loss of hydrocarbon due to vaporization of
                 the oil. The pressure normally used in a desalting process is in the range
                 50–250 psi.






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