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Moreover, hydrochloric acid can be produced as a byproduct of crude oil desalting process and some oil refinery treatments [2].
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For example, crude oil desalting processes normally use dispersion valves to mix the dilution water.
For high salt-contenting crude oil (40-70 mg·L−1), the salt content is still above 10.0 mg·L−1 after crude oil has been treated by two-stage electric desalting process in refinery, which cannot meet the need of refinery.
The results show that the ultrasonic-electric united process is more effective than the electric process in high salt-contenting oil desalting.
Electrical desalter is an effective method in crude oil desalting.
If one stage of desalting process could not achieve the norm, two stages of desalting process should be considered.
Next to multistage flash distillation, reverse osmosis is the second-ranking desalting process.
Experiments in both the laboratory and field have shown the desalting process parameters to be very complicated.
Conditions in the Cienega and Santa Clara Slough could be altered by operation of the Yuma Desalting Plant (YDP), which will divert water from the Cienega and replace it with brine water resulting from the desalting process.
Field results were used to project and compare the economics of the seawater RO desalting process using conventional and membrane pretreatment.
The preference of one scheme over another would depend mainly on many factors, such as the required power to water ratio, cost of fuel energy charged to the desalting process, electricity sales, capital costs, and local requirements.
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