Method for extracting and separating aromatic hydrocarbon and saturated hydrocarbon in catalytic cracking slurry oil
A technology for catalytic cracking of oil slurry and aromatic hydrocarbons is applied in the direction of multi-stage series-connected refining process treatment, etc., and can solve the problems of increasing the scale and processing capacity of the extraction device, adding a large amount of the second solvent, and increasing the cost input, etc. To achieve the effect of reducing processing capacity and operation difficulty, reducing consumption and saving costs
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example 1
[0027] The catalytic cracking oil slurry A was taken as the separation object, and its properties are shown in Table 1.
[0028] At 60°C, add 100g of FCC oil slurry A, 150g of furfural, and 150g of n-octane into a separatory funnel, oscillate fully to mix evenly, and stand to separate into layers to obtain a raffinate phase and an extraction phase. Add 150g of n-octane to the extracted phase to simulate the operation of the second solvent entering the lower part of the first extraction tower, and the obtained n-octane layer is combined with the raffinate phase extracted for the first time to obtain a mixed raffinate phase. 300g of furfural was added therein for the second extraction operation; the obtained raffinate was then extracted with 300g of furfural for the third and fourth times respectively.
[0029] The raffinate after the fourth extraction was concentrated, and 250 g of n-octane was recovered by distillation under reduced pressure, and the quality of the raffinate w...
example 2
[0031] FCC oil slurry B is extracted and separated by the method of example 1, and the properties of FCC oil slurry B are shown in Table 1. Finally obtained raffinate oil 24.7g, its properties are shown in Table 2, and extracted oil 75.1g, its properties are shown in Table 3.
example 3
[0033] FCC oil slurry A is extracted and separated by the method of Example 1, except that the second solvent is changed from n-octane to n-heptane. Obtain raffinate oil 34.3g at last, its properties are shown in Table 2, and extracted oil 65.6g, its properties are shown in Table 3.
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