Method for removing asphalt in raw oil
A technology for raw oil and deasphalting tower, which is applied in the petroleum industry, processing hydrocarbon oil, and only multi-stage series refining process treatment, etc., can solve the problems of low processing capacity, low yield of deasphalted oil, and low separation efficiency , to achieve the effect of improving separation efficiency, rapid phase separation, and increasing separation rate
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Embodiment 1
[0046] A method for removing bitumen in raw oil, comprising the following steps:
[0047] (1) Mix the vacuum residue and n-pentane in a mass ratio of 1:1 to form a residue mixture;
[0048] (2) Heat the mixture to 150°C and enter the electric field treatment device from the upper part of the electric field treatment device; wherein, the electric field strength in the upper area of the electric field treatment device is 10000V / cm, the middle area is 5000V / cm, and the electric field in the bottom area The strength is 0; the residence time of the residual oil mixture in the electric field treatment device is 15min.
[0049] (3) The residual oil mixture treated by the electric field treatment device enters the deasphalting tower from the middle part of the deasphalting tower for sedimentation and separation.
[0050] (4) The deasphalted oil mixture discharged from the upper part of the deasphalting tower and the deoiled bitumen mixture discharged from the bottom enter the solve...
Embodiment 2
[0053] A method for removing bitumen in raw oil, comprising the following steps:
[0054] (1) Mix the vacuum residue and n-pentane in a mass ratio of 1:1 to form a residue mixture;
[0055] (2) Heat the mixture to 150°C and enter the electric field treatment device from the upper part of the electric field treatment device; wherein, the electric field strength in the upper area of the electric field treatment device is 10000V / cm, the middle area is 1000V / cm, and the electric field in the bottom area is 10000V / cm. The strength is 0; the residence time of the residual oil mixture in the electric field treatment device is 30min.
[0056] (3) The residual oil mixture treated by the electric field treatment device enters the deasphalting tower from the middle part of the deasphalting tower for sedimentation and separation.
[0057] (4) The deasphalted oil mixture discharged from the upper part of the deasphalting tower and the deoiled bitumen mixture discharged from the bottom e...
Embodiment 3
[0060] A method for removing bitumen in raw oil, comprising the following steps:
[0061] (1) Mix the vacuum residue and n-pentane in a mass ratio of 1:1 to form a residue mixture;
[0062] (2) Heat the mixture to 150°C and enter the electric field treatment device from the upper part of the electric field treatment device; wherein, the electric field strength in the upper area of the electric field treatment device is 8000V / cm, the middle area is 5000V / cm, and the electric field in the bottom area The strength is 0; the residence time of the residual oil mixture in the electric field treatment device is 60min.
[0063] (3) The residual oil mixture treated by the electric field treatment device enters the deasphalting tower from the middle part of the deasphalting tower for sedimentation and separation.
[0064] (4) The deasphalted oil mixture discharged from the upper part of the deasphalting tower and the deoiled bitumen mixture discharged from the bottom enter the solven...
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