Heavy oil separation method
A separation method and heavy oil technology, applied in the multi-stage series refining process, etc., can solve the problems of reduced solubility, long extraction time, and reduced density, and achieve the effect of preventing entrainment and increasing separation efficiency.
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Embodiment 1
[0024] Send 1000g of Iranian residue-reducing feedstock oil into the primary extraction tower, use n-pentane and n-butane as the solvent in a 1:1 mixture, and the extraction temperature ranges of the primary extraction tower are 31, 32, and 33. 210°C, 220°C, the extraction temperature range of the secondary extraction tower 41, 42, and 43 temperatures are divided into: 160°C, 170°C, 180°C, and the volume space velocity of the mixed solvent is 6h -1 , the initial stable pressure of extraction is 3.9MPa, and the pressure is increased linearly to 12 MPa, and the pressure increase rate is 1.0 MPa / h r , taking 10% as the narrow fraction cut point, Iran can be cut into 7 narrow fractions and one residue.
Embodiment 2
[0031] Send 1000g of Luolian residue reduction raw material oil into the extraction kettle, use n-pentane and n-butane as the solvent in a 1:1 mixture, and the extraction temperature range of the first-stage extraction tower is 31, 32, and 33. The temperature is divided into: 200°C, 210°C ℃, 220℃, and the extraction temperature range of the secondary extraction tower 41, 42, 43. The temperature is divided into: 160℃, 170℃, 180℃, and the solvent space velocity is 6h -1 , the extraction initial stable pressure is 3.9MPa, linearly increase the pressure to 12MPa, and the pressure increase rate is 1.0 MPa / h r , with 5% as the narrow fraction cut point, Iran can be cut into 12 narrow fractions and one residue.
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