A method and system for continuous separation and recovery of carbonate-rich oil sands
A technology for separation and recovery of carbonates, which is applied in the petroleum industry, the preparation of liquid hydrocarbon mixtures, etc., to achieve the effects of cost reduction, convenient and easy access to raw materials, and reduction of environmental protection treatment costs
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Embodiment 1
[0056] A continuous separation system and method for carbonate-rich oil sands, the specific operations are as follows:
[0057] (1) 15kg of oil sand (carbonate content 42%, maximum particle size 0.5cm) crushed by crushing device A is sent to mixing-reactor B (three reactors are used alternately in parallel) and hydrochloric acid with a pH of 1 according to the solid-liquid The ratio is 1:30 (mass ratio), fully mixed and reacted at room temperature for 1 hour.
[0058] (2) After the degassing operation, 0.5 times the volume of pentane is added to the obtained asphalt foam for solid-liquid separation (secondary sedimentation and first-stage centrifugation), and the moisture content in the upper oil phase clear liquid obtained after separation is less than 3.5%, and the solid content is less than 1.5%. enter E for separation, recover the solvent, and obtain the asphalt oil product 14 at the same time, and the asphaltene content in the asphalt oil product is less than 10%.
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Embodiment 2
[0064] A continuous separation system and method for carbonate-rich oil sands, the specific operations are as follows:
[0065] (1) 15kg of oil sand (carbonate content 61%, maximum particle size 5cm) crushed by crushing device A is sent into mixing-reactor B (four reactors are used in parallel and alternately) and hydrogen bromide with a concentration of 5 mol / liter The acid is fully mixed at room temperature according to the solid-liquid ratio of 1:3 (mass ratio), and reacted for 120 minutes.
[0066] (2) After the degassing operation, the obtained asphalt foam is added with 5 times the volume of heptane for solid-liquid separation (first-stage sedimentation and third-stage centrifugation), and the moisture content in the upper oil phase clear liquid obtained after separation is less than 1.5%, and the solid content is less than 1.5%. enter E for separation, recover the solvent, and obtain the asphalt oil product 14 at the same time, and the asphaltene content in the asphalt ...
Embodiment 3
[0072] A continuous separation system and method for carbonate-rich oil sands, the specific operations are as follows:
[0073] (1) 15kg of oil sludge (carbonate content 56%, maximum particle size 1.5cm) pulverized by pulverizing device A is sent into mixing-reactor B (three reactors are used alternately in parallel) and nitric acid with a concentration of 3 mol / liter according to The solid-liquid ratio is 1:3 (mass ratio), fully mixed at room temperature, and reacted for 120 minutes.
[0074] (2) After the degassing operation, 5 times the volume of hexane is added to the obtained asphalt foam for solid-liquid separation (two-stage sedimentation and three-stage suspension), and the moisture content in the upper oil phase clear liquid obtained after separation is less than 1.5%, and the solid content is less than 1.5%. , enter E for separation, recover the solvent, and obtain the asphalt oil product 14 at the same time, the asphaltene content in the asphalt oil product is less ...
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