Heavy oil four-component separation method
A separation method, a four-component technology, applied in the direction of material separation, material analysis, measuring devices, etc., can solve the problems of large amount of solvent, hidden dangers of health, safety and environmental protection of operators, long separation time, etc., to reduce the steps of manual operation, The effect of saving time and solvent consumption, and eliminating the separation step
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Embodiment 1
[0094] use as figure 1 The structure of the four-component separation device for heavy oil is shown.
[0095] In this embodiment, two three-way solenoid valves are used as the pre-column flow path switching valve 5 and the post-column flow path switching valve 8, and software is used to control the pre-column flow path switching valve 5 and the post-column flow path switching valve 8. The chromatographic solvent output from the outlet 4 is switched to be introduced into the chromatographic column 6 or into the bypass line 7 . In order to prevent the asphaltenes flowing out of the bypass line 7 from flowing back into the alumina chromatographic column 6, the pre-column flow path switching valve 5 and the post-column flow path switching valve 8 are set to have the same phase to play a protective role.
[0096] In this embodiment, a glass fiber filter disk is used, an alumina chromatographic column with a filter membrane pore size of 100 μm and a capacity of 12 g, an inner diame...
Embodiment 2
[0118] In this example, using figure 1 Shown is the same heavy oil four-component separation device structure as in Example 1. The same elements or operation steps are not repeated here. The difference between this embodiment and embodiment 1 is:
[0119] In this embodiment, the glass fiber filter disc used, the pore diameter of the filter membrane is 0.1 μ m and the capacity of 2 g, the inner diameter of the column tube of the chromatographic column is 8 mm, and the length of the column bed layer is 50 mm. The alumina chromatographic column has a packing density of 0.8 g / mL. The mass of particles with a particle size of 60-200 microns in alumina accounts for 60% of the total mass, and the specific surface area is 197m 2 / g, the pore volume is 0.29mL / g.
[0120] In the liquid splitting device of this embodiment, the solvent is preheated to 40°C. The metal pipe is made of 316 stainless steel, with an inner diameter of 0.05mm and a length-to-diameter ratio of 50,000:1.
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Embodiment 3
[0142] In this example, using figure 1 Shown is the same heavy oil four-component separation device structure as in Example 1. The same elements or operation steps are not repeated here. The difference between this embodiment and embodiment 1 is:
[0143] In this embodiment, the glass fiber filter disc used, the pore diameter of the filter membrane is 2.0 μ m and the capacity of 20 g, the inner diameter of the chromatographic column tube is 13 mm, and the column bed length is 130 mm. The alumina chromatographic column has a packing density of 1.2 g / mL. The mass of particles with a particle size of 60-200 microns in alumina accounts for 79% of the total mass, and the specific surface area is 152m 2 / g, the pore volume is 0.26mL / g.
[0144] In the liquid splitting device of this embodiment, the solvent is preheated to 60°C. The material of the metal pipe is 316 stainless steel, the inner diameter is 0.5mm, and the length-to-diameter ratio is 5000.
[0145]The receiving de...
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Abstract
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