Combined process for processing heavy oil
A combined process and heavy oil hydrogenation technology, which is applied in the fields of hydrogenation treatment process, petroleum industry, hydrocarbon oil treatment, etc., can solve the problems of high colloid and asphaltene content, difficult to use hard asphalt, harsh operating conditions, etc. The effects of reducing quality and asphaltene content, reducing carbon residue value, and prolonging the start-up period
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Embodiment 1
[0037] Processing sand light and heavy oil.
[0038] Shaqing vacuum residue is divided into two parts, wherein one part accounting for 48% by weight of the total weight of Shaqing vacuum residue is used as the feedstock of the solvent deasphalting device; the other part accounting for 52% by weight of the total weight of Shaqing vacuum residue The deoiled bitumen produced by the solvent deasphalting unit is mixed with the deoiled asphalt produced by the solvent deasphalting unit as the feed of the delayed coking unit; the feed of the heavy oil hydrotreating unit is: mixed oil of vacuum wax oil, deasphalted oil and coker heavy oil. Solvent deasphalting test, delayed coking test and heavy oil hydrotreating test were all carried out on medium-scale test equipment.
[0039] Adopting this process route can prevent the light sand and normal slag from being directly used as the feed of the heavy oil hydrotreating unit, thereby reducing the operating severity of the heavy oil hydrotre...
Embodiment 2
[0060] Processing sand light and heavy oil.
[0061] Atmospheric residue is divided into two parts, and one part that accounts for 92.5% by weight of the total weight of atmospheric residue obtains vacuum wax oil and vacuum residue after vacuum distillation, and the other part that accounts for 7.5% by weight of the total weight of atmospheric residue One part enters the heavy oil hydrotreating unit. The vacuum residue obtained after vacuum distillation is also divided into two parts, wherein one part accounting for 50.0% by weight of the total weight of the vacuum residue is blended with catalytic cracking oil slurry and heavy coking wax oil as the feed of the solvent deasphalting unit. The deasphalted oil was obtained after the feed was deasphalted with a mixed solvent, and the yield of the deasphalted oil was 84.6m%. The properties are shown in Table 6. The other part, accounting for 50.0% by weight of the total weight of the vacuum residue, enters the heavy oil hydrotreat...
Embodiment 3
[0069] This technical scheme processes Iranian normal slag with poor processing properties. Its processing technology route is that the Iranian slag is directly used as the feed of the solvent deasphalting unit; the deoiled asphalt is used as the feed of the delayed coking unit; Oil replaces the original Iranian slag and directly enters the heavy oil hydrotreating unit. Hydrotreated heavy oil is used as feedstock for catalytic cracking units. Solvent deasphalting test, delayed coking test and heavy oil hydrotreating test were all carried out on the medium-scale test unit.
[0070] The Iranian slag is used as the raw material oil of the solvent deasphalting test device. The solvent used is mainly pentane, mixed with a small part of butane, and the weight ratio is 85:15. The test temperature is 175 °C and the pressure is 3.0Mpa. The oil weight ratio was 5.5:1. The main properties of Iranian slag and deasphalted oil are shown in Table 9.
[0071] Table 9 Analysis of main prop...
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