Intermediate product hot tank feeding method and system thereof
A technology of feeding system and feeding method, which is applied in the direction of separation method, chemical instrument and method, and treatment of hydrocarbon oil, etc. It can solve problems such as difficult operation and adjustment, no mention of hot tank feeding method, lack of thermal flexibility in the process, etc. , achieve the effect of saving circulating water, inhibiting the formation of colloid, good safety and reliability
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Embodiment 2
[0064] The difference from Example 1 is that the intermediate product of the upstream device in this example is the vacuum gas oil produced by the atmospheric and vacuum device, the catalytic heavy cycle oil produced by the catalytic device, and the coker gas oil produced by the coking device, and the distillation range is 350-500°C. The downstream unit is a wax oil hydrotreating and upgrading unit with an operating pressure of 13.8MPa (table), which removes sulfur and nitrogen impurities, and deeply saturates the polycyclic aromatic hydrocarbons in the wax oil components to generate single-ring aromatic hydrocarbons, which are used as high-quality Catalytic raw material.
[0065] The method of using the device of this embodiment to carry out the hot tank feeding of the wax oil component can be divided into a hot tank feeding and discharging process and a volatile gas recovery process, wherein,
[0066] The described hot tank feeding and discharging process comprises the step...
Embodiment 3
[0077] The difference from Example 2 is that the upstream unit in this example is an atmospheric unit, a catalytic unit and a coking unit, which produce atmospheric diesel, catalytic diesel and coked diesel respectively, with a distillation range of 180-365°C, and the downstream units are Diesel hydrotreating unit, hydrogenation pressure 10.0MPa (table), removal of sulfur, nitrogen impurities and deep saturation of aromatics, production of national V vehicle diesel.
[0078] The method of using the device of this embodiment to carry out the hot tank feeding of diesel components can be divided into a hot tank feeding and discharging process and a volatile gas recovery process, wherein,
[0079] The described hot tank feeding and discharging process comprises the steps:
[0080] (1) The diesel component of the intermediate product from the upstream device enters the static mixer at a temperature of 155°C without air cooling or water cooling, and makes the temperature and propert...
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Abstract
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