Distillate yield improving vacuum distillation method and device
A distillation method and a technology for a vacuum distillation column, which are applied in the field of vacuum distillation methods and devices, can solve problems such as the limited function of a flash column, and achieve the effects of being conducive to capacity expansion, reducing pipe diameter, and high extraction rate.
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Embodiment 1
[0030] The method of the present invention is used in the design of a new crude oil atmospheric and vacuum device, and the process flow of the decompression part and the accompanying figure 1 Same as shown.
[0031] The processing capacity of the decompression device is 1.2 million tons per year, and the decompression process includes a decompression furnace, a flash tank, and a decompression tower. The decompression tower is a structured packing tower, which adopts wet process operation. The steam blowing volume at the bottom of the tower is 1% of the tower feed, the operating pressure at the top of the tower is 1.315kPa, and the pressure drop of the whole tower is 600Pa~750Pa.
[0032] The constant bottom oil 1 is fed into the vacuum distillation device at 150 tons / hour, heated to 390°C-400°C by the vacuum furnace 2, and then enters the vacuum flash tank 4 through the vacuum transfer line 3. The flash tank is directly connected with the vacuum tower, and the pressure of the...
Embodiment 2
[0038] The method of the present invention is used for the expansion and transformation of a certain crude oil atmospheric and vacuum device. The normal pressure part is the same as the conventional atmospheric and vacuum device, and the decompression part figure 1 The schematic diagram of the process flow of the vacuum distillation method for improving the extraction rate shown mainly includes a vacuum furnace, a flash tank, and a vacuum tower.
[0039] The decompression tower is a structured packing tower, the operating pressure at the top of the tower is 1.315kPa, and the pressure drop of the whole tower is 600Pa~750Pa.
[0040] The constant bottom oil 1 enters the vacuum distillation device, is heated to 390°C-400°C by the vacuum furnace 2, and then enters the vacuum flash tank 4 from the transition section 3 of the vacuum-to-oil line. The flash tank is directly connected with the vacuum tower, and the pressure of the flash tank is 13kPa. After the adiabatic flash, the fla...
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Abstract
Description
Claims
Application Information
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