Sectional feeding vacuum distillation method and apparatus for crude oil
A technology of segmented feeding and distillation method, which is applied in the field of petroleum refining, can solve the problems of low vacuum degree of flash tower and limited flashing effect of flash tower, so as to improve product quality and avoid gas phase mist Entrainment, reduce the effect of investment
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Embodiment 1
[0026] 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.
[0027] The processing capacity of the decompression device is 550 tons / hour, and the decompression process includes a decompression furnace, a flash tower, and a decompression tower. The decompression tower is a structured packing tower, which is operated by a wet process. The steam blowing volume at the bottom of the tower is 1% of the mass of the tower feed, the operating pressure at the top of the tower is 1.315 kPa, and the pressure drop of the whole tower is 600 Pa to 750 Pa.
[0028]The normal bottom oil 1 is fed into the vacuum distillation device at 550 tons / hour, heated to 390°C-420°C by the vacuum furnace 2, and then enters the vacuum flash tower 4. The top flash gas of the flash tower directly enters the middle and upper part of the vacuum tower, and the flash...
Embodiment 2
[0030] 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 flow diagram of the vacuum distillation method and equipment for crude oil with staged feeding shown mainly includes a vacuum furnace, a flash tower, and a vacuum tower. The vacuum tower is a structured packing tower, the operating pressure at the top of the tower is 1.315 kPa, and the pressure drop of the whole tower is 600 Pa to 750 Pa.
[0031] The normal bottom oil 1 enters the vacuum distillation device, is heated to 390° C. to 420° C. by the vacuum furnace 2, and then enters the vacuum flash tower 4 . The top flash gas of the flash tower directly enters the middle and upper part of the vacuum tower, and the flash oil at the bottom of the flash tower enters the flash distillation section 3 of the ...
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