Crude oil reduced pressure distillation method and apparatus for reducing yield of residual oil
A distillation method and vacuum distillation tower technology, applied in the field of petroleum refining, can solve the problems of thermal stress safety design and installation difficulty, unfavorable vacuum distillation tower operation, etc., so as to improve the gas-liquid separation effect, reduce the yield, Reduce the effect of irreversibility
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Embodiment 1
[0058] The method of the present invention is used in the design of a newly-built 10 million tons / year crude oil atmospheric and vacuum distillation unit, and the process flow of the decompression part and the accompanying figure 1 Same as shown.
[0059] The processing capacity of the decompression device is 5 million tons per year. The decompression process includes a primary gasifier, a primary decompression flash tank, a secondary gasifier, a secondary decompression flash tank, and a tertiary gasifier , Three-stage vacuum flash tank, vacuum distillation tower. The vacuum distillation 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 feed to the tower, the operating pressure at the top of the tower is 1.315 kPa, and the pressure drop of the whole tower is 685 Pa.
[0060] The decompression flash tanks at all levels adopt the decompression flash tank with the above structure of the prese...
Embodiment 2
[0074]The method of the present invention is used for the capacity expansion transformation of a crude oil atmospheric and vacuum device. The normal pressure part is the same as the conventional atmospheric and vacuum device, and the decompression part mainly includes a first-stage gasifier, a first-stage decompression flash tank, and a second-stage gasification Furnace, secondary vacuum flash tank, tertiary gasifier, tertiary flash tank, vacuum distillation tower.
[0075] The decompression tower is a structured packing tower, the operating pressure at the top of the tower is 1.315 kPa, and the pressure drop across the tower is 685 Pa.
[0076] The decompression flash tanks at all levels adopt the decompression flash tank with the above structure of the present invention, which is a decompression flash tank with two rotary evaporators. The rotary evaporator is a disc structure, and the upper rotary evaporator The diameter d1 is 40% of the inner diameter D of the vacuum flash ...
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