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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

Active Publication Date: 2015-06-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the oil transfer line must be more than 15m (to ensure that the gas-liquid phase has a certain stratification time, which is beneficial to improve product quality and the extraction rate of the vacuum tower), the large-diameter and long-distance oil transfer line occupies a large part of the investment in vacuum distillation equipment. At the same time, factors such as heat loss and pressure drop increase are not conducive to the operation of the vacuum distillation tower, and the resulting thermal stress and thermal displacement cause certain difficulties in design and installation in terms of safety.

Method used

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  • Crude oil reduced pressure distillation method and apparatus for reducing yield of residual oil
  • Crude oil reduced pressure distillation method and apparatus for reducing yield of residual oil
  • Crude oil reduced pressure distillation method and apparatus for reducing yield of residual oil

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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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Abstract

The invention discloses a crude oil reduced pressure distillation method for reducing yield of residual oil. Atmospheric tower bottom oil is introduced into a first stage flash tank for separation after being heated in a first stage gasifier; a liquid phase is introduced to a second stage gasifier and then to a second stage flash tank after being heated; the liquid phase is introduced to a third stage gasifier and then to a third stage flash tank after being heated; the liquid phase is introduced to a reduced pressure flash section; gas phases obtained in various stages are introduced to the upper, the middle and the lower fractional distillation sections of reduced pressure tower; lateral line products are pumped out from lateral lines of the reduced pressure tower; a part of residues at the bottom of the tower is introduced to the flash tanks in the various stages, wherein at least two rotary evaporation coils are arranged in a gas phase zone in the upper part of the reduced pressure flash tower; tank walls between the two rotary evaporation coils are provided with baffle plates for preventing wall flows; and the rotary evaporation coils are fixed on a rotary shaft at a longitudinal shaft center position of the tank body. The method provided by the invention can obviously reduce the yield of the reduced pressure residual oil, increase economic benefits of the apparatus, reduce energy consumption of the apparatus, and save investment for the apparatus.

Description

technical field [0001] The invention belongs to the field of petroleum refining, and relates to a crude oil vacuum distillation method and device for reducing the yield of residual oil, in particular to a device for increasing the extraction rate, reducing the yield of residual oil, and reducing the yield of residual oil in the vacuum distillation process of crude oil. Energy consumption, method and device for increasing economic benefit of crude oil vacuum distillation unit. technical background [0002] Atmospheric and vacuum distillation process of crude oil in refinery is the first process of petroleum refining. It divides crude oil into components with different distillation ranges by distillation to meet the process requirements of products and downstream devices for raw materials. The level of its light oil yield and the size of energy consumption directly affect the economic benefits of petroleum refining. The vacuum distillation process is to use the principle of v...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G7/06
Inventor 方向晨张龙齐慧敏王海波李经伟王岩姜阳
Owner CHINA PETROLEUM & CHEM CORP
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