Tower feeding distributor

The technology of feed distributor and flow divider is applied in the field of anti-gas mist entrainment feed distributor, single tangential or double tangential feed distributor, which can solve the problem of large rising gas swirl and rising gas in the distributor. Fog entrainment, inability to distribute materials evenly, etc., to avoid uneven gas distribution, achieve highly uniform distribution, and avoid easy coking

Active Publication Date: 2011-05-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, most of the feed distributors for vacuum towers that are widely used in the industry are straight pipe openings or through various settings for the diversion of the feed stream to complete the uniform distribution of the feed stream. Since the feed is opened at different positions The outflow rate of the hole is different, and such a distributor cannot meet the requirements of uniform distribution of materials; moreover, the feed of the vacuum tower is a gas-liquid mixed mist flow containing 60% to 70% liquid phase, and the gas after the feed is distributed The entrainment of mist is relatively serious, which has a great impact on the product quality of the side line at the bottom of the tower
[0005] Although the existing double tangential feed distributor can meet the purpose of uniform distribution, there are disadvantages such as large gas swirl flow and many vortices in the ascending gas of the distributor, serious entrainment of rising gas mist, and large pressure drop of gas flowing through it; foreign countries Although the double-row vane-type feed distributor has a small process pressure drop, which is beneficial to the deep-drawing operation of vacuum distillation, there are problems such as uneven air distribution and serious droplet entrainment, which seriously affect the production of distillate oil in vacuum distillation. Product quality, thus restricting the vacuum distillation deep drawing treatment, the vacuum distillation extraction rate cannot be improved

Method used

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Experimental program
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Embodiment 1

[0021] A novel feed distributor of the present invention is specifically a blade-type double tangential feed distributor, the basic structure of which includes a feed inlet 6, a deflector 1, a louver flow channel 2, blades 3, and a flow divider 5. like figure 1 As shown, the splitter 5 and the tower wall form a fan-shaped structure closed up and down, which is located between the feed port 6 and the louver flow channel 2, and communicates with the feed port 6 and the louver flow channel 2. The end of the flow plate 1 is fixed on the end plate 8 of the flow divider, and the upper and lower elevations are welded to the upper and lower cover plates of the flow divider to form several watersheds that are not connected to each other, such as figure 2 As shown; the louver flow channel 2 is a rectangular or circular channel whose flow area gradually decreases along the feeding direction, and the front end is fixed on the support end plate 8 of the splitter; the front end of the lou...

Embodiment 2

[0025] A novel feed distributor of the present invention is specifically a blade-type single tangential feed distributor, and its basic structure includes a feed inlet 6, a deflector 1, a louver flow channel 2, blades 3, and a flow divider 5, like Figure 4 shown. The structure of the flow divider 5 and the deflector 1 is the same as that of the embodiment 1. One end of the opening of the louver flow channel 2 faces the flow divider 5 , the top and bottom are closed, and the end is a closed structure, which is fixed on the support beam 4 . On both sides of the louver flow channel 2, multiple groups of blades 3 of different sizes are arranged in sequence from the inlet end, and the directions of the blades on both sides are staggered; Figure 5 shown. The specific positions, quantities and heights of the deflectors 1 and vanes 3 are determined by CFD simulation calculations according to the amount of feed gas-liquid, feed gas-liquid ratio, etc.

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Abstract

The invention relates to a tower feeding distributor, comprising a feeding inlet, a splitter and a shutter flow channel. The splitter is of a fan-shaped structure, comprising an arch-shaped guide plate, upper and lower cover plates and a support end plate. The shutter flow channel is a horizontal channel with a gradually decreasing flow area, and an inlet end of the shutter flow channel is fixed on a support end plate of the splitter. At both sides of the shutter flow channel, 4-12 groups of blades are arranged in order from the inlet end, and directions of the blades on the two sides are staggered to form an outlet between the adjacent blades. The feeding distributor can carry out both uniform distribution on the gas-liquid mixing feed for two times and gas-liquid separation on the gas-liquid mixing feed for two times, and generate airflow collision by utilizing an inertial force of the gas phase, thereby basically eliminating the entrainment of liquid drop by gas. Non-uniform gas distribution caused by a sudden change in feeding amount is avoided. High uniform rising gas distribution is realized. Meanwhile, a tower diameter width is fully used to ensure the feeding distributor to be low and to effectively save the space.

Description

technical field [0001] The invention relates to a gas-liquid two-phase feeding device for a tower, in particular to a vane-type single-tangential or double-tangential feed distributor. More specifically, it belongs to a feed distributor for preventing gas and mist entrainment, which is especially suitable for the deep drawing treatment of the vacuum tower of the atmospheric and vacuum distillation device of the petroleum refinery. technical background [0002] The tower is one of the most important equipment in the petroleum refinery, in order to realize the full contact between the gas-liquid or liquid-liquid two phases, and achieve the purpose of interphase heat transfer and mass transfer. [0003] The vacuum tower of the atmospheric and vacuum distillation unit in the petroleum refinery is a vacuum distillation method to obtain more light fraction oil from the atmospheric residue and ensure the <500°C fraction content ≯5% in the vacuum residue Gas-liquid, liquid-liqui...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D3/14B01D3/32
Inventor 张龙王海波齐慧敏刘忠信李欣姜阳
Owner CHINA PETROLEUM & CHEM CORP
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