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Multistage cyclone gas liquid removal method and liquid removal apparatus

A cyclone and gas technology, applied in the field of gas-liquid separation, can solve problems such as the weakening of the cyclone effect, and achieve the effects of easy processing, improved liquid removal efficiency, and simple structure

Inactive Publication Date: 2015-10-07
QINGDAO JINGRUN PETROCHEM ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The purpose of separation can only be achieved when the separation time of the droplets is less than the residence time of the gas in the swirl field. Increasing the length of the cylinder can increase the residence time of the fluid in the swirl field and improve the efficiency of liquid removal, but as the axial distance increases As the velocity increases, the hoop velocity gradually decreases, the separation power of the droplet becomes smaller and smaller, and the swirl effect is weakened; secondly, because the liquid is still in contact with the gas, the flowing gas will break up the liquid gathered in the wall area at any time, making the liquid In addition, due to the fluidity of the liquid, after the liquid coalesces into a larger volume along the wall, the gravity will naturally break the surface tension, forming small particles and returning to the gas. Therefore, even if the swirling flow scheme is used in the existing technology, since the liquid cannot be drawn out at any time, the separated liquid will be broken again under the action of the air flow, and become small droplets, which are re-involved in the smoke

Method used

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  • Multistage cyclone gas liquid removal method and liquid removal apparatus
  • Multistage cyclone gas liquid removal method and liquid removal apparatus
  • Multistage cyclone gas liquid removal method and liquid removal apparatus

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Embodiment

[0044] It is used for dehydration of flue gas in wet flue gas desulfurization unit. The flue gas volume is 200,000 standard cubic meters per hour, and the water content of the flue gas is 97099kg / h. Six sets of multi-stage cyclone separators of the same size are installed. Each set of separators has three stages. L1=1440mm, D2=680mm, L2=1224mm, D3=560mm, L3=1008mm, d=2750mm, H=420mm, α=0°, S=60mm, each stage swirl sheet 11 is 4 pieces, the total dehydrator The pressure drop is 1085Pa, and the water content in the exhaust gas is almost zero.

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Abstract

The invention relates to a multistage cyclone gas liquid removal method and a liquid removal apparatus, and belongs to the technical field of gas-liquid separation. The method and the apparatus are especially used for dehydration and liquid removal of flue gas discharged from a wet flue gas desulphurization device, and the apparatus comprises a multistage cyclone, a connection cylinder and a gas discharge cylinder. The multistage cyclone is composed of multiple stages of up-and-down serially connected cyclones, every stage of the cyclones is composed of a cylinder body, a cyclone part and a liquid influx zone, the cyclone part is arranged in the center of the flue gas cylinder body of every stage of the cyclones, a liquid conglomerating from all the cyclones is timely leaded out in a centrifugal effective zone, and a gas enters a next stage of the cyclone, finally enters the gas discharge cylinder, and is discharged.

Description

technical field [0001] The invention belongs to the technical field of gas-liquid separation, and in particular relates to a multistage cyclone liquid removal method and a liquid remover. Background technique [0002] Flue gas desulfurization mostly adopts a wet process. The so-called wet process uses an absorbent prepared as a slurry to wash the flue gas and remove the SO in the flue gas. 2 It is absorbed into the slurry and reacts with the absorbent. The core device is the absorption tower. Since most of the reaction of the absorption tower adopts spray washing, the treated flue gas contains a large number of mist droplets. If the mist is allowed to When the droplets are taken out of the absorption tower, the mist droplets will be discharged from the chimney with the flue gas, and fall around the chimney to form "light rain", thereby polluting the environment. From the point of view of energy saving, a large amount of slurry is taken out, which is also a loss to the opera...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D45/14
Inventor 石宝珍房媛媛李亮
Owner QINGDAO JINGRUN PETROCHEM ENG
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