Wet desulphurization sulfur flotation device and method

A wet desulfurization and sulfur technology, applied in flotation, separation methods, chemical instruments and methods, etc., can solve the problems of difficult air volume, huge equipment investment, and high air utilization rate, so as to reduce equipment investment costs and avoid sedimentation and accumulation , the effect of high air utilization

Pending Publication Date: 2021-06-15
BEIJING RUNYU ENVIRONMENTAL PROTECTION ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in practical applications, it is found that the passive supply of this kind of air determines that it is difficult to self-adjust according to the actual demand; more importantly, the throat of the jet regenerator is easily blocked, resulting in the actual amount of regenerated air being much less than Design value, which seriously affects the overall efficiency of the device
[0008] It can be seen that for the separation and recovery of sulfur in wet desulfurization, whether to use sedimentation separation or flotation separation has its own advantages and disadvantages.
For the sedimentation separation process, if an air pulse loosening device is installed in the sulfur sedimentation tank to periodically make the settled and compacted sulfur fluffy and easy to flow, the equipment is difficult to manufacture and the control method is complicated
For the flotation process, the high-tower regeneration technology with relatively stable performance has a huge investment in equipment, and it is difficult to bear the expensive equipment investment for small and medium-scale desulfurization; the jet regeneration technology with high air utilization rate and relatively small equipment size exists. The air volume is difficult to adjust independently according to the actual demand, and there is a serious defect that the throat of the injection regenerator is easily blocked, resulting in the actual amount of regenerated air being far less than the design value

Method used

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  • Wet desulphurization sulfur flotation device and method
  • Wet desulphurization sulfur flotation device and method

Examples

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Embodiment 1

[0053] One of the application cases of the method of the present invention is desulfurization of coke oven gas. Coke oven gas volume is 40000Nm 3 / h, the hydrogen sulfide content in the gas is 5g / Nm 3 . Coke oven gas is desulfurized to 50mg / Nm by two-stage desulfurization towers 3 Then go to the downstream device for further processing. The amount of desulfurized lean liquid entering the absorption tower is 1000m 3 / h, desulfurization lean liquid absorbs and converts hydrogen sulfide in coke oven gas to form desulfurization rich liquid, such as figure 1 As shown, the desulfurized rich liquid is pumped from the rich liquid pipeline 2 to the hydraulically driven rotary agitator 3 of the regeneration tank 4 through the solution circulation pump 1 . The size of the regeneration tank 4 is 7.6 meters in diameter and 9.6 meters in height. The hydraulically driven rotary agitator 3 is located in the middle of the regeneration tank 4 near the bottom. After the desulfurization li...

Embodiment 2

[0055] Another application case is in the field of biogas desulfurization. The amount of sulfur-containing biogas is 2000Nm 3 / h, the hydrogen sulfide content in the biogas is 4g / Nm 3 . The biogas is desulfurized to 20mg / Nm by a single desulfurization tower 3 Then go to the downstream device for further processing. The amount of desulfurized lean liquid entering the absorption tower is 50m 3 / h, the desulfurization lean liquid absorbs and converts the hydrogen sulfide in the biogas to form a desulfurization rich liquid, such as figure 1 As shown, the desulfurization rich solution is pumped from the rich solution pipeline 2 to the hydraulically driven rotary agitator 3 of the regeneration tank 4 through the solution circulation pump solution circulation pump 1 . The size of the regeneration tank 4 is 4 meters in diameter and 3 meters in height. The hydraulically driven rotary agitator 3 is located in the middle of the regeneration tank 4 near the bottom. After the desulf...

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Abstract

The invention relates to a wet desulphurization sulfur flotation device and method, and belongs to the technical field of chemical engineering. The wet desulphurization sulfur flotation device comprises a regeneration tank, a Roots blower or an air compressor, an air aeration connecting pipeline and an air aeration membrane pipe; the Roots blower or the air compressor is communicated with the air aeration membrane pipe through an air aeration connecting pipeline; and the air aeration membrane pipe is positioned in the regeneration tank. Air bubbles formed by the tubular aeration membrane are small, the air utilization rate is high, the size of regeneration equipment is small, the height of the regeneration equipment is not more than 10 m and is less than or equal to 1/4 of that of high tower regeneration equipment, and the equipment investment cost is obviously reduced. A rotary stirrer is driven by hydraulic power, so that sulfur is always kept in a suspended state in the desulfurization liquid, sedimentation and accumulation of the sulfur are avoided, and flotation of the sulfur is facilitated. And no extra energy is supplemented in the stirring process.

Description

technical field [0001] The invention relates to a wet desulfurization sulfur flotation device and method, belonging to the technical field of chemical industry. Background technique [0002] Typical chelated iron (also known as complexed iron) wet desulfurization technology such as Chinese invention patent CN108130147A describes this desulfurization process: the sulfur-containing raw material gas (usually greater than 10KPa) with a certain pressure enters the desulfurization tower, and the top flow The desulfurized liquid is contacted in countercurrent to carry out the chemical absorption of liquid-phase catalytic oxidation. After the desulfurized liquid absorbs the hydrogen sulfide in the raw material, the hydrogen in the gas is purified. 2 S content less than 10PPM is sent out of the boundary through the pipeline after the mist is removed by the mist trapping section. Absorbed H 2 All the desulfurization solution of S is sent to the regeneration tank for air oxidation re...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B03D1/16B03D1/22B01D53/52B01D53/86B01D53/96
CPCB01D53/52B01D53/8612B01D53/96B03D1/16B03D1/22
Inventor 黄显波李洋潘启华阮小卫胡勇张晓惠周一民王莱
Owner BEIJING RUNYU ENVIRONMENTAL PROTECTION ENG
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