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Basic aluminum sulfate regeneration desulfurization process based on retarded oxidation and multi-field synergistic desorption

A technology for inhibiting oxidation and aluminum sulfate, applied in chemical instruments and methods, separation methods, gas treatment, etc., can solve the problem of increasing the supplementary cost of basic aluminum sulfate, increasing the supplementary cost of basic aluminum sulfate, and reducing the cyclic desulfurization-desorption performance. and other problems, to achieve the effect of realizing the economical supply of aluminum sulfate, promoting the physical gas-liquid mass transfer ability, and enhancing the chemical dissociation ability.

Active Publication Date: 2020-03-31
INNER MONGOLIA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, there are certain defects in the basic aluminum sulfate regeneration method of the prior art, which are shown in the following points: traditional thermal desorption of SO 2 The desorption rate is low and the desorption time is long, which leads to the rapid attenuation of cycle desulfurization-desorption performance and increases the supplementary cost of basic aluminum sulfate; the simultaneous presence of SO 2 3- Oxidation problem, which weakens the desorption regeneration performance and indirectly increases the supplementary cost of basic aluminum sulfate. These problems are the technical bottlenecks that restrict the sustainable development and economic operation of this method
[0004] In summary, the traditional basic aluminum sulfate regeneration method is due to the presence of SO in the desulfurization-desorption cycle 3 2- Oxidation leads to a decrease in desorption potential, and at the same time, traditional thermal desorption or auxiliary steam stripping cannot achieve the ideal desorption performance, resulting in the limitation of desulfurizer regeneration. The combined results lead to an increase in desulfurizer supplementary costs, which is not conducive to industrial application and promotion.

Method used

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  • Basic aluminum sulfate regeneration desulfurization process based on retarded oxidation and multi-field synergistic desorption
  • Basic aluminum sulfate regeneration desulfurization process based on retarded oxidation and multi-field synergistic desorption
  • Basic aluminum sulfate regeneration desulfurization process based on retarded oxidation and multi-field synergistic desorption

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Effect test

Embodiment 1

[0044] Based on the basic aluminum sulfate regenerative desulfurization method based on oxidation inhibition and multi-field synergistic desorption, dust-containing raw flue gas is desulfurized through a device including an aluminum loss economic supply module 15, a desulfurization inhibition oxidation module 16, and a multi-field synergistic enhanced desorption module 17;

[0045] The aluminum loss economic replenishment module 15 includes a dust collector 1 and a fly ash soaking pool 5, and the desulfurization suppression oxidation module 16 includes a desulfurization device 6, a basic aluminum sulfate preparation pool 7 and a desulfurization mixed liquid circulation pool 8, and the multi-field synergy The enhanced desorption module 17 includes a desorption device 10;

[0046] The desulfurization process of the dust-containing raw flue gas is as follows: after the dust-containing raw flue gas enters the dust collector 1 for filtering dust, the dust-removed raw flue gas and fl...

Embodiment 2

[0051] Based on the basic aluminum sulfate regenerative desulfurization method based on oxidation inhibition and multi-field synergistic desorption, dust-containing raw flue gas is desulfurized through a device including an aluminum loss economic supply module 15, a desulfurization inhibition oxidation module 16, and a multi-field synergistic enhanced desorption module 17;

[0052] The aluminum loss economic replenishment module 15 includes a dust collector 1 and a fly ash soaking pool 5, and the desulfurization suppression oxidation module 16 includes a desulfurization device 6, a basic aluminum sulfate preparation pool 7 and a desulfurization mixed liquid circulation pool 8, and the multi-field synergy The enhanced desorption module 17 includes a desorption device 10;

[0053] The desulfurization process of the dust-containing raw flue gas is as follows: after the dust-containing raw flue gas enters the dust collector 1 for filtering dust, the dust-removed raw flue gas and fl...

Embodiment 3

[0058] Based on the basic aluminum sulfate regenerative desulfurization method based on oxidation inhibition and multi-field synergistic desorption, dust-containing raw flue gas is desulfurized through a device including an aluminum loss economic supply module 15, a desulfurization inhibition oxidation module 16, and a multi-field synergistic enhanced desorption module 17;

[0059] The aluminum loss economic replenishment module 15 includes a dust collector 1 and a fly ash soaking pool 5, and the desulfurization suppression oxidation module 16 includes a desulfurization device 6, a basic aluminum sulfate preparation pool 7 and a desulfurization mixed liquid circulation pool 8, and the multi-field synergy The enhanced desorption module 17 includes a desorption device 10;

[0060] The desulfurization process of the dust-containing raw flue gas is as follows: after the dust-containing raw flue gas enters the dust collector 1 for filtering dust, the dust-removed raw flue gas and fl...

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Abstract

The invention relates to the technical field of energy and power and chemical industry production, and particularly discloses a basic aluminum sulfate regeneration desulfurization process based on retarded oxidation and multi-field synergistic desorption. The process includes: performing desulfurization treatment on dust-bearing raw flue gas through combination of SO3<2-> retarded oxidation and multi-field synergistic desorption, thereby obtaining fly ash and dust-removed raw flue gas; immersing the fly ash in desulfurization rich liquor to prepare aluminum sulfate, and mixing the aluminum sulfate with water, CaCO3 or CaO to obtain basic aluminum sulfate; mixing the basic aluminum sulfate, a oxygen blocking agent, desulfurization rich liquor and desorption lean liquor to obtain a desulfurization mixed liquid; and performance a reaction on the dust-removed raw flue gas and the desulfurization mixed liquid to obtain desulfurization rich liquor and clean flue gas. In the invention, by combination of the characteristics of the desulfurization agent and aiming at the common defects of regeneration desulfurization process, the basic aluminum sulfate having excellent comprehensive performance is selected, so that the desorption effect of the basic aluminum sulfate regeneration desulfurization process is enhanced and the cost of the basic aluminum sulfate desulfurization agent, and meanwhile the technical purpose of economic operation is achieved.

Description

technical field [0001] The invention relates to the technical fields of energy, power and chemical production, and specifically relates to a basic aluminum sulfate regenerative desulfurization method based on oxidation inhibition and multi-field synergistic desorption. Background technique [0002] SO at home and abroad 2 Recyclable wet regenerative flue gas desulfurization technologies mainly include sodium sulfite circulation method, sodium citrate method, organic amine method and basic aluminum sulfate regeneration method, among which the traditional thermal desorption basic aluminum sulfate regenerative desulfurization method uses industrial aluminum sulfate [Al 2 (SO 4 ) 3 】with CaCO 3 Or CaO reacts in aqueous solution to prepare basic aluminum sulfate [(1-x)Al 2 (SO4) 3 ·xAl 2 o 3 】Desulfurization solution for SO 2 Absorption, desulfurization rich liquid thermal desorption to obtain high-purity SO 2 At the same time, basic aluminum sulfate can be regenerated a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/50B01D53/96
CPCB01D53/50B01D53/502B01D53/504B01D53/78B01D53/96B01D2258/0283
Inventor 张子敬韩锋崔鹏张维蔚云峰曹泽李斌豪王哲王世昌冯宇王俊娜
Owner INNER MONGOLIA UNIV OF TECH
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