Double-oxidation ammonia desulfurization process and device

A double ammonia oxidation method and a desulfurization technology technology, which is applied in the field of double ammonia oxidation method desulfurization technology and devices, can solve the problems of being unsuitable for a large amount of flue gas, a large amount of ammonia escaping from an outlet flue gas, and a reduction in absorption efficiency, so as to improve the equipment. The effect of utilization rate, increasing economic benefits and reducing desulfurization cost

Inactive Publication Date: 2011-11-02
潍坊恒安散热器集团有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005]At present, the desulfurization tower in most ammonia desulfurization processes mainly adopts the absorption liquid spray absorption method, which will mainly cause the outlet flue gas A large amount of ammonia escape will cause secondary pollution to the surrounding environment
There are also some desulfurization towers that use trays to absorb sulfides, but because the temperature of the flue gas is difficult to drop to the optimum temperature of 60°C for desulfurization when passing through the trays, the absorption liquid on the trays absorbs the sulfides in the flue gas Finally, under high temperature conditions, it will be decomposed soon. Only by adding excessive ammonia to absorb the sulfide in the flue gas, this will cause a large amount of absorbent, which is uneconomical, and the amount of ammonia slip at the outlet is also large, and the outlet is decomposed. The sulfide and ammonia escape will continue to react, the by-products will be attached to the outlet flue, the amount of by-products that can be collected is small, and the outlet flue is easy to block
There is also a form of spraying under the tray of the desulfurization tower, but this absorption method basically relies on tray absorption. In order to ensure the desulfurization rate, it is necessary to ensure the reaction time of the flue gas passing through the tray and the absorption liquid on the tray. Therefore The hole spacing of the tray design is small, the resistance is large, and the energy consumption is high. When the flue gas passes through the liquid film of the tray, the droplet entrainment is serious
[0006] Yet by oxidation in the absorption tower, it is difficult to ensure that the ammonium sulfate oxidation time is greater than 2 hours and the optimum pH value is 5.5, thus it is difficult to produce ammonium sulfate; The first is oxidation in the concentration section. However, because the ammonium sulfite is unstable, it begins to decompose at a temperature above 60°C. If the concentration section is oxidized, the high-temperature flue gas above 130°C will decompose a large amount of ammonium sulfite, which also reduces the absorption efficiency and is difficult. ammonium sulfate
[0007] Chinese patent 200310115523.2 provides an integrated desulfurization and dedusting tower with ammonia method. The desulfurization and dedusting tower is equipped with a first-stage spraying section and a tray layer from bottom to top And the demister, the disadvantage of this device is that it is not suitable for handling large amounts of flue gas, and when the tower diameter of the desulfurization tower is large, the solution on the tray is difficult to distribute evenly
However, due to the use of oxidation treatment in the tower, this process and device will affect the desulfurization rate of the entire desulfurization system. If in order to ensure the desulfurization rate, excessive ammonia gas is added for absorption, and the ammonia escape in the outlet flue gas will inevitably exceed the standard.

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  • Double-oxidation ammonia desulfurization process and device
  • Double-oxidation ammonia desulfurization process and device

Examples

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Embodiment 1

[0050] A hydrogen peroxide desulfurization process, comprising the following steps:

[0051] (1) Preparation of desulfurizing agent ammonia water, ammonia water is prepared from liquid ammonia through an ammonia water preparation device, the mass fraction of the prepared ammonia water is 20%, stored in the ammonia water storage tank, and pumped into the bottom circulation pipeline of the absorption tower by a circulation pump when in use;

[0052] The ammonia water preparation process is as follows: liquid ammonia enters two liquid ammonia gasification heat exchange devices respectively, and the ammonia water gasifies into an endothermic reaction, which can cool down the circulating water that is fed in, and at the same time cool down the ammonia water to be discharged, and the gasified The ammonia water gas mixture enters the spray ammonia water absorption device, mixes the circulating water and the preparation water to prepare ammonia water with a mass concentration of 20%, a...

Embodiment 2

[0064] Such as figure 1 and figure 2 Shown, a kind of hydrogen peroxidation method desulfurization device comprises ammonia water preparation device 10, absorption tower 4, pre-washing tower 5, buffer oxidation box 6, cyclone 7, centrifuge 8, drying bed 9, tail gas scrubber 11, Packaging machine 12, ammonia storage tank 101; described absorption tower 4 is provided with demister 1, rotary plate convection ammonia absorption device 2, spray layer 3 and 1 / 2 perforated plate 41 sequentially from top to bottom, described The bottom of the absorption tower 4 is a slurry pool 42; the ammonia water preparation device 10 is connected with the ammonia water storage tank 101, and the ammonia water storage tank 101 is connected with the buffer oxidation tank 6, and the described pre-washing tower 5 is connected with the bottom of the absorption tower 4 , the top of the absorption tower 4 is connected with the chimney; the pre-wash tower 5 is connected with the buffer oxidation tank 6, ...

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Abstract

The invention discloses a double-oxidation ammonia desulfurization process and a double-oxidation ammonia desulfurization device. The device comprises an ammonia water preparation device, an absorption tower, a pre-scrubber, a buffer oxidation tank, a cyclone, a centrifugal machine, a drying bed, a tail gas scrubber, a packaging machine and an ammonia water storage tank. Sulfur dioxide is removedfrom flue gas by liquid ammonia, and ammonium sulfate crystals with the purity of over 99 percent are obtained; and the invention has the advantages that: the cost of the conventional ammonia desulfurization is reduced, the absorption efficiency is improved, the desulfurization efficiency is over 95 percent, the yield is improved, the ammonium sulfate crystals with the purity of over 99 percent are obtained, the waste is changed into treasure, economic benefit is increased, the ammonium sulfate yield is over 96 percent, and the ammonia escape volume is reduced and is less than 8mg/m<3>.

Description

technical field [0001] The invention relates to a flue gas desulfurization process, in particular to a double ammonia oxidation desulfurization process and device, which uses liquid ammonia to remove sulfur dioxide in flue gas, and belongs to the field of chemical industry. Background technique [0002] With the development of economy, the progress of society and the enhancement of people's awareness of environmental protection, the removal of SO2 from industrial flue gas has been paid more and more attention. [0003] Ammonia desulfurization process is based on ammonia and SO 2 , The basic mechanism of water reaction to generate desulfurization products, mainly wet ammonia method, electron beam ammonia method, pulse corona ammonia method, simple ammonia method and so on. [0004] The wet ammonia desulfurization process system is mainly composed of desulfurization washing system, flue gas system, ammonia storage system, ammonium sulfate production system (if it is not the a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/50C01C1/24
Inventor 李绍志曹国强
Owner 潍坊恒安散热器集团有限公司
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