Flue gas absorbent which simultaneously has functions of desulphurization and denitration and preparation method and application thereof

A desulfurization, denitrification and absorbent technology, applied in the field of flue gas purification and treatment, can solve the problems of cumbersome preparation process of highly active absorbent, cumbersome preparation process of absorbent, huge investment and operating costs, etc. Small, low investment and operating costs

Inactive Publication Date: 2012-02-15
NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The current main problems of dry process technology are relatively low removal efficiency, cumbersome preparation process of absorbent and low utilization rate, etc.
Chinese patent 200310103954.7 discloses a flue gas desulfurization and denitrification purification method and device, which sprays a solid high-activity absorbent based on fly ash, lime and additives into a circulating fluidized bed reactor, Absorb sulfur dioxide SO in flue gas 2 NO x ; Use the return leg on the dust removal device to send the incompletely reacted highly active absorbent back to the feeding pipe for recycling, but the preparation process of the highly active absorbent in this method is cumbersome
Moreover, changing the flue gas flow mode from a single upward to an upward and then downward flow mode reduces the space height of the flue gas purification equipment, but this method is cumbersome and occupies a large area. It can be expected that this method will be used in practical engineering The investment and operating costs will be huge
[0005] In addition, in order to achieve simultaneous desulfurization and denitrification at low cost, some desulfurization and denitrification agents used to be prepared with chlorine-containing strong oxidants as additives, such as Chinese patent 200610051721.0 and Chinese patent 200610012525.2. Although the removal efficiency is high, it is easy to cause equipment corrosion. and secondary pollution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Embodiment 1: The desulfurization and denitrification absorbent of the present embodiment is calculated according to the consumption of 1L deionized water, which is made of 1.66g of sodium ferrate Na with a purity greater than 98%. 2 FeO 4 , 300g of borax Na 2 B 4 o 7 10H 2 O, 2.7g of sodium sulfite Na 2 SO 3 and 1 L of deionized water. Add the stated amount of borax Na to 1 L of deionized water 2 B 4 o 7 10H 2 O, obtain buffer solution after dissolving and mixing; Add the sodium sulfite Na of described amount in buffer solution 2 SO 3 , after dissolving and mixing, add the sodium ferrate Na with the purity greater than 98% 2 FeO 4 , fully dissolved and mixed to obtain the absorbent. The simultaneous desulfurization and denitrification absorbent described above is used in the semi-dry flue gas desulfurization device, which requires the ambient humidity in the desulfurization device to be 3-10%, the pH value to be 7-11, and the inlet flue gas temperature to...

Embodiment 2

[0024] Embodiment 2: The desulfurization and denitrification absorbent of this embodiment is calculated according to the consumption of 1L deionized water, which is made of potassium ferrate K with a purity of 594g greater than 98%. 2 FeO 4 , 3.8g of potassium dihydrogen phosphate KH 2 PO 4 , 2.7g of sodium silicate Na 2 SiO 3 and 1 L of deionized water. Add the stated amount of potassium dihydrogen phosphate KH to 1 L of deionized water 2 PO 4 , to obtain a buffer solution after dissolving and mixing; add the amount of sodium silicate Na in the buffer solution 2 SiO 3 After dissolving and mixing, add the potassium ferrate K with the purity greater than 98% 2 FeO 4 Fully dissolve and mix to obtain the absorbent. The simultaneous desulfurization and denitrification absorbent described above is used in the semi-dry flue gas desulfurization device, which requires the ambient humidity in the desulfurization device to be 3-10%, the pH value to be 7-11, and the inlet flue ...

Embodiment 3

[0025] Embodiment 3: The desulfurization and denitrification absorbent of the present embodiment is calculated according to the consumption of 1L deionized water, which is made of 332g of sodium ferrate Na with a purity greater than 98%. 2 FeO 4 , 1144g of potassium dihydrogen phosphate KH 2 PO 4 , 222g of sodium persulfate Na 2 S 2 o 8 and 1 L of deionized water. Add the stated amount of potassium dihydrogen phosphate KH to 1 L of deionized water 2 PO 4 , to obtain a buffer solution after dissolving and mixing; add the amount of sodium persulfate Na in the buffer solution 2 S 2 o 8 After dissolving and mixing, add the sodium ferrate Na with the purity greater than 98% 2 FeO 4 Fully dissolve and mix to obtain the absorbent. The simultaneous desulfurization and denitrification absorbent described above is used in the semi-dry flue gas desulfurization device, which requires the ambient humidity in the desulfurization device to be 3-10%, the pH value to be 7-11, and t...

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PUM

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Abstract

The invention discloses a flue gas absorbent which simultaneously has functions of desulphurization and denitration and a preparation method and an application thereof. Calculated according to 1L of deionized water, the flue gas absorbent provided by the invention is composed of 1.66-594g of an oxidizing agent, 3.8-1144g of a buffering agent, 2.7-222g of a stabilizing agent and 1L of deionized water. The preparation method provided by the invention comprises the following steps of: adding the buffering agent into 1L of deionized water, dissolving and uniformly mixing, adding the stabilizing agent, dissolving and uniformly mixing, adding the oxidizing agent, fully dissolving and uniformly mixing to obtain the absorbent. The absorbent provided by the invention and a calcium-based absorbent are simultaneously used so as to realize desulphurization and denitration in a same device, have high removal efficiency, and have less corrosion to the device with no discharge of desulphurization wastewater. In addition, desulphurization byproducts are dry, which is in favor of comprehensive utilization, disposal and stacking.

Description

technical field [0001] The invention belongs to the field of flue gas purification treatment, and relates to an absorbent for flue gas purification treatment and application thereof, in particular to an absorbent for simultaneous desulfurization and denitrification of flue gas, a preparation method and application thereof. Background technique [0002] At present, fossil fuels such as coal, oil, and natural gas are still the main energy sources for human beings. It is well known that the SO emitted from its combustion process 2 and NO x It can form acid rain and other secondary pollutants, which have seriously affected human production and life, and caused huge economic losses. Relevant data show that the annual economic loss caused by acid rain in China is about 110 billion yuan. Therefore, the control and purification of harmful gas pollution such as sulfur dioxide and nitrogen oxides are very important, which is related to the development of the national economy, especi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/82B01D53/60
Inventor 赵毅韩颖慧
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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