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Simultaneous desulfurization and denitration catalyst without reducing gas and preparation method thereof

A desulfurization, denitrification, and catalyst technology, which is applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem of poor resistance to sulfur poisoning and water vapor resistance, and difficulty in removing nitrogen oxides and sulfur oxides , the high cost of electron accelerators, etc., to achieve the effect of low cost, high mechanical strength and simple operation

Inactive Publication Date: 2019-04-02
CHANGCHUN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] While the current electron beam / ammonia method (EBA), which is gradually becoming industrialized, can reach more than 80% in desulfurization rate and denitrification rate, it needs to produce electron beam accelerators and high-power electron guns of high-energy electrons, and needs radiation protection facilities, electron accelerators Expensive, high energy consumption, heavy maintenance workload, high operating costs
Most of the currently developed catalysts require reducing gas, and it is difficult to remove nitrogen oxides and sulfur oxides at the same time. The activated carbon adsorption method requires frequent dry regeneration treatment. CuO / γ-Al 2 o 3 The anti-sulfur poisoning and anti-water vapor performance of the catalyst is not good, and it is easy to deactivate

Method used

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  • Simultaneous desulfurization and denitration catalyst without reducing gas and preparation method thereof
  • Simultaneous desulfurization and denitration catalyst without reducing gas and preparation method thereof
  • Simultaneous desulfurization and denitration catalyst without reducing gas and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Weigh 0.115g ammonium metavanadate and 0.23g oxalic acid into a 100mL clean beaker, add distilled water (about 20mL) to dissolve, then add 0.19g copper nitrate, add ammonia water dropwise to the cloudy solution until the solution is uniform. Then weigh 0.124g of nickel nitrate and 0.65g of potassium nitrate respectively, add them, the solution is still in a uniform state, measure its pH between 6-7, add distilled water to 60mL. Finally, 5 g of spherical ZSM-5 molecular sieve carriers were added and immersed in a water bath at 50° C. for 4 hours. Filter after impregnation, put the solid in a crucible, evaporate to dryness at 120°C for 12h, and then bake at 500°C for 6h. Weigh 0.124g of cobalt nitrate and place it in a 100mL beaker, add distilled water to dissolve it, and set the volume to 60mL, add the roasted solid semi-finished catalyst to it, and immerse at 50°C for 4h. Filter after impregnation, put the solid in a crucible, evaporate to dryness at 120°C for 12 hours...

Embodiment 2

[0031] As in Example 1, under the same conditions and preparation method, copper and vanadium were simultaneously impregnated at a concentration of 1% by weight in the impregnating solution at one time to obtain a Cu-V / ZSM-5 catalyst. This catalyzer is formed with the reaction device of embodiment one and feed gas, under the same reaction condition, records following table 2 result:

[0032] Table 2

[0033]

[0034]

Embodiment 3

[0036] As in Example 1, with the same preparation conditions and preparation method, copper, vanadium and tungsten were simultaneously impregnated at a concentration of 1% by weight of the impregnating solution at one time to prepare a Cu-V-W / ZSM-5 catalyst. The catalyst is composed of the same reaction device and raw material gas as in Example 1. Under the same reaction conditions, the reaction tail gas is absorbed by 5% lye or activated at 500°C under the original atmosphere, and then reacted at 350°C. The results are as follows Table 3 results:

[0037] table 3

[0038] Catalyst use time

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Abstract

The invention discloses a catalyst for simultaneous desulfurization and denitration without reducing gas and a preparation method thereof. The catalyst can directly decompose oxynitride into nitrogen gas and oxygen gas, which are discharged then, and oxidize sulfur oxides into sulfur trioxide, which can be easily removed, in the absence of reducing gas (ammonia gas). The catalyst is composed of the following components in percentage by weight: 0.5 to 2.5% of ZSM-5 molecular sieve, 0 to 1.5% of CuO, 0-1.5% of K2O, 0-1.5% of CoO, 0 to 1.5% of Ni2O3, 0.5 to 2.5% of V2O5, and 0-1.5% of WO3; wherein CuO, K2O, CoO, Ni2O3, V2O5, and WO3 are active components. The catalyst is impregnated for one time or more, and then dried and burned before using. The catalyst has the advantages of easily-available raw material, low cost, simple preparation, good activity and stability, high desulfurization rate and denitration rate, and no secondary pollution (reducing ammonia gas).

Description

technical field [0001] The invention relates to the field of chemical technology, especially the field of industrial catalysts, and particularly provides a catalyst and a preparation method for simultaneously removing sulfur dioxide and nitrogen oxides in coal-fired flue gas without reducing gas. Background technique [0002] With the development of the economy, my country's demand for coal is increasing day by day. The development and utilization of coal has caused serious damage to the ecological environment, and people are very concerned about the ecological environment and health and safety. my country is the world's largest coal-producing and coal-utilizing country, and the combustion and utilization of coal is the most important way. SO emissions from thermal power plants and coal-fired boilers 2 and NO X It is currently the main source of sulfur oxides and nitrogen oxides, and has also become a major factor restricting China's economic and social development. [000...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/48B01D53/60B01D53/86
Inventor 王承学刘鹏举王海博
Owner CHANGCHUN UNIV OF TECH