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Preparation method of spherical low-temperature denitration catalyst, spherical low-temperature denitration catalyst prepared by method and application of catalyst

A low-temperature denitration and catalyst technology, which is applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of high cost, complex preparation process, poor denitration efficiency, etc., and achieves low cost and preparation process. The effect of a simple, low temperature window

Inactive Publication Date: 2019-05-14
CHINA BUILDING MATERIALS ACAD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The most mature catalyst used in industry is MoO 3 or WO 3 Auxiliary V 2 o 5 / TiO 2 Catalyst (with TiO 2 As a carrier, with V 2 o 5 As the main active ingredient, WO 3 or MoO 3 It is an auxiliary ingredient for anti-oxidation and anti-toxicity), but V 2 o 5 The catalyst has obvious biological poisoning effect, and the activity of the catalyst generally requires high temperature, which is suitable for treating flue gas denitrification at 300-400 °C, while the temperature of flue gas emitted by some coal-fired devices is generally in the low-to-medium range, but In the prior art, the denitrification efficiency of flue gas at medium and low temperatures, especially at temperatures lower than 200°C, is very poor, and there are problems such as complicated preparation process and high cost.

Method used

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  • Preparation method of spherical low-temperature denitration catalyst, spherical low-temperature denitration catalyst prepared by method and application of catalyst

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preparation example Construction

[0030] The present invention proposes a preparation method of a spherical low-temperature denitration catalyst, which comprises the following steps:

[0031] 1) adding the metal salt and the spherical carrier into water in turn, and stirring to obtain a mixed solution;

[0032] 2) adding an alkaline precipitant to the mixed solution to adjust the pH of the system to be alkaline;

[0033] 3) the above-mentioned system is placed in a reactor for hydrothermal reaction;

[0034] 4) washing the product of the above-mentioned hydrothermal reaction with clear water, and drying;

[0035] 5) Calcining the dried product above to obtain a spherical low-temperature denitration catalyst.

[0036] Preferably, the aforementioned method for preparing a spherical low-temperature denitration catalyst, wherein the metal salt includes a soluble manganese salt and auxiliary components; the auxiliary components are iron salts, copper salts, cobalt salts, nickel salts of transition metal salts At...

Embodiment 1

[0066] Calculate and measure 6.74g of manganese nitrate solution (50wt%), weigh 2.10g of cerium nitrate hexahydrate and dissolve it in 15mL of water, then add 20g of gamma-Al 2 o 3 Place in the above solution, stir magnetically at room temperature for 10 minutes; then add 3 g of urea, stir to dissolve it, place it in a reaction kettle at 120°C for hydrothermal reaction, and the reaction time is 12 hours; wash it with clean water, and dry it in an oven at 100°C ; Finally, calcining and activating at 500° C. for 3 hours in a muffle furnace to prepare a spherical low-temperature denitration catalyst.

Embodiment 2

[0068] Calculate and measure 6.74g of manganese nitrate solution (50wt%), weigh 1.26g of cerium nitrate hexahydrate and dissolve it in 15mL of water, then add 20g of gamma-Al 2 o 3 Place in the above solution, stir magnetically at room temperature for 10 minutes; then add 3 g of urea, stir to dissolve it, place it in a reaction kettle at 120°C for hydrothermal reaction, and the reaction time is 12 hours; wash it with clean water, and dry it in an oven at 100°C ; Finally, calcining and activating at 500° C. for 3 hours in a muffle furnace to prepare a spherical low-temperature denitration catalyst.

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Abstract

The invention aims at providing a preparation method of a spherical low-temperature denitration catalyst, a spherical low-temperature denitration catalyst prepared by the method, and an application ofthe spherical low-temperature denitration catalyst. The preparation method of the spherical low-temperature denitration catalyst comprises the following steps of: 1) sequentially adding metal salt and a spherical carrier into water, and performing stirring to form a mixed solution, 2) adding an alkaline precipitant into the mixed solution to regulate a pH (potential of hydrogen) of a system to bealkaline, 3) putting the system in a reaction kettle for a hydrothermal reaction, 4) washing a product of the hydrothermal reaction with clear water and drying the product, and 5) calcining the driedproduct to form the spherical low-temperature denitration catalyst. A denitration rate of the spherical low-temperature denitration catalyst prepared by the method reaches above 70% at 80-200 DEG C;an improvement effect of the denitration rate is obvious as compared with a catalyst prepared from the same formula as the catalyst by an impregnation method; and an improvement rate of the denitration rate at 80-120 DEG C is 20-30%.

Description

technical field [0001] The invention relates to the technical field of flue gas denitration, in particular to a preparation method of a spherical low-temperature denitration catalyst, a spherical low-temperature denitration catalyst prepared by the method and an application thereof. Background technique [0002] Nitrogen oxides can produce photochemical smog, acid rain, ozone hole and greenhouse effect, and are one of the main pollutants in the atmosphere. At present, flue gas denitrification is one of the effective methods to control the emission of nitrogen oxides in the process of coal combustion. Selective catalytic reduction (SCR) technology is widely used in flue gas denitrification due to its high denitrification efficiency, good selectivity, stable and reliable operation, etc. has been widely used in the process. [0003] The technical key of the selective catalytic reduction denitration catalyst lies in: an excellent catalyst carrier, an active catalyst formula and...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J35/08B01J37/03B01J37/08B01J37/10B01J23/34B01D53/56B01D53/86
Inventor 赵春林陈鑫吴彦霞陈琛梁海龙唐婕戴长友
Owner CHINA BUILDING MATERIALS ACAD