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Flue gas denitration catalyst applied at a low temperature and preparation method thereof

A technology of denitrification catalyst and low temperature conditions, which is applied in the direction of chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of large operation fluctuations, large flue gas temperature fluctuations, and high concentrations, and achieve anti-sulfur and anti-water Strong poisoning ability, good low-temperature denitrification activity, and reasonable process effect

Inactive Publication Date: 2015-12-16
SHANDONG GEMSKY ENVIRONMENTAL PROTECTION TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with coal-fired power stations, the temperature of flue gas emitted by glass, coking, cement, industrial kilns, waste incineration and chemical plants is lower (often the flue gas emitted by waste heat boilers), and the temperature range is concentrated at 150~ Between 300°C (Note: The activity of the denitrification catalyst decreases with the decrease of temperature), SO 2 and H 2 The concentration of O is high, and the operation fluctuates greatly (the fluctuating operation will lead to large fluctuations in the temperature of the flue gas). It is difficult for the widely used denitrification catalysts to adapt to this kind of working conditions. , a catalyst with strong resistance to sulfur and water poisoning is necessary

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] A flue gas denitrification catalyst for low temperature conditions, with TiO 2 Composite SiO 2 and ZrO 2 as carrier, TiO 2 , SiO 2 , ZrO 2 The weight ratio is 95:1:2, the glass fiber is used as the skeleton, and the vanadium compound manganese is used as the active component, and the vanadium accounts for 10% by weight of the active component.

[0047] The preparation method is:

[0048] (1) Mixing

[0049] Step 1: Add 350 parts by weight of the carrier into a strong mixer, then add 2 parts by weight of stearic acid, 5 parts by weight of lactic acid, 220 parts by weight of water, 50 parts by weight of 20% ammonia water, and the mixing time is 15 Minutes, the temperature of the mud is greater than 70°C;

[0050] Step 2: adding 110 parts by weight of the carrier and 15 parts by weight of water into a strong mixer for mixing, and the mixing time is 20 minutes;

[0051] Step 3: Add 110 parts by weight of the carrier and 5 parts by weight of 25% ammonia water into a po...

Embodiment 2

[0069] A flue gas denitrification catalyst for low temperature conditions, with TiO 2 Composite SiO 2 as carrier, TiO 2 with SiO 2 The weight ratio is 99.5:2, with glass fiber as the skeleton, vanadium composite tungsten, molybdenum and cerium as the active component, vanadium accounts for 5% by weight of the active component.

[0070] The preparation method is:

[0071] Step 1: Add 340 parts by weight of the carrier into a strong mixer, then add 1 part by weight of stearic acid, 7 parts by weight of lactic acid, 190 parts by weight of water, 40 parts by weight of 25% ammonia water, and the mixing time is 10 Minutes, the temperature of the mud is greater than 70°C;

[0072] Step 2: adding 120 parts by weight of the carrier and 20 parts by weight of water into a strong mixer for mixing, and the mixing time is 30 minutes;

[0073] Step 3: Add 120 parts by weight of the carrier and 15 parts by weight of 15% ammonia water into a powerful mixer for mixing. When the temperature...

Embodiment 3

[0091] A flue gas denitrification catalyst for low temperature conditions, with TiO 2 Composite ZrO 2 as carrier, TiO 2 with ZrO 2 The weight ratio is 95:5, the glass fiber is used as the skeleton, and the vanadium-complexed niobium is used as the active component, and the vanadium accounts for 20% by weight of the active component.

[0092] The preparation method is:

[0093] Step 1: Add 360 parts by weight of the carrier into a strong mixer, then add 3 parts by weight of stearic acid, 8 parts by weight of lactic acid, 250 parts by weight of water, 60 parts by weight of 15% ammonia water, and the mixing time is 20 Minutes, the temperature of the mud is greater than 70°C;

[0094] Step 2: adding 100 parts by weight of the carrier and 10 parts by weight of water into a strong mixer for mixing, and the mixing time is 15 minutes;

[0095] Step 3: Add 115 parts by weight of the carrier and 10 parts by weight of 20% ammonia water into a powerful mixer for mixing. When the temp...

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Abstract

The invention relates to a catalyst and a preparation method thereof, in particular to a flue gas denitration catalyst applied at a low temperature and a preparation method thereof. TiO2 doped with one or multiple of Al2O3, SiO2 or ZrO2 is taken as a carrier, glass fiber is taken as a skeleton, and vanadium compounded with one or multiple of tungsten, molybdenum, cerium, manganese, niobium or phosphorus is taken as an active component. The flue gas denitration catalyst comprises the carrier, active precursor aqueous solution, glass fiber, stearic acid, lactic acid, wood pulp, monoethanolamine, polyoxyethylene, methylcellulose, ammonia water and water. The catalyst has good low-temperature denitration activity; and within the temperature of 150-300 DEG C, denitration efficiency of the catalyst is up to 85% or above. The catalyst has high sulfur-poisoning resistance and water-poisoning resistance capacity, and long-term use of the catalyst at a low temperature is guaranteed. Further, the catalyst can be applied to fields such as glass production, coking, cement, industrial kilns, waste incineration and chemical engineering widely. The invention further provides a preparation method of the catalyst, which is reasonable in processing.

Description

technical field [0001] The invention relates to a catalyst and a preparation method thereof, in particular to a flue gas denitrification catalyst used under low temperature conditions and a preparation method thereof. Background technique [0002] With the increasingly stringent environmental protection requirements, in addition to coal-fired power stations, waste gas discharged from glass, coking, cement, industrial kilns, waste incineration and chemical plants also needs to be denitrified. Among many denitrification methods, selective catalytic reduction (SCR) technology is widely used due to its high denitrification efficiency and good selectivity. This technology is mainly based on the use of NH 3 As a reducing agent, the NOx in the flue gas (mainly NO and NO 2 ) is reduced to N 2 , while generating H 2 O. The core component is the denitration catalyst. The key to the success of this technology is the activity, selectivity and life of the denitration catalyst under ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34B01J23/28B01J23/22B01D53/86B01D53/56
Inventor 王志民张延东李慧远翟长征张红超许磊
Owner SHANDONG GEMSKY ENVIRONMENTAL PROTECTION TECH CO LTD
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