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A low-temperature flue gas denitration catalyst using CO to selectively reduce NOx and its application

A denitration catalyst, low temperature flue gas technology, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of reduced NO removal rate, unsuitable catalyst preparation, and low specific surface area.

Active Publication Date: 2022-06-17
山东逸轩环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this study, due to the high concentration of CO, when the conversion rate is high, the catalyst particles and bed temperature will increase significantly, thereby improving the NO removal rate. If the volume concentration of CO is 0.15%, the catalyst particles and bed temperature When the temperature is at the corresponding value, the NO removal rate will drop significantly
On the other hand, when an alumina carrier calcined at a temperature below 850°C is used, because of its high activity, a nitration reaction will occur at a temperature below 180°C and oxygen-containing conditions, resulting in the gradual deactivation of the catalyst; 850°C The alumina carrier calcined at the above temperature is not suitable for the preparation of the catalyst due to its low specific surface
[0007] There is also the prior art of using noble metals as catalyst active components, which has high activity in the low-temperature reaction of CO selective reduction of NOx, but the cost is too high, and it is not easy to apply in ordinary occasions

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] The low-temperature flue gas denitration catalyst using CO to selectively reduce NOx of the present embodiment is prepared according to the following steps:

[0033] A. Add Cu(NO) to the 5L stirred tank 3 ) 2 0.20mol / L, Mn(NO 3 ) 2 2.0L of 0.20mol / L aqueous solution (quality 2110g), pH 3.5; start stirring, heat up to 90°C, add 1280g of newly prepared ammonium type SSZ-13 molecular sieve water-containing suction filter cake (550g in terms of solids), control The temperature was 85°C for 1.5h for ion exchange, suction filtration, rinsing and suction filtration with 2400g water three times, the filter cake was dried at 120°C for 5h, calcined at 570°C for 6h in an air-conditioned muffle furnace, and pulverized to -600 mesh to obtain Cu -Mn / SSZ-13 molecular sieve calcined powder; the Cu-Mn / SSZ-13 molecular sieve calcined powder obtained by testing, in terms of oxide mass content, contains CuO2.6% and MnO1.7%; ammonium type SSZ-13 is prepared The sodium type SSZ-13 molecu...

Embodiment 2

[0038] The steps A-C of Example 1 were basically repeated to prepare the low-temperature flue gas denitration catalyst using CO to selectively reduce NOx in this example. The difference was that in step B, the amount of basic copper carbonate was 160 g, and the aluminum phosphate sol-pseudoboehmite composite glue was used. The consumption of the liquid is 1300g, and the water absorption rate of the obtained roasted bar is 0.42ml / g; in step C, 84ml of acetic acid aqueous solution with a mass concentration of 75% is sprinkled.

[0039] It is estimated that the mass percentage of each main component in the low-temperature flue gas denitration catalyst of this embodiment is about 37.7% of SSZ-13 molecular sieve in hydrogen form, 9.5% of copper in CuO, and 5.0% of manganese in MnO.

Embodiment 3

[0041] Basically repeat the steps A-C of Example 2 to prepare the low-temperature flue gas denitration catalyst using CO to selectively reduce NOx in this example, the difference is that the amount of basic manganese carbonate in step B is 180g, the aluminum phosphate sol-pseudoboehmite composite glue The consumption of the liquid is 1400g, and the water absorption rate of the obtained roasted bar is 0.43ml / g; in step C, 86ml of acetic acid aqueous solution with a mass concentration of 80% is sprinkled.

[0042] It is estimated that the mass percentage of each main component in the low-temperature flue gas denitration catalyst of this embodiment is about 36.0% of SSZ-13 molecular sieve in hydrogen form, 10.0% of copper in CuO, and 8.0% of manganese in MnO.

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PUM

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Abstract

The invention provides a low-temperature flue gas denitrification catalyst using CO to selectively reduce NOx, comprising 20-50% of SSZ-13 molecular sieve in terms of hydrogen type, 5-12% of copper in terms of CuO, and 4-8% of manganese in terms of MnO ; Made through the following steps: ammonium-type SSZ‑13 molecular sieve, adding Cu and Mn nitrate aqueous solution for ion exchange, filtering, washing, drying, and roasting at 550‑580 ° C to obtain Cu‑Mn / SSZ‑13 molecular sieve roasting powder , containing CuO2‑4%, MnO1‑2%; Cu‑Mn / SSZ‑13 molecular sieve roasting powder 30‑60 parts, basic copper carbonate 5‑12 parts, manganese carbonate 4‑11 parts, washed kaolin 30‑50 parts, Mix evenly, sprinkle 100-130 parts of aluminum phosphate sol-pseudo-boehmite composite glue, knead, extrude, dry, and roast at 500-550°C; the roasted bars are soaked in aqueous acetic acid solution, and after drying, dry at 300- Roasting at 330°C for 2-4hrs to prepare a low-temperature flue gas denitrification catalyst; at 120-160°C, the concentration of CO is relatively low and reacts with NOx to form N 2 Under the condition of required excess of 10-200%, 2000mg / m 3 NOx treatment below ≤60 mg / m 3 , including 300‑500mg / m 3 NOx treatment to ≤40mg / m 3 .

Description

technical field [0001] The invention belongs to the technical field of NOx-containing gas treatment, and in particular relates to a low-temperature flue gas denitration catalyst for selectively reducing NOx by using CO and its application. Background technique [0002] There are many combustion and roasting processes with a small amount of exhaust gas in industrial production, and the exhaust gas flow contains a relatively low concentration such as 300-3000mg / m 3 NOx and CO with a slightly higher concentration, the airflow temperature is low such as 100-160 ℃, and there are generally fluctuations in temperature and airflow. This kind of gas is treated with dry chemical denitrification agent, or wet chemical absorption denitration treatment, which can reach 200 or 100 mg / m 3 However, it is inconvenient to pass the selective catalytic reduction reaction (NH 3 -SCR) for denitration. The dry chemical denitrification treatment has high cost of solid denitrification and disposa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/78B01J35/10B01D53/86B01D53/56
CPCB01J29/78B01J35/1033B01D53/8628
Inventor 胡文宾解小虎宋西磊
Owner 山东逸轩环保科技有限公司
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