Flue gas treatment method for realizing desulphurization and denitrification simultaneously by using lanthanum-cerium oxide-loaded titanium dioxide nanotube array for catalytic reduction

A nanotube array, titanium dioxide technology, applied in the field of environmental protection science, can solve the problems of difficult separation and recovery of subsidiary products, difficult catalyst preparation, etc.

Active Publication Date: 2017-05-10
CENT SOUTH UNIV
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AI Technical Summary

Problems solved by technology

Using this method can achieve the purpose of catalytic desulfurization and denitrification at the same time, and can recover high value-added products elemental sulfur and nitrogen, and can also ensure the conversion rate of sulfur dioxide and nitrogen oxides in the flue gas and the recovery rate of product elemental sulfur and nitrogen. Difficult preparation of catalysts in the prior art and difficulties in separation and recovery of by-products

Method used

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  • Flue gas treatment method for realizing desulphurization and denitrification simultaneously by using lanthanum-cerium oxide-loaded titanium dioxide nanotube array for catalytic reduction
  • Flue gas treatment method for realizing desulphurization and denitrification simultaneously by using lanthanum-cerium oxide-loaded titanium dioxide nanotube array for catalytic reduction
  • Flue gas treatment method for realizing desulphurization and denitrification simultaneously by using lanthanum-cerium oxide-loaded titanium dioxide nanotube array for catalytic reduction

Examples

Experimental program
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Effect test

preparation example Construction

[0025] The preparation of catalyst of the present invention:

[0026] First, take a certain amount of tetrabutyl titanate and 40ml of absolute ethanol and put them in a beaker, add a certain amount of glacial acetic acid, which is called A liquid, and stir the A liquid on a magnetic stirrer until it is evenly mixed. Take another beaker, add 20ml of absolute ethanol, 5ml of distilled water and proportionately weighed crystals of lanthanum nitrate hexahydrate and cerium nitrate hexahydrate, stir and dissolve in the beaker, which is called liquid B. Pour liquid B into an acid burette, add it drop by drop to vigorously stirred liquid A at a uniform and slow speed, age at 30-80°C for 6-72h to form a gel, and then dry it in an oven at 105°C for 12h , and then roasted in a muffle furnace at 400-800°C for 1-9h to obtain catalyst particles, grind and sieve, and select 20-40 mesh particles for later use.

Embodiment 1

[0027] Example 1: 1La 2 o 3 -3CeO 2 -4TiO 2 Catalytic reduction and simultaneous desulfurization and denitrification

[0028] Load 10g of catalyst 1La in the reactor of the tubular resistance furnace 2 o 3 -3CeO 2 -4TiO 2 10 minutes with nitrogen gas first, then start to heat up, and nitrogen gas at the same time, when the temperature rises to 500°C, a mixed gas (10% by volume of nitrogen monoxide, 50% by volume of carbon monoxide, 20% by volume of sulfur dioxide, and the rest Nitrogen), the space velocity is 7000mL / (g h), the aeration time is 120 minutes, the exhaust gas is detected by the flue gas analyzer after passing through the condensation tank, and then the nitrogen is recovered after passing through the lime water, and the elemental sulfur and carbon are calculated by gravimetric method . The denitrification efficiency is 100%, the desulfurization efficiency is 97.1%; the elemental sulfur recovery rate is above 97.3%, and the N 2 The recovery rate is 98.4%, i...

Embodiment 2

[0029] Example 2: 2La 2 o 3 -5CeO 2 -7TiO 2 Catalytic reduction and simultaneous desulfurization and denitrification

[0030] Load 10g of catalyst 2La in the reactor of the tubular resistance furnace 2 o 3 -5CeO 2 -7TiO 2First pass nitrogen for 10 minutes, then start to heat up, and feed nitrogen at the same time, when the temperature rises to 500°C, feed mixed gas (10% by volume of sulfur dioxide, 5% by volume of nitrogen monoxide, 5% by volume of nitrogen dioxide , the volume percentage of carbon monoxide is 35%, and the rest is nitrogen), the space velocity is 10000mL / (g h), the aeration time is 120 minutes, the exhaust gas is detected by the flue gas analyzer after passing through the condensation tank, and then the nitrogen is recovered after passing through the lime water , elemental sulfur and carbon are calculated by gravimetric method. The denitrification efficiency is 100%, the desulfurization efficiency is 97.0%, the elemental sulfur recovery rate is 97.1%, ...

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Abstract

The invention provides a flue gas treatment method for realizing desulphurization and denitrification simultaneously by using lanthanum-cerium oxide-loaded titanium dioxide nanotube array for catalytic reduction. The method takes a titanium dioxide nanotube array as a catalyst carrier, and a catalyst is prepared by doping the catalyst carrier with lanthanum oxide and cerium oxide; the method comprises the steps of enabling mixed gas of carbon monoxide and flue gas containing sulfur dioxide or nitrogen oxide (nitric oxide and nitrogen dioxide) to pass through the catalyst at the temperature of 500 DEG C so as to enable the sulfur dioxide and the nitrogen oxide to respectively have catalytic reduction reaction with the carbon monoxide, wherein the sulfur dioxide is transformed into sulfur by means of reduction, cooling and then recovering the elemental sulfur, and the nitrogen oxide is transformed into nitrogen by means of reduction, absorbing the tail gas by using alkaline liquor and then recovering the nitrogen. After the method is adopted, not only are the aims of realizing desulphurization and denitrification at the same time achieved, but high added-value products, i.e., the elemental sulfur and the nitrogen are also recovered, and the tail gas also can reach the current emission standard. After the method is adopted, the desulphurization efficiency is 96% or above, the denitrification efficiency is 99.9% or above, the elemental sulfur recovery rate is 97% or above, and the N2 recovery rate is 98% or above.

Description

technical field [0001] The invention belongs to the field of environmental protection science, and relates to a flue gas treatment method for catalytic reduction of titanium dioxide nanotube arrays loaded with lanthanum cerium oxide and simultaneous desulfurization and denitrification. Background technique [0002] At present, simultaneous desulfurization and denitrification technologies are divided into two categories: (1) Selective catalytic reduction method: using reducing agents CO, H 2 , NH 3 and CH 4 Etc to reduce SO 2 and NOx are elemental sulfur and N, respectively 2 , to achieve desulfurization and denitrification; (2) Oxidation method, using an oxidant to oxidize water-insoluble NO to generate NO 2 , thus with SO 2 At the same time, it is absorbed in the lye in the later stage to achieve the purpose of desulfurization and denitrification. The oxidant of the oxidation method is expensive, the equipment requirements are relatively high, and the oxidation produc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/90B01D53/60B01J23/10
CPCB01D53/8637B01D53/90B01D2251/204B01D2255/2063B01D2255/2065B01D2255/20707B01D2256/10B01D2258/0283B01J23/002B01J23/10B01J2523/00B01J2523/3706B01J2523/3712B01J2523/47Y02A50/20
Inventor 何汉兵秦毅红张党龙
Owner CENT SOUTH UNIV
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