Catalyst and method for reducing nitrogen oxides in exhaust streams with hydrocarbons or alcohols

一种氮氧化物、催化剂的技术,应用在氮氧化物的催化剂领域,能够解决不适合空间有限的应用、不存在还原剂、不可重现性等问题

Active Publication Date: 2008-03-05
TANAKA PRECIOUS METAL IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Three-way catalysts are not effective in removing NO from exhaust gases with high concentrations of oxygen, such as those from steam turbines, diesel engines, and gasoline engines operating in lean burn mode x , this is because there is not enough reducing agent in the exhaust gas to reduce NO x
It is also necessary to selectively reduce NO with hydrocarbons or alcohols x Catalysts and methods wherein the catalyst system does not rely on the spacing between the two catalysts, as this spacing can lead to non-reproducible or bulky systems unsuitable for space-constrained applications

Method used

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  • Catalyst and method for reducing nitrogen oxides in exhaust streams with hydrocarbons or alcohols
  • Catalyst and method for reducing nitrogen oxides in exhaust streams with hydrocarbons or alcohols
  • Catalyst and method for reducing nitrogen oxides in exhaust streams with hydrocarbons or alcohols

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0182] NO on silver on alumina catalyst with and without oxidation catalyst as a function of temperature x conversion rate of

[0183] Silver / alumina monolithic catalysts were prepared as described below. A slurry is formed by mixing water, silver nitrate and alumina. Ball mill this slurry, and at 400 cells / inch 2 Coating on a monolithic substrate of , and firing at 600 °C, yielded 1.2% silver on alumina monolithic substrate coated catalyst 10.

[0184] Figure 2 shows the results for 1.2% silver / Al with and without platinum on an alumina oxidation catalyst 30 placed in the feed stream after the silver catalyst as shown in Figure 1 2 o 3 Catalyst 10, NO x A graph of conversion versus temperature (°C). Contains 500ppmNO x Tests were conducted with a feed stream of 600 ppm ethanol. The feed gas also contains 15% oxygen, 5% carbon dioxide, 10% water vapor and the balance nitrogen. The flow rate of the raw material stream is maintained at 1 standard liter / minute, which cor...

Embodiment 2

[0189] Contains 25ppmNO x In the case of a feed stream, with and without an oxidation catalyst, NO over a silver catalyst x Conversion rates

[0190] Silver / alumina monolithic catalysts were prepared using two different preparation methods. Catalyst 1 was prepared using the one-step carrier coating method described in Example 1.

[0191] Catalyst 2 was prepared in a two-step process by coating a substrate with an alumina support and then impregnating the alumina support coat with an aqueous solution of silver nitrate. Catalyst 2 was prepared as described below. An alumina slurry is formed by mixing alumina and water. Ball mill the slurry at 400 cells / inch 2 coated on monolithic substrates and dried. Silver nitrate was impregnated on the alumina coated monolith and fired at 600°C to yield 1.2% silver on alumina catalyst.

[0192] Table 2 shows the metal loading on the calcined monolith catalysts, where the percentage loading is calculated on a metal basis relative to the...

Embodiment 3

[0205] With and without oxidation catalyst, using propane as reductant, with 9ppm NO x feed stream, NO over silver / alumina catalyst x Conversion and CO production

[0206] Figure 4 shows the use of 9ppm NO x raw material gas, using 6000ppm propane as reducing agent, for silver / alumina catalyst, NO x A series of plots of conversion (left-hand axis) and outlet CO (right-hand axis) versus temperature for . The feed gas also contains 12% oxygen, 4% carbon dioxide and 10% water vapor, with the balance being nitrogen. at 8000h -1 Experiments were performed at a space velocity of .

[0207] When propane is used as reducing agent, as NO x A by-product of the conversion produces CO. CO is oxidized with an oxidation catalyst, thereby removing CO. However, in the presence of an oxidation catalyst, the apparent NO x The conversion rate dropped significantly, as shown in Figure 4. Oxidation catalysts are thought to oxidize the nitrogen-containing intermediates formed via Reaction...

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Abstract

A catalyst system and a method for reducing nitrogen oxides in an exhaust gas by reduction with a hydrocarbon or oxygen-containing organic compound reducing agent are provided. The catalyst system contains a silver catalyst and a modifier catalyst, where the modifier catalyst contains a modifier oxide, where the modifier oxide is selected from the group consisting of iron oxide, cerium oxide, copper oxide, manganese oxide, chromium oxide, a lanthanide oxide, an actinide oxide, molybdenum oxide, tin oxide, indium oxide, rhenium oxide, tantalum oxide, osmium oxide, barium oxide, calcium oxide, strontium oxide, potassium oxide, vanadium oxide, nickel oxide, tungsten oxide, and mixtures thereof. The modifier oxide is supported on an inorganic oxide support or supports, where at least one of the inorganic oxide supports is an acidic support. The catalyst system of the silver catalyst and the modifier catalyst provides higher NOx conversion than either the silver catalyst or the modifier catalyst alone.

Description

[0001] priority claim [0002] This application claims the benefit of US Provisional Application No. 60 / 657,500, filed February 28, 2005, under 35 U.S.C. 119(e). technical field [0003] This invention relates to catalysts and methods for the selective reduction of nitrogen oxides in exhaust gases containing excess oxygen by hydrocarbons or oxygen-containing organic compounds. Background technique [0004] Exhaust gases from internal combustion engines, power plants, industrial furnaces, heaters, diesel engines, and other devices contain nitrogen oxides, carbon monoxide, and unburned hydrocarbons. Exhaust gases from these sources also contain excess oxygen, water vapor and sulfur dioxide. [0005] Emissions of nitrogen oxides, carbon monoxide and hydrocarbons are limited due to environmental regulations. [0006] Nitrogen oxides from static and dynamic sources are one of the causes of acid rain. Various methods have been proposed to reduce nitrogen oxide emissions from ex...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J35/00B01J23/10B01J35/04B01J23/745B01J21/04B01J23/72B01J23/50B01J23/83
CPCB01D2255/908B01J37/0234B01J37/0215B01D2251/21B01J37/0242B01J21/04B01D53/8628B01J23/50B01D2255/504B01J23/89B01J35/0006B01J23/83B01D2255/502B01D53/8625B01D2251/208B01D53/9418B01J35/04B01J23/66B01J37/0246B01J23/894B01D2255/104B01J35/19B01J35/56
Inventor R·V·马尔亚拉S·J·戈尔登S·伊列斯加亚
Owner TANAKA PRECIOUS METAL IND
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