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Exhaust treatment system including a nickel-based catalyst

a technology of exhaust treatment system and catalyst, which is applied in the direction of metal/metal-oxide/metal-hydroxide catalyst, machine/engine, arsenic compound, etc., can solve the problems that conventional cerium-based oxides do not generate the oxygen needed for hc and co oxidation, and achieve the reduction of carbon monoxide, hydrocarbon emissions, and nitrogen oxides

Active Publication Date: 2013-08-08
FORD GLOBAL TECH LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent describes a catalyst that reduces harmful emissions from vehicle exhausts. The catalyst is made with a special carrier that does not react with nickel, which is commonly used in catalysts. The catalyst contains a small amount of nickel and is effective at reducing carbon monoxide, hydrocarbons, and nitrogen oxides. The catalyst also helps to produce further reductions of carbon monoxide and hydrocarbons through a water-gas-shift reaction or steam-reforming reaction. Overall, the invention provides a novel and effective catalyst for reducing harmful emissions from vehicle exhausts.

Problems solved by technology

However, in some vehicle operations with long and rich air / fuel excursions, conventional cerium-based oxides do not generate sufficient amounts of oxygen needed for the oxidation of HC and CO.

Method used

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  • Exhaust treatment system including a nickel-based catalyst
  • Exhaust treatment system including a nickel-based catalyst
  • Exhaust treatment system including a nickel-based catalyst

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0052]Samples with various Ni loadings on a cordierite carrier were prepared. A 2.15 g of nickel nitrate solution with 0.1013 g Ni / g-solution was prepared and impregnated into a 4.53 g cordierite substrate having a honeycomb structure of 1 inch×1 inch. The impregnated sample was then dried at 150° C. for 1 hour and calcined at 350° C. in air for one hour prior to use. The resulting substrate contained 4.6 wt % Ni. The OSC values for the sample were measured shortly after preparation by placing the sample in a quartz reactor with helium flowing through the reactor, followed by the addition of CO into the helium flow. The consumption of CO or the production of CO2 from the reaction of CO to oxygen contained in the OSC-bearing catalyst was monitored using a quadruple mass spectrometer. The OSC values are shown in Table 1 below.

TABLE 1OSC values for 4.6 wt % Ni on cordierite of 1″ L × 1″ DOSC (mole O) measured at ° C.Theoretical OSC400° C.600° C.700° C.3.73 × 10−3 mole O3.86 × 10−33.81 ...

example 2

[0053]A commercial catalyst containing 5 wt % nickel was prepared and subjected to a simulated aging process mimicking 4,000 (4K) or 120,000 (120K) vehicle miles. The samples were aged on a pulse-flame combustor (pulsator) using a Ford standard 4-mode aging cycle (the pulsator combusts fuel to generate a simulated vehicle exhaust). The samples were placed in the pulsator exhaust gas stream and subjected to cyclic air-fuel conditions at an exponentially weighted temperature of 930° C. in order to accelerate the aging process. The 4K samples were aged for 8 hours and the 120K samples were aged for 120 hours.

[0054]The OSC value of the commercial catalyst was determined using a gasoline flame-combustor (pulsator). These values were compared to catalysts prepared as described below containing 1) 12 wt % Ni on cordierite and 2) 12 wt % Ni and 1.7 wt % Pt.

[0055]Sample 1 was prepared by impregnating a substrate of 4.53 g cordierite (1″L×VD) with 2.15 g of Ni solution with 0.1013 g Ni / g-solu...

example 3

[0059]A catalyst was prepared by washcoating alumina onto a cordierite substrate and then impregnating the alumina / cordierite with nickel. The process of loading nickel was the same as that described in Example 1. The catalyst of nickel on alumina / cordierite the two samples of nickel on cordierite were aged under alternative flows of 1% CO and 0.5% O2 at 1000° C. (redox-aging) for 12 hours, simulating the rich-lean cycles of gasoline engine exhausts. The OSC values after the redox-aging are shown in Table 3.

TABLE 3OSC after the redox-aging at 1000° C. over 1′ L × 1″ D samples: alumina effectOSC (×10−3 mole O) measured at T =Ni loadingSupport600° C.700° C.13.8 wt %alumina / cordierite0.630.768.95 wt %cordierite3.045.1012.6 wt %cordierite4.757.96

[0060]As can be seen, the OSC values for nickel on alumina / cordierite after aging were dramatically diminished in comparison with those for the sample of nickel on cordierite. It is believed that the nickel-alumina interaction caused the severe ...

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Abstract

A nickel-based catalyst is provided for reducing carbon monoxide, hydrocarbon emissions, and nitrogen oxides from vehicle exhausts. The catalyst is impregnated directly onto a carrier which is non-reactive with nickel. The nickel is contained on said carrier at a loading of between about 2 to about 20 wt %. When used in a vehicle exhaust gas treatment system, the catalyst provides improved efficiency in reducing CO, HC, and NOx emissions over the use of conventional three-way-catalysts.

Description

BACKGROUND OF THE INVENTION[0001]Embodiments described herein relate to the preparation and use of nickel-based catalysts in reducing carbon monoxide, hydrocarbon emissions, and nitrogen oxides (NOx) from vehicle exhausts, and more particularly, to a nickel-based catalyst used in a vehicle aftertreatment system to provide supplemental oxygen storage capacity for the oxidation of carbon monoxide and hydrocarbons, and the reduction of nitrogen oxides.[0002]In recent years, government regulations in the United States have restricted emissions of carbon monoxide (CO), hydrocarbons (HC) and nitrogen oxides (NOx) from vehicle engine exhausts. This has necessitated the use of catalysts in gasoline-powered vehicles which function to stimulate the oxidation reaction of HC and CO and the reduction of NOx. Such catalysts are typically referred to as three-way conversion (TWC) catalysts because they simultaneously oxidize CO and HC to CO2 and water while reducing NOx to nitrogen. Three-way conv...

Claims

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Application Information

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IPC IPC(8): B01D53/94B01J21/06B01J29/072B01J27/224B01J21/08B01J37/02B01J23/89B01J23/83B01J21/02B01J23/78B01J23/86B01J23/889B01J23/755B01J21/04
CPCB01D53/56B01D2255/908B01D53/72B01D53/94B01J23/755Y02T10/22B01J37/0244B01J37/038B01J23/8892B01J35/0006B01J23/42B01J23/44B01J23/464B01J23/58B01J23/63B01J23/866B01J23/892B01J35/04B01J37/0201B01D53/945B01D2255/1021B01D2255/1023B01D2255/1025B01D2255/2042B01D2255/2063B01D2255/2066B01D2255/2073B01D2255/20746B01D2255/20753B01D2255/20761B01D2255/20784B01D2255/9022B01D53/62Y02A50/20Y02T10/12B01J35/19B01J35/56
Inventor HEPBURN, JEFFREY SCOTTJEN, HUNGWENTHANASIU, EVA
Owner FORD GLOBAL TECH LLC
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