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Commercial three way catalysts (TWC) are designed to eliminate HC, CO and NOx pollutants emitted from gasoline powered internal combustion engines. TWC have been optimized over many years to meet ever more stringent emission regulations. It has long been speculated that surface electrical conductivity may be a key parameter in controlling catalytic activity, however until now it has not been possible to reliably measure this physical parameter on a catalytic surface. In this study, the surface electrical conductivity of catalyst powders, such as Rh/ CeO1-x-ZrxO2, Rh/ZrO2 and Rh/Al2O3, were measured by EUPS (Extreme Ultraviolet excited Photoelectron Spectroscopy). Then the measured electrical conductivity was compared with catalyst performance from CO-NO and water gas shift reactions which are important for controlling automobile exhaust emissions from gasoline vehicles.

Palladium catalysts are known to show higher methane oxidation performance than platinum and/or rhodium catalysts. In this paper, the higher oxidative dehydrogenation activity on palladium is proposed as a reason for the superior methane oxidation. When other oxidation reactions are considered, higher affinity of palladium to oxygen has also been suggested[1]. In this study, oxygen chemical potential on platinum and palladium catalyst surfaces under oxidation conditions was measured using a specially designed electrochemical sensor. The oxygen chemical potential was calculated from the sensor potential by the Nernst equation. As a result, oxygen potential on palladium during the methane oxidation reaction was found to be much higher than that of platinum, correlating with affinity to oxygen and higher methane oxidation performance. The rate of oxygen adsorption and desorption on platinum and palladium was evaluated in an engine experiment using a dual lambda-sensor procedure.

Precious metal catalysts, such as Pt/Al2O3, are the primary active ingredient in diesel oxidation catalysts (DOC) used to control CO, HC and SOF emissions. Sintering of precious metal is one of the main deterioration factors of catalytic performance. In hot applications sintering of the alumina support material has also been suggested to accelerate precious metal sintering. Investigation of sintering rates may allow estimation of the catalyst life and provide information important for catalyst durability improvement. In this study, Pt/Al2O3 was used as a model catalyst and a sintering model for thermal aging was constructed. Pt sintering could be expressed by a differential equation which includes both Pt and support material sintering, but better fit to experimental data resulted from inclusion of a factor that includes an Al2O3 phase change.

To predict how DOC performance deteriorates with a lifetime of use, it is important to understand the mechanisms of catalyst aging. In off-road applications, due to the continuous high load usage and relatively high oil consumption rate, poisoning of the Diesel Oxidation Catalyst (DOC) with Phosphorus may become an important durability issue. In this study, 3D modeling has been performed to study the P poisoning mechanism and 1D modeling has been performed to investigate P poisoning parameters that effect DOC performance deterioration. From postmortem analysis on engine aged DOCs there is a general trend that P deposits tend to collect at the outermost catalyst surface. Two types of 3D modeling were performed in this study to understand how P migrates into the bulk of the catalyst. In one case, P migrates into catalyst layer by gas phase diffusion and in the other case P first adsorbs on the catalyst surface and then migrates by solid diffusion into the bulk.

Sulfate generation by diesel oxidation catalysts (DOC) is still a problem although sulfur concentration in the diesel fuel will be reduced in future. Two approaches were attempted to reduce the sulfate generation without inhibiting the HC and CO oxidation performance. One was to use an optimized support material that adsorbs less SO2 and has sufficient specific surface area for HC/CO oxidation. Another approach was to apply a layer on the catalyst, which prevents SO2 adsorption. Sulfate generation was successfully reduced while maintaining high HC/CO oxidation performance.

The reduction of NOx in exhaust gas has been a major challenge in diesel engine development. For the NOx reduction issues, a new Lean NOx Catalyst (LNC) aftertreatment system has been developed by Honda. A feature of the LNC system is the method that is used to reduce NOx through an NH₃-Selective Catalytic Reduction (NH₃-SCR). In an LNC system NOx is adsorbed at lean conditions, then converted to NH₃ at rich conditions and subsequently reduced in the next lean phase. In recent years, as the efficiency of the diesel engine has improved, the exhaust gas temperatures have been reduced gradually. Therefore, the aftertreatment system needs to be able to purify NOx at lower temperatures. The development of a new LNC which has a high activity at low temperature has been carried out. For the improvement of the LNC three material improvements were developed. The first of these was the development of a NOx adsorbent which is matching the targeted exhaust gas temperatures.

Combustion behavior of the SOF (Soluble organic fraction) fraction of diesel particulate by flow-thru type diesel oxidation catalysts (DOC) was studied. A two brick DOC system with an air gap showed higher SOF performance than a single brick DOC of the same total volume. Collision frequency of the TPM (total particulate matter) to the catalyst layer was studied by calculation of the turbulence energy in the gas flow channel. No large difference in collision frequency was observed between one brick and two bricks. The front face effect was calculated from the geometric surface and it was confirmed that such an effect was small in the two brick DOC case. The SOF performance advantage for the two brick DOC system separated by an air gap was due to a thermo-mass effect created by reducing the DOC volume.

The transient HC performance of diesel oxidation catalysts is known to be greatly improved by addition of Zeolite material. The authors already reported how to estimate the effective washcoat thickness in our previous study [1]. To understand in more detail the effective catalyst layer thickness, a precise gas diffusion model and parameters of HC adsorption and desorption rate were determined in this study. The random pore model was used for a gas diffusion calculation to simulate the macro porosity of the catalyst layer and micro porosity of the Zeolite material. HC adsorption capacity as a function of temperature and HC concentration was measured by Temperature Programmed Desorption (TPD). HC desorption rate was evaluated by changing the TPD ramping rate. HC reaction rate was evaluated by using a model gas reactor. Calculated catalyst performance correlated to the experimental results, thus validating the model.

Palladium is well known to catalyze methane (CH4) oxidation more efficiently than platinum (Pt) and/or rhodium (Rh) catalysts. The mechanism for methane oxidation on palladium is hypothesized to proceed via a radical intermediate. Direct identification of a radical species was not detected by Electron Spin Resonance Spectroscopy (ESR). However, indirect evidence for a radical intermediate was found by identification of ethane (C2H6), the methyl radical(CH3 ˙ ) coupling product, by Mass spectroscopy analysis under CH4/O2 conditions.

A new Pd-Rh three-way catalyst (TWC) for close-coupled (CC) applications was developed to improve low temperature gas activity. In this study the TWC has a layered structure with Pd in the top layer and Rh in the bottom layer. The specific objectives of this study was to compare Ba and La additives to Pd in the top layer. Alumina was used for the Pd support and La or Ba were co-impregnated with Pd. The catalysts were engine aged at 950°C for 200 h and evaluated on a vehicle using the European NEDC test, for CO, HC and NOx performance. After this aging, the Pd-La catalyst showed higher gas performance than the Pd-Ba catalyst, especially in the cold start region. This improvement was correlated to the Pd particle size and the sintering suppression observed upon addition of La. Sintering suppression was also observed upon addition of Ba; however, the mechanism appears to be different from that of La addition.

Diesel oxidation catalysts (DOCs) combining the functions of Pd and Pt-Pd alloys have been used in practice to satisfy the strict exhaust emission regulations that have been specified for passenger cars in recent years. Pd is an indispensable component in DOCs because it exhibits superior oxidation activity for CO and HC. To reduce the amount of precious metal used and to improve robustness, it is important to control the electronic state and gas adsorption characteristics of Pd and PdOx during catalytic reactions.In this study, by investigating the CO adsorption behavior of Pd, it was observed that Pd supported on a CeO2/ZrO2 mixed-oxide material (CZ) showed a preferable CO adsorption state and better CO light-off performance. Pd in Pd/CZ became metallic with increasing reaction time, and the CO oxidation performance of Pd/CZ decreased. This change in activity was correlated with CO adsorption on Pd changing from linear-type to bridge-type adsorption.