Abstract

According to the strict European exhaust emissions standards that have been imposed by European legislation there is an elevated need for the decrease of the toxic gas emissions from vehicles. Therefore, car manufacturers have implemented a series of catalytic devices in the aftertreatment of the engine to comply with the standards. All catalytic devices (such as three-way catalysts, diesel particulate filters and diesel oxidation catalysts) accumulate concentrated loading of platinum group metals (PGMs, platinum, palladium, rhodium) as the active catalytic phase. Thus, the demand for PGMs is constantly increasing with a subsequent increase in their market prices. As a result, the research on catalytic converters of high activity and reduced cost/PGM loading is of great interest. In the present work, the Prometheus catalyst, a polymetallic nanosized copper-based catalyst for automotive emission control applications, is presented in two different metal loadings (2 wt% and 5 wt%) and metal ratios (Cu/Pd/Rh = 21/7/1 and Cu/Pd/Rh = 21/7/3). For the first time, a three-metal (copper, palladium, rhodium) nano-catalyst has been synthesized and characterized on a large scale. By using copper as an active catalytic phase, a reduction of PGMs loading is achieved (up to 85%) resulting in a novel catalytic device with similar or improved catalytic performance compared to commercial ones. The Prometheus catalyst is prepared by a wet impregnation method, using as a carrier an inorganic mixed oxide (CeZrO4) exhibiting elevated oxygen storage capacity (OSC). The heterogeneous catalytic powders produced were characterized by both spectroscopic and analytical methods. The metal content and ratio were determined by inductively coupled plasma mass spectrometry (ICP-MS), X-ray fluorescence (XRF) and energy-dispersive X-ray spectroscopy (EDS). The morphology and the catalyst particle size were determined with scanning electron microscopy (SEM) and X-ray diffraction (XRD). The investigation revealed homogeneous particle formation and dispersion. The deposition of the metal nanoparticles on the porous inorganic carrier was verified with N2 sorption. Catalytic performance and reactivity of a catalyst (pure wash coat) with molar ratio 21/7/1 and a full-scale Prometheus catalyst with the desired loading of 15 g/ft3 were tested on an in-house synthetic gas bench (SGB) for the abatement of CO, CH4 and NO, both presenting high catalytic activity.

Highlights

  • The growth of the vehicle fleet and the extensive use of cars during the last decades are the main causes of the observed increasing trend of the emissions originated from the transport sector

  • It must be mentioned that palladium and platinum are the active components for CO and HC oxidation and the main role of rhodium is in NOx reduction (Figure 1) [1]. and platinum are the active components for CO and HC oxidation and the main role of

  • A novel trimetallic copper-based nano-catalyst comprising copper, palladium and rhodium supported on Ce0.68Zr0.32O2 carrier (CZ) was produced and physiochemically characterized

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Summary

Introduction

The growth of the vehicle fleet and the extensive use of cars during the last decades are the main causes of the observed increasing trend of the emissions originated from the transport sector. The need for automotive industries for catalytic converters of high efficiency is essential, since they represent a key part of the exhaust system of every modern vehicle with internal combustion engine Such catalytic converters, named three-way catalysts, demand higher content of the catalytic phase, which consists mainly of platinum, palladium and rhodium (platinum group metals, PGMs), leading subsequently to increased cost for the manufacturers and the automotive industry. According to Lin Dong et al, NO conversion has an intimate relation with the loading amount of CuO and the supports used at temperature lower than 200 ◦C, and the activities decreased in the order: CuO/CeO2 > CuO/γ-Al2O3 > crystalline CuO Under these reaction conditions, the activity of the catalysts strongly depended on the surface dispersed copper oxide species. Approximately 1.5 g of each sample was loaded into the BET tube and degassed at 300 ◦C for 19 h under high vacuum prior analysis in order to completely remove the chemisorbed water from sample surface

Catalytic Activity Measurement
MorpChHol4ogy and Structure of the Catalyst2500 ppm
Catalyst Loading
Catalytic Performance
Conclusions
Findings
Patents
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