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OCTOBER 19-20, 2012 - YMCA University of Science & Technology

OCTOBER 19-20, 2012 - YMCA University of Science & Technology

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Proceedings <strong>of</strong> the National Conference on<br />

Trends and Advances in Mechanical Engineering,<br />

<strong>YMCA</strong> <strong>University</strong> <strong>of</strong> <strong>Science</strong> & <strong>Technology</strong>, Faridabad, Haryana, Oct <strong>19</strong>-<strong>20</strong>, <strong>20</strong>12<br />

4.2 Catalytic converter for diesel engines<br />

For compression-ignition (i.e., diesel engines), the most-commonly-used catalytic converter is the Diesel<br />

Oxidation Catalyst (DOC). This catalyst uses O 2 (oxygen) in the exhaust gas stream to convert CO (carbon<br />

monoxide) to CO 2 (carbon dioxide) and HC (hydrocarbons) to H 2 O (water) and CO 2 . These converters <strong>of</strong>ten<br />

operate at 90 percent efficiency, virtually eliminating diesel odor and helping to reduce visible particulates<br />

(soot). These catalysts are not active for NO x reduction because any reductant present would react first with the<br />

high concentration <strong>of</strong> O 2 in diesel exhaust gas.<br />

Reduction in NO x emissions from compression-ignition engine has previously been addressed by the addition <strong>of</strong><br />

exhaust gas to incoming air charge, known as exhaust gas recirculation (EGR). In <strong>20</strong>10, most light-duty diesel<br />

manufactures in the U.S. added catalytic systems to their vehicles to meet new federal emissions requirements.<br />

There are two techniques that have been developed for the catalytic reduction <strong>of</strong> NO x emissions under lean<br />

exhaust condition - selective catalytic reduction (SCR) and the lean NO x trap or NO x adsorber. Instead <strong>of</strong><br />

precious metal-containing NO x adsorbers, most manufacturers selected base-metal SCR systems that use a<br />

reagent such as ammonia to reduce the NO x into nitrogen. Ammonia is supplied to the catalyst system by the<br />

injection <strong>of</strong> urea into the exhaust, which then undergoes thermal decomposition and hydrolysis into ammonia.<br />

One trademark product <strong>of</strong> urea solution, also referred to as Diesel Emission Fluid (DEF), is AdBlue.<br />

Diesel exhaust contains relatively high levels <strong>of</strong> particulate matter (soot), consisting in large part <strong>of</strong> elemental<br />

carbon. Catalytic converters cannot clean up elemental carbon, though they do remove up to 90 percent <strong>of</strong> the<br />

soluble organic fraction, Diesel exhaust contains relatively high levels <strong>of</strong> particulate matter (soot), consisting in<br />

large part <strong>of</strong> elemental carbon. Catalytic converters cannot clean up elemental carbon, though they do remove up<br />

to 90 percent <strong>of</strong> the soluble organic fraction.<br />

5. Performance Analysis <strong>of</strong> Catalytic Converter<br />

The experimental methodology consists <strong>of</strong> two different parts. The first one is the emission test and the other one<br />

is microstructure and materials composition analysis. The emission test was conducted by multi-gas analyzer for<br />

emission measurements. After completing the test, the converters were cut to extract the substrate or<br />

‘honeycomb’ inside the housing and being analyzed for microstructure and materials composition using<br />

Scanning Electron Microscopy (SEM) and Energy Dispersive Analysis (EDX) [7].<br />

Fig 4: Experimental Setup [7]<br />

Two ceramic catalytic converters (underbody type) <strong>of</strong> different vehicle models were evaluated. The first one is<br />

extracted from PROTON Wira 1.3L and another one from FIAT Punto Selecta 1.2L. Both converters had same<br />

substrate material, synthetic cordierite ceramic and substrate shape, square cell except they differ in size,<br />

chemical properties and geometrical attributes. Double substrate systems are as thermal mass, geometric surface<br />

area, and washcoat distribution (Presti et. al <strong>20</strong>02). Per Marsh et. al (<strong>20</strong>01) have shown that less favorable mass<br />

transfer and higher flow velocity can be found as a results <strong>of</strong> the reduction <strong>of</strong> diameter, however, compensated<br />

with the cases <strong>of</strong> lower cell densities implemented on both converters for separate reduction and oxidation<br />

purposes.<br />

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