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Automotive spark-ignited direct-injection gasoline engines

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526<br />

F. Zhao et al. / Progress in Energy and Combustion Science 25 (1999) 437–562<br />

distributed uniformly to individual cylinders at a much<br />

lower pressure differential than is typical with PFI <strong>engines</strong>.<br />

Such an increased EGR rate may result in a substantial<br />

temperature increase of the intake air, which may degrade<br />

the full load performance. It is also quite difficult to provide<br />

an appropriate amount of EGR during GDI mode transitions.<br />

Fraidl et al. [142] designed a variable EGR distributing<br />

system to circumvent the disadvantages of current EGR<br />

systems. A distribution plenum in close proximity to the<br />

cylinder is designed to be closed by means of a rotary<br />

disk valve. The opening of the cylinder feed lines is<br />

synchronized with the firing order, with the actual metering<br />

occurring within an electrically operated EGR valve. At part<br />

load, a large cross-section is opened to each individual<br />

cylinder, allowing a high EGR mass flow rate while maintaining<br />

an even distribution to all cylinders. At full load, or<br />

during engine transients, the EGR system close to the cylinder<br />

is shut off, improving the EGR dynamics. For the transition<br />

into part load operation, EGR is available close to the<br />

cylinder head by opening the distributing plenum. As only a<br />

small section of intake manifold is exposed to hot exhaust<br />

gas, the temperature increase of the induction air is less than<br />

with the conventional central feed design.<br />

Even though EGR is widely employed for reducing the<br />

NOx emissions in SI <strong>engines</strong>, there is a general view in the<br />

literature that the progress of GDI <strong>engines</strong> is strongly<br />

coupled to the development of lean-NO x catalysts. This is<br />

because EGR cannot reduce the NOx emissions over the<br />

entire engine speed-load map to meet the scheduled<br />

emission limits in North America, Europe and Japan. For<br />

example, within the US FTP emission test cycle the GDI<br />

engine operates for a significant fraction of the time with a<br />

lean homogeneous mixture at a stable lean limit. In such an<br />

operating condition, large amounts of EGR cannot be used,<br />

as the engine combustion stability would be significantly<br />

degraded. Also, the stratified-charge region in the operating<br />

map is narrowed when restricted to low NO x levels, thus<br />

reducing the achievable fuel economy improvement. Therefore,<br />

a proven lean-NOx-catalyst technology would definitely<br />

be a welcome tool in order to make optimum use of stratified<br />

combustion technology, as the conversion efficiencies and the<br />

durability of lean-NOx catalysts are still lacking when<br />

compared with the current three-way catalyst. A significant<br />

research effort is currently being <strong>direct</strong>ed toward this desired<br />

technology [232]. A stoichiometric homogeneous mixture<br />

could be used in the GDI engine in combination with the<br />

three-way catalyst, but the achievable level of fuel economy<br />

would be theoretically lower for this class of GDI engine.<br />

A number of technologies are currently being explored<br />

for NO x reduction in lean-burn and stratified-charge <strong>engines</strong>.<br />

These, with the associated technical issues, are summarized<br />

as follows.<br />

• Selective-reduction, lean NO x catalysis:<br />

◦ reduces tailpipe NOx emissions when engine is operated<br />

lean;<br />

Fig. 91. Comparison of the selective-reduction-type and storagetype<br />

lean-NOx catalysts [17].<br />

◦ requires some UBHC to reduce NO x;<br />

◦ lower conversion efficiency;<br />

◦ narrow working temperature range, depending on<br />

catalyst materials;<br />

◦ not as durable as conventional three-way catalysis;<br />

◦ high resistance against sulfur contamination.<br />

• NO x absorber:<br />

◦ stores NOx while engine is operated lean;<br />

◦ converts stored NOx during a rich excursion in air–<br />

fuel ratio;<br />

◦ no UBHC required to store NOx;<br />

◦ can be installed downstream from other catalysts;<br />

◦ higher conversion efficiency over an operating<br />

window of 350–500C;

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