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Catalysis : an Integrated Approach to Homogeneous ...

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1 -HISTORY OF CATALYSIS 17<br />

1960 laws on mo<strong>to</strong>r vehicle emission st<strong>an</strong>dards were enacted which would<br />

become operative when at least two different devices were developed which<br />

could measure these st<strong>an</strong>dards. This gave a large impetus for the research.<br />

However, in the mid-’60s, the car industry <strong>an</strong>nounced that engine modifications<br />

were successful <strong>an</strong>d that the st<strong>an</strong>dards could be met without catalytic converters.<br />

This delayed further research in the development of catalytic converters. In the<br />

late ‘60s a further tightening of the st<strong>an</strong>dards was <strong>an</strong>nounced <strong>an</strong>d catalytic<br />

research increased considerably. The Cle<strong>an</strong> Air Act of 1970 set st<strong>an</strong>dards that<br />

went well beyond existing technology <strong>an</strong>d it was clear that catalytic mufflers<br />

would be essential.<br />

The initial objective was <strong>to</strong> reduce the emission of CO <strong>an</strong>d hydrocarbons. The<br />

mixture in the engine was fuel-rich <strong>an</strong>d under those conditions the concentration-<br />

s of CO <strong>an</strong>d hydrocarbons are relatively high, whereas the NO, concentration is<br />

low. The exhaust gases were oxidized in a converter <strong>to</strong> which air was supplied.<br />

Somewhat later the NO, st<strong>an</strong>dards tightened <strong>an</strong>d also the amount of NO had <strong>to</strong><br />

be reduced. So both oxidation <strong>an</strong>d reduction reactions were required. In the<br />

beginning, a so-called dual bed system with separate reduction <strong>an</strong>d oxidation<br />

catalysts was envisaged. The engine would be operated under fuel-rich condi-<br />

tions in the first bed; reduction would take place. After air injection in<strong>to</strong> the<br />

second bed, CO <strong>an</strong>d the hydrocarbons would be oxidized. The next generation of<br />

catalysts could catalyze all reactions simult<strong>an</strong>eously, provided the fuel-air ratio<br />

in the gas mixture was s<strong>to</strong>ichiometric. A typical example of the influence of the<br />

fuel-air ratio (lambda) is given in Fig. 1.6.<br />

0.8 -<br />

0.9 3 1 .o 1.07<br />

Lambda<br />

Fig. 1.6. The concentration of CO, NO, CH, <strong>an</strong>d 0 2 emitted by a gasoline engine as a function of<br />

h, the fuel-air ratio.

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