Page 474 - Air Pollution Control Engineering
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                    total pollution control system. Because the implementation of a single control technology
                    may not in itself be adequate and may even directly cause other emission problems, it
                    is often desirable to consider combinations of several different control techniques so
                    that the final system selected is optimized from both economic and environmental
                    considerations.

                    2. PROCESS MODIFICATION
                       Process modification should be utilized as the first and last steps when planning to
                    control air pollution emissions. In most processes, there are many ways to obtain the
                    desired end product. One or more of these alternatives may eliminate or, at least, reduce
                    the emission of pollutants. Combustion operations are perhaps the best known in this
                    regard. Boilers have been redesigned to reduce nitrogen oxide (NO ) emissions by
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                    permitting the use of recirculated air, reducing hot zones, and eliminating flue gas
                    quenching. Automobile engines are good examples in which redesign to eliminate cold
                    spots and to recirculate vapors has reduced hydrocarbon (HC) emissions, and changes
                    in timing, electronic charge distribution, and air-to-fuel ratios have improved fuel econ-
                    omy while reducing emissions. Furthermore, an automobile engine using the advanced
                    fuel-cell technology is being developed in the United States for emission reduction.
                       High-efficiency control devices may need to be installed to meet regulations if pro-
                    cess alterations do not result in an adequate reduction of pollution quantities. However,
                    process improvements can change the character of the emissions to make their control
                    easier. An ideal control device would close the process loop and return valuable prod-
                    uct to the system. In these situations, it may be necessary to modify the process system
                    so that it can successfully accept the returned material.
                       Combustion processes are examples of systems that can be modified to produce
                    fewer pollutants (e.g., NO and HC), to accept return of recovered pollutants (e.g., HC),
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                    and to eliminate formation of pollutants. Elimination of fly ash and SO can be accom-
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                    plished, for example, by conversion from solid fuel (coal) to gaseous fuel (natural gas,
                    which is methane, or compressed natural gas [CNG], which is propane). This, however,
                    simply relocates the pollution control facilities because adequate gaseous fuels currently
                    are not available, although they could be in the future if produced from coal, solid waste,
                    or some other abundant raw material. Air pollution control would then be required at
                    these conversion facilities. Liquefaction of these raw materials can also produce a low-
                    pollution fuel, but the same constraint applies (i.e., air pollution control facilities will
                    be required at the conversion site).

                    3. VEHICLE AIR POLLUTION AND ITS CONTROL

                    3.1. Background
                       Transportation vehicles in the United States have been the single largest source of air
                    pollution emissions. In 1972, it was estimated that nearly 104 million tons of trans-
                    portation source pollutants were released, which amounted to 48.7 weight percent
                    (wt%) of total air pollution emissions. For the same year, the emission concentration of
                    the various transportation-source pollutants by weight percent was 74.5% carbon
                    monoxide (CO), 15.6% hydrocarbons (HCs), 8.4% nitrogen oxides (NO ), 0.8% partic-
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