James A. Jahnke

Continuous Emission Monitoring


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the greater will be the losses of SO2 in gas coolers. To certify a CEM system in a RATA, comparing data with a source tester’s reference system operating under a different set of variables could lead to a failed certification, or where bias correction factors are required, inaccurate bias adjustments. At low SO2 concentrations, it is recommended that instead of installing a source‐level extractive system with a gas cooler, a hot/wet extractive system, a dilution‐extractive system, or a source‐level extractive system, using a Nafion dryer, be considered for the application.

      As a last resort in source‐level extractive systems using chillers, SO2 absorption can be decreased by increasing the acidity of the condensate. One technique has been to acidify the gas stream with an unmonitored acid (such as HCl) to reduce SO2 solubility during condensation (DeFriez 1992; Williams 1992).

       Miscellaneous Drying Techniques.

      Other drying techniques have been used or attempted in extractive monitoring systems. Cyclone‐type devices installed in or near the probe, coalescing filters, “knock‐out jars,” and other engineering afterthoughts are sometimes encountered.

      The use of chemical desiccants (such as calcium chloride, CaCl2; concentrated sulfuric acid, H2SO4; calcium sulfate, CaSO4) to remove moisture is not common in CEM systems. Because desiccants have to be periodically regenerated or replaced, they are considered to present an unnecessary maintenance task. Also, to justify their use, it must be shown that the gases being measured do not react with, adsorb onto, or absorb into the material.

      In cases where acid gas formation, such as SO3, might occur, a “freezer” chiller designed to achieve a dew point of −25 °C can be used to reduce moisture levels to less than 650 ppm and minimize the loss of SO2 by acid formation.

      Sample Pumps

      The sample pump is an important element of the extractive system and is used to transport the sample from the stack to the analyzer. A pump should be sized appropriately to meet the demands of gas analyzers and be designed so that no air in‐leakage occurs (i.e. around a rotary shaft seal) and that no contamination is introduced from pump lubricating oils. Two types of pumps meeting these criteria are (i) diaphragm and (ii) ejector pumps. These pumps are commonly used in source monitoring applications.

Schematic illustration of a diaphragm pump.

      Diaphragm pumps can be used before the sample gas conditioning system and can even be operated hot. However, particulate matter and condensed acid can weaken the pump head by particle abrasion or chemical attack. Unless the gas is properly filtered and the pump head adequately heated, it is better to locate the pump after the conditioning system. Eventually, the continual, rapid flexing action of the pump will cause the diaphragm to split or tear.

      The flow rate of a diaphragm pump can be controlled by placing a throttle valve in the line on the discharge side of the pump or by installing a by‐pass line and valve from the suction side to the discharge side. If the pump is operating at less than its full capacity, controlling flow with the throttle valve will cause the pump to work against a high discharge pressure and pump life will be reduced. For this reason, it is better to control the flow using a bypass valve.

Schematic illustration of the ejector pump or eductor.

      Fine Filters

      The coarse filter is used to remove larger particles from the sample gas. Because the majority of gas analyzers require almost complete removal of particles larger than 0.5 μm, additional filtration is necessary. This is accomplished by incorporating a fine filter before the analyzer inlet. The location of the fine filter is an important consideration in the CEM system design and is dependent upon the susceptibility of the other system components to the effects of fine particles. There are two types of fine filters: (i) surface filters and (ii) depth filters.

      A surface filter can be simply a filter paper that excludes particles of a certain size. The filter material is porous to the moving gas, but the pores are of such a size that they prevent penetration of fine particulate matter. A filter cake can also build up on the filter, further reducing the size of particles passing into the gas stream. Because of the filter cake and developed electrostatic charges, surface filters can remove particles smaller than the actual filter pore size.

      Depth filters collect particles within the bulk of a filter material. The filter may consist of loosely packed fibers of quartz wool or of filter material wrapped to a depth sufficient to remove fine particles. Such filters work particularly well for dry solids and moist gas streams containing aerosols. A depth filter can also be used as a probe filter, a technique that is used in some systems.

      Assembling a Cool/Dry Extractive System

      Designing and assembling a cool/dry extractive system is a relatively straightforward process. System components, such as probes, chillers, filters, and pumps are available from many suppliers and can be purchased individually to incorporate into a system design. Alternatively, several suppliers provide modular conditioning systems and modular calibration gas distribution systems that simplify the assembly. An example of a plumbing system for a cool‐dry extractive system is shown in Figure 3‐15.