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Application Note Wet Flue Gas Desulfurization Scrubbers Power: Environmental

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Application Note Wet Flue Gas Desulfurization Scrubbers Power: Environmental Application Note Wet Flue Gas Desulfurization Scrubbers Power: Environmental Coal fi red power plant emissions are a global concern. collects in the bottom of the absorber. A paste-like calcium The burning of coal produces sulfur dioxide (SO2). When sulfi te (CaSO3) sludge forms in the liquid. CaCO3 can be released into the atmosphere SO2 combines with water very diffi cult to remove if it settles out at the bottom of the to form sulfuric acid (H2SO4). Coal fi red power plants will absorber. More recent scrubber designs will blow outside use a fl ue gas desulfurization (FGD) scrubber to remove air through liquid to convert the sulfi te to sulfate in the the SO2 before release up the stack. The scrubbing following reaction. process is pH dependent. In this paper we will explore some of the challenges in this type of pH measurement. CaSO3 + H2O + 1/2O2 ► CaSO4 + H2O The FGD scrubber uses chemical reagents sprayed into The addition of air is referred to as forced oxidation. The the fl ue gas to react with the SO2. Many different reagents resulting calcium sulfate (CaCO4) crystallizes in the liquid have been used over the years. Examples include and is easily removed through fi ltration. An added benefi t ammonia, caustic, lime, limestone, and sodium carbonate. from the process is that CaCO4 (known as gypsum) can Due to cost, the most common reagents are Lime (CaO) be sold as additive for wallboard and cement production. and Limestone (CaCO3). Since both chemicals are very similar we will limit the scope of this paper to them. Both As the fl ue gas continues through the scrubber it will pass materials are solids thus they are mixed with water to form through mist eliminators to further remove any entrained a slurry. The chemistry is as follows: liquid. The fi nal fl ue gas may still contain some trace sulfur compounds. It will be reheated to avoid corrosion prior to Lime: CaO + 2H2O + SO2 ► CaSO3 + 2H2O entering the stack for release into the environment. Limestone: CaCO3 + 2H2O + SO2 ► CaSO3 + 2H2O + CO2 Measurement challenges Downstream from the boiler the flue gas passes through FGD scrubbers have multiple variables that can effect their an electrostatic precipitator (ESP). The ESP removes effi ciency. These include: fly ash so it does not pass into the atmosphere. Quench water cools the flue gas at the entrance of the scrubber. • fl ue gas fl ow rate • coal moisture • changing coal supplies • chloride content Quenching reduces evaporation losses thus lowering • coal sulfur content • fl y ash content chemical usage. Inside the scrubber spray nozzles mist the lime slurry down on the fl ue gas. This section is The pH of the slurry in the absorber is one of the main referred to as the absorber. The slurry and quench water control parameters of the scrubber. It is typically kept in a Flue Gas Desulfurization Process Flue Gas Exit Mist Eliminators Flue Gas Stack Lime / Limstone Reheater Slurry Storage Absorber Quench Water Flue Gas Inlet ESP Flue Gas From Boiler 547 pH Sensor Forced Air Blower CaCO4 Slurry to Waste or Filtration Figure 1 Application Note Wet Flue Gas Desulfurization Scrubbers range of 5.7 to 6.8pH. If the slurry drops below 5pH Historically, scrubber pH measurements have been then the scrubber will not effi ciently remove SO2 from made on sample lines. While this simplifi es cleaning the fl ue gas. If the pH gets above 7.5pH then CaCO3 / and calibration of the sensor it may not provide the best CaCO4 scale can begin to plug nozzles, mist eliminators, response time for adequate pH control. Over time the and other hardware. In addition to build-up problems, slurry can plug up sample lines causing maintenance maintaining high pH increases reagent chemical usage issues. Barben Analytical recommends mounting the resulting in additional wear on pumps and valves plus pH sensor directly on the recirculation piping using a increased chemical cost. retractable sensor such as the 547 or 567 “Hot Tap” sensor. Installation in the recirculation piping improves The slurry in the bottom of the scrubber is typically 5-15% speed of response while the slurry fl ow rate helps keep solids. It is continuously recirculated to through the spray build-up from forming on the electrode tip. Material of nozzles to use up the residual lime compounds. Solids construction should be either Hastelloy or Kynar to best concentration is controlled by bleeding off the bottom of deal with the corrosive nature of the process. Barben the absorber to either waste or gypsum production. sensors should be specifi ed with “CR” Coat Resistant high temperature glass electrodes. pH Measurement Solutions pH measurement can be diffi cult in these applications. Barben pH sensors will easily connect to most modern Problems include: pH analyzers in use today, Wiring diagrams for commonly available instruments can be found on www. • High sulfi des that attack the sensor BarbenAnalytical.com or via request from technical • Heavy metals that attack the sensor support. • Abrasion and coating due to particulates • Elevated temperatures shorten sensor life 547 Retractable “Hot Tap” Sensors 1-1/4” OR 1-1/2“ Barben Performance Series pH sensors with Axial Ion FULL PORT BALL VALVE Path® reference technology help to overcome the issues listed above. The internal fi ltering junction prevents PIPE NIPPLE ® chemical ingress into the sensor while the Axial Ion Path 547 PH SENSOR seals ensure that the measurement signal is maintained. SENSOR Barben sensors are rate up to 130°C (266°F) so they can TIP easily handle the slurry temperatures. Figure 3 Figure 2 Multiple Axial Ion Paths Plug free communication Seal individual fi ltering chambers Annular Filtering Junction Maintains measurement signal Wood slows process ingress Highly resistant to strong chemicals Tefl on Junction Interface Initial protection against process + Large surface area + H H+ H H+ H+ H+ H+ H+ ION PATH® Barben Analytical reserves the right to make technical changes or modify the contents of this document without prior notice. We reserve all rights in this document and in the subject matter and illustrations contained within. Kynar® is a registered trademark of Elf Atochem North America Inc. Hastelloy® is a registered trademark of Haynes Intl Inc. © 2015, by AMETEK, Inc. All rights reserved • FGD_Scrubber_AN_RevA • August, 2015 USA • BELGIUM • CHINA • SINGAPORE Toll Free +1(800)993-9309 • Phone +1(775)883-2500 • Fax +1(775)297-4740 ales. @ metek.com • www.BarbenAnalytical.com ISO 9001:2008 S Barben A Cert. No. 43271.
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