31 research outputs found

    Mechanism and Kinetics of Lead Capture by Kaolinite in a Downflow Combustor

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    An 18 kW, 6 m long, gas-fired downflow combustor was used to examine the postflame reaction between lead vapor and kaolinite. Since the focus of this work was to evaluate the reaction with lead vapor, samples were extracted at a temperature above the metal dew point. The sample was rapidly diluted with nitrogen such that lead vapor homogeneously nucleated to form small particles in the presence of a pre-existing particle population. These small lead particles were easily distinguished from lead reacted to large sorbent particles; hence, multicomponent particle size distributions were used to determine the extent of lead capture. A parametric study was conducted in which sorbent/metal molar ratio and sorbent injection temperature were controlled. Temperatures and residence times were varied by changing the sorbent injection point in the combustor, which had the approximate time and temperature profile of practicalscale units. The effect of chlorine was evaluated by doping chlorine gas into the flame. Results show that lead capture by kaolinite was reduced at higher temperatures and in the presence of chlorine. A two-reaction mechanism is proposed to model the apparent temperature inhibition. In the primary capture reaction, lead oxide reacts with activated kaolinite and forms a lead aluminosilicate product. Subsequently, a reaction between this product and activated kaolinite acts to inhibit further lead capture. First-order rate expressions are proposed for each reaction, and kinetic parameters are estimated from experimental results. The primary capture reaction appears to have an activation energy that is approximately zero. The inhibition reaction has an activation energy of Ļ³10 2 kJ mol ā€«1מā€¬ . To model the effect of chlorine, the reaction scheme is modified to account for the partitioning of lead between lead oxide and lead chloride. Based on experimental results, the concentration of lead chloride vapor in the system is significantly higher than predicted by equilibrium calculations. Introduction The emission of toxic elements from stationary combustion sources, such as incinerators and coalfired boilers, is a major concern. Of particular concern are semivolatile toxic elements, for example, lead and cadmium, which vaporize and condense within the combustion system. At high temperatures, lead vaporizes and is liberated from ash particles. As the temperature of the combustor decreases, the vapor condenses to form, in part, submicron particles. These submicron particles can penetrate conventional air pollution control systems, like baghouses and electrostatic precipitators, and be emitted to the environment One potential method to control toxic metal emissions is to inject a high-temperature sorbent into the postflame region. The sorbent powder, which is easily collected, reacts with metal vapors and prevents the subsequent vapor-to-particle transformation processes that form submicron particles. Previous researchers have examined the reaction of lead and a clay-based sorbent, kaolinite. In a series of benchtop experiments where large kaolinite flakes were exposed to lead chloride vapor, Uberoi and co-author

    Oxy-coal combustion for retrofit: challenges and opportunities

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    This paper is concerned with Oxy-Fuel Combustion, a process for the control of carbon dioxide from a range of solid fuel combustion processes. The focus is on the applicability of this technology for retrofit and hence on entrained flow combustors rather than on circulating fluidized bed systems. First, the importance of retrofit technology for CO2 control from coal fired units in the US is outlined. The current state of the technology (applied mainly to pulverized coal combustors), and critical research needs are identified. There are three over-arching issues that must be resolved in order for oxy-coal retrofit to be attractive: the first is related to the O2 supply energy penalty since current cryogenic technology can consume 15-20% of energy produced; the second is related to the purity of CO2 in the flue gas for sequestration; and the third is related to air ingress through leaks that are present in most existing systems. Resolution of these over-arching issues requires efforts by industrial gas engineers, politicians, and combustion engineers, respectively. One objective of current research in oxy-coal combustion for retrofit is to create enabling technology to be used for: 1) extrapolation of boiler performance from conventional air firing to oxygen firing with sufficiently large amounts of flue gas recycle to match heat transfer to existing heat exchange surfaces. 2) extrapolation to substantially modified existing units that "still look like boilers" but that optimize and reduce the amount of flue gas to be recycled and therefore may require some relocation of heat transfer surfaces. This enabling technology will be comprised of simulations employing validated heat transfer sub-models (radiant and convection zones), and validated chemistry sub-models (coal jet ignition, chemistry, char burnout, ash partitioning, trace metals, and combustion by-products - NOx, SOx, Hg), where validation must be under oxy-fuel combustion conditions, with varying amounts and compositions of flue gas recycle streams. Recent research results in each of these areas are presente

    Oxy-coal combustion for retrofit: challenges and opportunities

    No full text
    reportThis paper is concerned with Oxy-Fuel Combustion, a process for the control of carbon dioxide from a range of solid fuel combustion processes. The focus is on the applicability of this technology for retrofit and hence on entrained flow combustors rather than on circulating fluidized bed systems. First, the importance of retrofit technology for CO2 control from coal fired units in the US is outlined. The current state of the technology (applied mainly to pulverized coal combustors), and critical research needs are identified. There are three over-arching issues that must be resolved in order for oxy-coal retrofit to be attractive: the first is related to the O2 supply energy penalty since current cryogenic technology can consume 15-20% of energy produced; the second is related to the purity of CO2 in the flue gas for sequestration; and the third is related to air ingress through leaks that are present in most existing systems. Resolution of these over-arching issues requires efforts by industrial gas engineers, politicians, and combustion engineers, respectively. One objective of current research in oxy-coal combustion for retrofit is to create enabling technology to be used for: 1) extrapolation of boiler performance from conventional air firing to oxygen firing with sufficiently large amounts of flue gas recycle to match heat transfer to existing heat exchange surfaces. 2) extrapolation to substantially modified existing units that "still look like boilers" but that optimize and reduce the amount of flue gas to be recycled and therefore may require some relocation of heat transfer surfaces. This enabling technology will be comprised of simulations employing validated heat transfer sub-models (radiant and convection zones), and validated chemistry sub-models (coal jet ignition, chemistry, char burnout, ash partitioning, trace metals, and combustion by-products - NOx, SOx, Hg), where validation must be under oxy-fuel combustion conditions, with varying amounts and compositions of flue gas recycle streams. Recent research results in each of these areas are presente

    Chemical and environmental engineering or ā€œTo go where the puck is going to beā€

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    Measurement of Liquid-Phase Diffusivities

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