No description available.

No description available.

Abstract The research compares the efficiency of particle removal from exhaust of ritual money burning by an electrostatic precipitator (ESP) and a bag-house filter (BH), both have a capacity of around 30-35 Am3/min. A stainless steel chamber of 0.6 m in diameter and 1.0 m in height was used for the ritual money burning. Combustion gas from the chamber was cooled to 300-400oC by mixing with a certain proportion of ambient air and further cooled to around 100-130oC by a fin tube gas cooler before entering either to the ESP or the BH. Results indicate that TSP in the influent gas could be reduced from 6-392 (average 83) to 1-143 (average 22) mg/Nm3 by the ESP with gas velocities of 5-10 cm/s at 100-120 oC through the spacing between collecting plates. TSP emission factors of 0.0295-9.94 (average ¡Ó standard deviation = 1.81¡Ó2.25) and 0.031-3.36 (average ¡Ó standard deviation = 0.27¡Ó0.26) g/(kg combusted ritual money), respectively, were obtained before and after the ESP filtration. Although the ESP had an initial TSP removal of 80-99%, the performance dropped in a few operation hours because of a fouling of the plate surfaces by the collected fume dusts. Cleaning of the plate surfaces helped in the recovery of the performance, however, it dropped after a few cycles of collection and cleaning. Results from BH tests indicate that TSP in the influent gas to it could be reduced from 9-182 (average 72) to 0-12 (average 2.0) mg/Nm3 with the gas flow through the filter cloth with a velocity of 3.3 cm/s at 120-130 oC which resulted in an initial pressure drop of around 100 mmAq. It was observed that some fine dusts would escape from the cloth fiber spaces when the backwash pulse was operated. It is recommended that the backwash cycle should be minimized and trigged after the gas pressure drop over the cloth reaches up to 300 mmAq. TSP emission factors of 0.0176-1.64 (average ¡Ó standard deviation = 0.52¡Ó0.33) and 0-0.491 (average ¡Ó standard deviation = 0.02¡Ó0.05) g/(kg combusted ritual money), respectively, were obtained before and after the BH filtration. BH filtration is recommended for the TSP control in the ritual money buring. XRD(X-Ray Diffraction) examination of a bottom ash sample indicates that the ash has an elemental composition of O, Na, Al, and Si of 49.9, 11.8, 23.8, and 15.1%, respectively. SEM(Scanning Electron Microscope) analysis indicates that the collected fly ash and the bottom ash have particle sizes of 20-110 (mostly 45-60 nm) and 50-300 (average 250) nm, respectively.

No description available.

No description available.

O presente trabalho reúne elementos para projeto de precipitadores eletrostáticos, com dados levantados de cinzas volantes provenientes da combustão de gases em caldeiras de carvão mineral. Os objetivos desta pesquisa são construir um dispositivo padronizado para medição da resistividade ôhmica de materiais, levantar dados de resistividade ôhmica das cinza volantes de carvão mineral utilizado no Brasil e, com estes dados, listar recomendações sobre cuidados no dimensionamento de precipitadores (cálculo da área de captação), quando este equipamento é posicionado após uma caldeira que queima o carvão mineral nacional. A metodologia utilizada foi baseada em norma americana ASME, em que o pó (material a ser testado) é colocado sobre eletrodos de descarga e de coleta, uma alta tensão elétrica é aplicada até atingir a tensão de ruptura elétrica e neste instante é medida a resistividade. A construção do experimento e procedimento de execução foram seguidos conforme esta norma. O material de teste foi coletado de precipitadores eletrostáticos existentes na região Sul do Brasil, onde o carvão mineral tem seu uso freqüente. Os resultados apresentaram baixos valores para resistividade da cinza volante nacional, se comparados com resultados de carvões de outros países. Sua variação em função da temperatura segue a tendência de cinza volantes de outros países, ou seja, aumento da resistividade ôhmica com o aumento da temperatura. Foram realizados também experimentos com material retirado de precipitadores eletrostáticos acoplados a caldeiras de biomassa, que forneceram valores de resistividade ainda menores do que os do carvão mineral nacional. O material de teste, composição química e processo de coleta foram totalmente caracterizados, disponibilizados e uma análise completa pôde ser realizada, fato inédito no Brasil. Esses resultados permitiram listar recomendações visando o projeto de precipitadores eletrostáticos acoplados a caldeiras que queimam carvão mineral nacional. / This report is a collection of elements to be used in the design of Electrostatic Precipitators, with experimental data of fly ashes from combustion gases of Mineral Coal Fired Boilers. The aims of this research are to construct a standard device to measure the ohmic resistivity of materials, to get data of ohmic resistivity of fly ashes from mineral coals used in Brazil and with this data, to list recommendations about the key points to size electrostatic precipitators (calculation of specific collection area), when this equipment is arranged after one boiler that burns Brazilian mineral coals. The method used was based on the ASME Standard, in which the fly ash (material to be tested) is put between the discharge and the collecting electrodes, a high electrical tension is applied until the electrical break down tension to be reached; at this moment, the resistivity is measured. The construction of this device and the experimental procedure were conducted according to this standard. The tested materials were collected from existing Electrostatic Precipitator of South of Brazil, where the mineral coal is commonly used. The results indicated low values of ohmic resistivity of the Brazilian fly ashes, if compared to results of coals from other countries. Its variation with the temperature has the same behavior of fly ashes from other countries, i.e., the ohmic resistivity increases when the temperature increases. It was also executed tests with particulate materials from electrostatic precipitator of biomass boiler whose ohmic resistivity is lower than the Brazilian mineral coal. The tested material, chemical composition, and collecting process were totally described, available and a full analysis can be executed; these data are inedita in Brazil. These results allow to list the recommendations to design Electrostatic Precipitators for Brazil Mineral Coal Fired Boilers.

Traditional aerosol samplers are limited in their abilities to collect large quantities of particulate matter due to their low flow rates, high pressure drops, and are noise intrusiveness. The goal of this study was to develop an alternate aerosol sampler using electrostatic precipitation technology that was safe and not noise intrusive to be deployed in homes. The O-Ion B-1000 was selected as the most suitable electrostatic precipitator (ESP) for achieving the goal of this study because of its affordability, the design of its collection electrode and its high flow rate. The collection efficiency of the ESP was assessed for three aerosols; Arizona Road Dust (ARD), NaCl and diesel fumes. ARD was found to have the highest average collection efficiency (65%) followed by NaCl (43%) and lastly diesel fumes (41%). A method for recovering the particulate matter deposited on the collection electrode was developed. The dust collected on the electrode was recovered onto polyvinyl chloride (PVC) filters moistened with deionized water. Additionally, the recovery of the three test aerosols, ARD, NaCl, and diesel fumes, from the collection electrode was assessed. A gravimetric analysis was done to determine the amount of dust recovered. The collection efficiency was used to calculate the amount of mass expected on the filter for a particular aerosol. NaCl had the highest recovery at 95% recovery, followed by ARD (73%) and lastly diesel fumes (50%). Two identical ESPs were also deployed in an office and in a bedroom, 104.47 mg and 9.64 mg of particulate matter (PM) was recovered respectively. The noise and ozone level produced by the ESP was evaluated to determine the ESP’s viability as a household aerosol sampler. The ESP’s high setting had a noise level of 45.8 dB and ozone generation rate of 0.036 mg/min. The results of the calculation showed that in an averaged size unventilated room (6.10 m × 6.10 m × 2.44 m), it would take 6 hours and 53 minutes for the ozone levels to reach the recommended maximum exposure limits per National Ambient Air Quality Standards (NAAQS). Additionally, a ventilation of 230 L/min is needed in order to prevent the ozone levels generated by the ESP from exceeding maximum exposure limits per NAAQS. Overall, the O-Ion B-1000 met the criteria of collecting 1 mg of PM in a 24 hour sampling for ARD and NaCl. Diesel fumes however, required 30 hours to collect 1 mg of PM. The noise levels generated by the ESP set on high was one dB above the Environmental Protection Agency (EPA) standards for indoor noise limit. However, the noise is proportional to inverse distance squared; the ESP should not pose a problem during household deployment. Ozone generated by the ESP was also found to be below 0.07 ppm as set by the EPA with an average ventilation of 230 L/min. The average ventilation of a household is 1500 L/min, thus the ozone generated by the ESP would not surpass 0.07 ppm. However, the ESP should not be deployed in unventilated rooms for a period of more than 6 hours and 53 minutes.

Gaseous exhaust of different industries contains dust particles of different chemical precipitates that are harmful for the environment. Electrostatic Precipitators are very often used in industries to filter their gaseous exhaust and to prevent the atmosphere to being polluted. Electrostatic Precipitators are very efficient in their work. Electrostatic Precipitators use the force of the electric field to separate the dust particles from gaseous exhaust. Electrostatic Precipitators charge the dust particles and remove these particles by attracting these charged dust particles toward the collecting plates. The charging of dust particles requires a charging zone. When gas passes through that charging zone, the dust particles in the gas stream become charged and then these charged particles are attracted toward the collecting plates. The design of an Electrostatic Precipitators requires the knowledge of its working principle and the problems that often arise during its working. This thesis is the study of the working and the problems of the Electrostatic Precipitators. The main reason for problems in working of an Electrostatic Precipitator is the dust resistivity. This dust resistivity affects the collection performance of an Electrostatic Precipitator. This thesis also contains the simulation of an Electrostatic Precipitator. In the simulation part, the Electric Potential and the Electric Field of an ESP is modeled in an ideal condition, when no gas is flowing through the ESP. The industrial software Comsol Multiphysics is used for the simulation. A Comsol Multiphysics guide is given in appendix of this thesis report that provides information about using this software.

Norska pappersmassaindustrin Norske Skog Saugbrugs AS använder flera olika biobränslen i en bränslemix vid produktion av ånga för internt bruk. Biobränslen visar stora variationer i asksammansättning och producerad askmängd, varför syftet var att studera dessa i förhållande till bränslemixen, via en statistisk analys av Saugbrugs befintliga data. Rökgaserna från förbränningen renas med ett elektrofilter med tre avskiljningsfält för askstoftet, och en teori om fraktionering av aska från de olika fälten vad gäller innehåll av ekotoxiska metaller fanns. Provtagning, analys av partikelstorlek och laboratorieanalys av askstoft i rökgasen samt aska avskilt av de olika fälten i elektrofiltret var därför motiverat. Förbränningen som helhet alstrar stora mängder aska som sedan deponeras. En undersökning av alternativa användningsområden i enlighet med myndighetskrav för aska gjordes baserat på resultaten från den statistiska analysen och de fyra provuttagningarna. Att statistiskt sammanföra bränslena i en varierande bränslemix med asksammansättning gav litet resultat, men bekräftade att stora variationer finns. Askmängden varierade till följd av vilka bränslen som eldades, snarare än mängden bränsle. Det ackrediterade laboratoriet hade använt sig av två olika analysmetoder vars resultat visade olika koncentrationer för vissa ämnen. Multivariat dataanalys tyder på att koncentrationerna var likvärdiga mellan den gamla och den nya metoden, därmed berodde koncentrationsförändringen inte på Saugbrugs förbränning eller bränslemix. Den befintliga askan innehåller höga koncentrationer av arsenik, bly och krom, och är inte direkt lämplig för alternativ användning. Innehållet av ekotoxiska metaller beror troligtvis främst på förbränning av RT-flis, men till viss del även slam och eget avfall. Mikroskopisk analys av askproven visar att partikelstorleken minskar ju längre in i rökgasreningen askstoftet kommer, och kemisk analys visar en tydlig fraktionering mellan de olika fälten där halten ekotoxiska metaller ökar med minskande partikelstorlek. Askan i de två sista fälten innehåller kritiska koncentrationer av ekotoxiska metaller. Askan uppfyller därmed inte myndighetskrav för skogsspridning eller liknande, och särskilt arsenikkoncentrationen är mycket hög. Saugbrugs aska måste fraktioneras eller behandlas om den skall användas. Fraktionering av aska för olika ändamål kan vara möjligt, men variationer kan förekomma och bör beaktas. Lämpligast vid alternativ användning är att späda askan eller en askfraktion med en annan aska, eller kalk. / The Norwegian paper pulp industry Norske Skog Saugbrugs AS combusts a variety of biofuels in a fuel mix, producing steam for internal use. Biomass is often associated with large variations in ash composition and produced ash quantity, thus the aim was to study these in relation to the used fuel mix through a statistical analysis of Saugbrugs existing data. Flue gases from the combustion are purified with an electrostatic precipitator (ESP), which consists of three fields for ash trapping. Other studies have shown that fractionation of ash from the different fields regarding the content of ecotoxical metals is possible; therefore the study also included sampling, particle size analysis and chemical analysis of samples from ash in the flue gas and ash from the three fields in the ESP respectively. The combustion produces large amounts of ash which is landfilled. An investigation of alternative uses in accordance with regulations for ash was made based on results from the statistical analysis and the four ash samples. The statistical analysis of the fuel mix in relation to the ash composition yielded little results, but showed that large variations exist. The produced ash quantity also varied due to the type of fuel used, rather than how much fuel is combusted. The existing data was based on different analytical methods at the accredited laboratory resulting in different substance concentrations. With multivariate analysis it was concluded that the different concentrations are equivalent between the old and the new method, thus the change is not due to Saugbrugs combustion or fuel mix. The ash contains high concentrations of arsenic, lead and chrome, and is not directly suitable for alternative use. The content of ecotoxic metals in the ash is mainly due to combustion of demolition wood, but also to sludge and waste in some extent. Analysis of the samples show that particle size decreases as the ash moves further in the flue gas purification process, and a distinct fractionation between the different fields where the content of ecotoxic metals increase with decreasing particle size. The ash collected in the two last fields therefore contains critical concentrations of ecotoxic metals. The ash does not meet the requirements regarding forest spreading or similar, and the concentration of arsenic is particularly high. Saugbrugs ash must be fractionated or treated if it is to be used alternatively. Fractionation of ash for various purposes might be possible, although variations may occur and must be considered. The most suitable approach is to dilute the ash or ash fraction with another ash, or lime.

A dust layer, especially based on high-resistivity dust, at the collecting electrodes may cause a back corona discharge in electrostatic precipitators (ESP). It can significantly reduce the ESP efficiency and as a result cause ecological damages. To study the dust layer influence inside ESPs, it is necessary to derive an adequate model of the ESP precipitation process with a dust layer at the collecting electrode. The research of the present thesis is focused on stationary studies of the precipitation process with a dust layer at the collecting electrode in ESPs. Three mathematical models are proposed as a description of the precipitation process with a dust layer at the collecting electrode. The models are based on Maxwell’s equations and the finite element method (FEM). COMSOL Multiphysics software is used for their implementation. In all models the dust layer has constant conductivity and the air region has constant ion mobility. In the first model there are no coupling conditions, which is required in mathematics, are given between the two regions. The solution found by COMSOL Multiphysics does not provide physically acceptable coupling conditions. In the second model, a continuous transition zone is introduced between the two regions so that no coupling conditions are required. With the large derivatives in the transition zone, the nonlinear solver in COMSOL Multiphysics does not converge. Finally, in the third model, the dust layer and the grounded collecting electrode are replaced with a boundary condition for the air region. The properties of the third model are investigated, and these models can be used to study the influence of the dust layer. The results of these investigations are reported and discussed.