ASHRAE LO-09-082-2009 Laboratory Evaluation and Modeling of Electrostatic Precipitation of PM Emissions from Poultry Buildings《家禽建筑PM放射静电沉淀的实验室评估和建模》.pdf
《ASHRAE LO-09-082-2009 Laboratory Evaluation and Modeling of Electrostatic Precipitation of PM Emissions from Poultry Buildings《家禽建筑PM放射静电沉淀的实验室评估和建模》.pdf》由会员分享,可在线阅读,更多相关《ASHRAE LO-09-082-2009 Laboratory Evaluation and Modeling of Electrostatic Precipitation of PM Emissions from Poultry Buildings《家禽建筑PM放射静电沉淀的实验室评估和建模》.pdf(19页珍藏版)》请在麦多课文档分享上搜索。
1、2009 ASHRAE 831ABSTRACT Particulate matter (PM) emissions from the poultry industry are a major pollution concern. Development of an effective PM mitigation technology is urgently needed. In this study, the potential of an electrostatic precipitator (ESP) for collecting PM emissions from poultry fac
2、ilities was evaluated using a commercial ESP unit under simulated laboratory conditions. The effects of operating parameters such as char-ger voltage, superficial air velocity and PM concentration on the performance of a two-stage plate ESP were evaluated. An empirical model for predicting ESP perfo
3、rmance was devel-oped. Preliminary factor screening analyses have shown that charger voltage (7 kV to 10 kV) and superficial air velocity 1 m/s (200 ft/min) to 5 m/s (1000 ft/min) affect ESP perfor-mance significantly while PM concentration (2.5 mg/m3to 5 mg/m3) had negligible effect (=0.05). The ES
4、P collection efficiency increased with voltage and decreased with velocity. The relationship between charger voltage and superficial air velocity and PM collection efficiency for particles within size ranges of 0.3-0.5, 0.5-1, 1-5, 5-10, 10-25, 25 , PM1, PM5, and PM10were apparently nonlinear. The E
5、SP performance approached a peak point at 9 kV charger voltage and 1 m/s air velocity. The optimized operating condition to be used at an actual farm would depend on the desired degree of PM collec-tion. To collect at least 90% of all particles, the operating conditions were 9 kV and 2.5 m s-1. The
6、power consumption of the ESP to collect 90% of the total particles is 90 watts/m2(29 BTU/h/ft2) of duct cross-sectional area. The ESP unit produced very negligible amount of ozone (5kV), industrial ESP power requirement is very minimal (16 watt m-2 5.1 BTU h-1ft-2 of treated duct cross-section, Vata
7、vuk, 1984) since the electric current consumed to charge and collect PM is very low (25 m with a Table 1. Screening Factorial Design for the ESP Operating ConditionsTreatmentVoltage (kV)Velocity ms-1(ftmin-1)PM Loadmgm-3(gr ft-3)A 7 1.25 (246) 2.5 (0.0011)B 7 1.25 (246) 5 (0.0022)C 7 2.5 (490) 2.5 (
8、0.0011)D 7 2.5 (490) 5 (.00022)E 10 1.25 (246) 2.5 (0.0011)F 10 1.25 (246) 5 (0.0022)G 10 2.5 (490) 2.5 (0.0011)H 10 2.5 (490) 5 (0.0022)Table 2. Full Factorial Design for the E-v Response CurveTreatmentVoltage (kV)Velocity ms-1(ft min-1)A 7 1 (200)B 8.5 1 (200)C 10 1 (200)D 7 3 (600)E 8.5 3 (600)F
9、10 3 (600)G 7 5 (1000)H 8.5 5 (1000)I 10 5 (1000)ASHRAE Transactions 835counting limit of 3.3 x 107particles m-3(9.3 x 10-5 particles ft-3). Sampling was performed using iso-kinetic sampling heads for accurate PM measurement. TSP PM mass concentration measurements were conducted at 1.25 and 2.5 m s-
10、1 (246 and 492 ft min-1) to calibrate the rotational speed of the dust feeder to generate 2.5, and 5 mg m-3 (0.0011 and 0.0022 gr ft-3). The temperature and relative humidity readings of the instrument were calibrated and used for all the measurements. Data AnalysisEfficiency Calculations. The perfo
11、rmance of the ESP is determined by particle collection efficiency measured at six particle size ranges (25 m) using the formula:(4)where= the particle collection efficiency at the ith range,COi= the outlet particle concentration at the ith range number m-3(number ft-3),CIi= the inlet particle concen
12、tration at the ith range number of particles m-3(number ft-3), andPi= particle penetration at the ith range.The average collection efficiency of classified ranges which includes PM1, PM5, PM10and the total particles measured were calculated (PMis mean particles whose aero-dynamic diameters are 25 m,
13、 PM1, PM5, PM10, and total particle size ranges are shown in table 4. Results indi-cated that voltage was highly correlated with the measured Table 3. Specifications of the Module Two-Stage Electrostatic PrecipitatorDimensions (W x H) in mm (in.) 400 x 640 (16 x 25)Weight in kg (lb) 2.26 (4.98)Numbe
14、r of Plates 71Number of Ionizers 9Design Ionizer Voltage in Vdc 8150Design Collector Voltage in Vdc 4075Pressure Drop at 680 m3h-1in Pa (in H20) 12.5 (0.05)Plate Width in mm (in.) 76 (3)Collector plate Spacing in mm (in.) 3.6 (0.14)Charger plate to wire spacing in mm (in.) 15 (0.59)i1COiCIi- 1 Pi=ii
15、 AVE,iCiiCii- 1 Pi AVE,=i AVE,PiAVE,i1 b0expEn1vn2- b1En3vn4=836 ASHRAE TransactionsFigure 3 Schematic diagram of the ESP laboratory evaluation set-up.ASHRAE Transactions 837collection efficiencies, with correlation coefficients ranging from 0.46 to 0.89. Air velocity showed higher correlation only
16、for collection efficiencies of particles greater than 5 m, with correlation coefficients ranging from -0.62 to -0.57. PM concentration, temperature and relative humidity all showed very weak correlations with collection efficiency with corre-lation coefficients ranging from -0.15 to 0.15 for PM conc
17、en-tration, -0.09 to 0.13 for temperature, and -0.27 to -0.08 for humidity, respectively.Results suggest that collection efficiency tend to increase with voltage and decrease with velocity as indicated by the positive and negative correlation coefficients computed for each respective factor. The tre
18、nd also agreed with the analysis of the parameters made in equation 3. In addition, the logical explanation for the observations mentioned is that increasing charger voltage increases the rate of ion generation which facilitates particle charging while increasing air velocity decreases retention tim
19、e and increases particle re-entrainment.The relatively high correlation coefficients between volt-age and collection efficiency also suggests that operating volt-age had strong influence on collection efficiency. However, the correlation coefficient between air velocity and collection efficiency inc
20、reased between 0.5 m to 10 m only while equation 3 predicts that increasing particle diameter should lead to an increase in effect. Oglesby and Nichols (1978) explains that deviations such as these are caused by PM re-entrainment which has stronger influence as particle size is increased. This obser
21、vation was not in agreement with the predictions of equation 3 since it did not account for the effect of reentrainment.The effects of environmental factors like PM load, temperature, and humidity (not directly implied in equation 3) were also evaluated. Results showed that the initial perfor-mance
22、of the ESP was not affected by PM loads ranging 2.5 to 5 mg m-3(0.0011 to 0.0022 gr ft-3), inside the air conditioned room whose temperature varied from 24oC to 27oC (75 to 81 oF), and relative humidity varied 18% to 62%. However, the wider range of temperature and humidity variations typically enco
23、untered in poultry houses may have an effect on ESP performance as suggested by Salam (1992). In the study, vari-ations in temperature and humidity were minimized to a degree which did not affect ESP performance.Effects of Voltage and Superficial Air VelocityFigure 4 shows the contour plots of the m
24、easured ESP collection efficiencies for particles sized 0.3 m-0.5 m, 0.5 m-1 m, 1 m-5 m, 5 m-10 m, 10 m-25 m, 25 m. In general, the plots confirmed observations obtained during the screening tests that collection efficiency increased with volt-age while it decreased with velocity. However, these act
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