- Page 1 and 2: Stationary Source Control Technique
- Page 3: CONTENTS TABLES ...................
- Page 7 and 8: CONTENTS (continued) 5.4.5.1 Capita
- Page 9 and 10: TABLES Table 2-1 Summary of Trends
- Page 11 and 12: FIGURES Figure 2-1 PM 2.5 Compositi
- Page 13 and 14: FIGURES (continued) Figure 5.4-2 Sc
- Page 15 and 16: SECTIONS 1 and 2 1. INTRODUCTION ..
- Page 17 and 18: programs, and major current sources
- Page 19 and 20: 2. BACKGROUND National ambient air
- Page 21 and 22: 2-3
- Page 23 and 24: 2.3 SOURCES OF PM 10 AND PM 2.5 EMI
- Page 25 and 26: 2-7
- Page 27 and 28: 2-9
- Page 29 and 30: 2.5 REFERENCES FOR SECTION 2 1. Rev
- Page 31 and 32: 3 MEASUREMENT The determination of
- Page 33 and 34: description of these methods, the E
- Page 35 and 36: Figure 3-1. EPA Test Method 5 Sampl
- Page 37 and 38: C Method 5E: Determination of PM Em
- Page 39 and 40: dissolved sulfur dioxide gases from
- Page 41 and 42: long time while others have been de
- Page 43 and 44: C Portable Wind Tunnel Method. This
- Page 45 and 46: particles either above and below a
- Page 47 and 48: provide this type of analysis. 64,6
- Page 49 and 50: 3.6.3 Spectrometry Spectrometry is
- Page 51 and 52: Methods for estimating the total ma
- Page 53 and 54: Waste Management Association, Pitts
- Page 55 and 56:
33. Pilat, M.J. D. S. Ensor, and J.
- Page 57 and 58:
57. Cushing, K.M., R.R. Wilson, W.E
- Page 59 and 60:
78. Snell, F.D. Photometric and Flu
- Page 61 and 62:
SECTION 4 4. FUEL SUBSTITUTION AND
- Page 63 and 64:
Table 4.1. Potential PM 10 Emission
- Page 65 and 66:
4.1.3 Costs The costs associated wi
- Page 67 and 68:
4.2 Process Modification/Optimizati
- Page 69 and 70:
a fluidized bed of alumina particle
- Page 71 and 72:
5. EXHAUST GAS CLEANING SYSTEMS FOR
- Page 73 and 74:
5.1 PRETREATMENT The performance of
- Page 75 and 76:
5.1-3
- Page 77 and 78:
5.1-5
- Page 79 and 80:
5.1-7
- Page 81 and 82:
5.1-9
- Page 83 and 84:
Table 5.1-1 Characteristics of Comm
- Page 85 and 86:
A multiple cyclone, shown in Figure
- Page 87 and 88:
Fractional Collection Efficiency (%
- Page 89 and 90:
Fractional Collection Efficiency (%
- Page 91 and 92:
where d 50 is the diameter of parti
- Page 93 and 94:
Cumulative Collection Efficiency (%
- Page 95 and 96:
5.1.4 Costs of Precollectors The co
- Page 97 and 98:
Total Capital Investment ($ x 10 )
- Page 99 and 100:
Table 5.1-3. Annual Cost Factors fo
- Page 101 and 102:
C Increase sparkover voltage of flu
- Page 103 and 104:
unconditioned ash. Ammonia conditio
- Page 105 and 106:
Costs of flue gas conditioning vary
- Page 107 and 108:
5.1.9 References for Section 5.1 1.
- Page 109 and 110:
5.2 ELECTROSTATIC PRECIPITATORS ...
- Page 111 and 112:
5.2-2
- Page 113 and 114:
5.2.1.3 Particle Charging Particle
- Page 115 and 116:
Dust reentrainment associated with
- Page 117 and 118:
In a wire-pipe ESP, a wire that fun
- Page 119 and 120:
5.2-10
- Page 121 and 122:
5.2-12
- Page 123 and 124:
5.2-14
- Page 125 and 126:
Pulses can be used alone or in addi
- Page 127 and 128:
5.2-18
- Page 129 and 130:
5.2-20
- Page 131 and 132:
For coal fly ash, surface resistanc
- Page 133 and 134:
5.2-24
- Page 135 and 136:
Utility Boilers (Coal, Oil) Table 5
- Page 137 and 138:
5.2.6 Costs of Electrostatic Precip
- Page 139 and 140:
Table 5.2-3. Capital Cost Factors f
- Page 141 and 142:
Total Capital Investment ($ x 10 )
- Page 143 and 144:
where Q l is the liquid flow rate (
- Page 145 and 146:
Direct Costs Labor Table 5.2-5. Ann
- Page 147 and 148:
5.2.8 References for Section 5.2 1.
- Page 149 and 150:
5..3 FABRIC FILTERS ...............
- Page 151 and 152:
Collection by diffusion occurs as a
- Page 153 and 154:
Gravitational sedimentation, i.e. t
- Page 155 and 156:
Table 5.3-1. Recommended Gas-to-Clo
- Page 157 and 158:
5.3-8
- Page 159 and 160:
shaking. In order to accomplish thi
- Page 161 and 162:
5.3-12
- Page 163 and 164:
elatively recent development has be
- Page 165 and 166:
5.3-16
- Page 167 and 168:
5.3.3 Fabric Characteristics Fabric
- Page 169 and 170:
Table 5.3-2. Temperature Ranges, an
- Page 171 and 172:
5.3-22
- Page 173 and 174:
a Application Copper 3-03-005 3-04-
- Page 175 and 176:
The potential for explosion is also
- Page 177 and 178:
Cleaning Mechanism: The fabric filt
- Page 179 and 180:
Particle Characteristics: Particle
- Page 181 and 182:
5.3-32
- Page 183 and 184:
Annual Operating Cost ($ x 10 ) Tab
- Page 185 and 186:
5.3.7 Energy and Other Secondary En
- Page 187 and 188:
15. Compilation of Air Pollutant Em
- Page 189 and 190:
5.4 WET SCRUBBERS Wet scrubbers are
- Page 191 and 192:
5.4.2.1 Spray Chambers Spray chambe
- Page 193 and 194:
5.4-5
- Page 195 and 196:
5.4-7
- Page 197 and 198:
5.4.2.3 Impingement Plate Scrubbers
- Page 199 and 200:
5.4-11
- Page 201 and 202:
5.4.2.5 Venturi Scrubbers A venturi
- Page 203 and 204:
5.4-15
- Page 205 and 206:
5.4.2.7 Condensation Scrubbers Cond
- Page 207 and 208:
5.4-19
- Page 209 and 210:
5.4.3 Collection Efficiency Collect
- Page 211 and 212:
5.4-23
- Page 213 and 214:
Table 5.4-2 lists current applicati
- Page 215 and 216:
Scrubber Type Table 5.4-3. PM 10/PM
- Page 217 and 218:
Table 5.4-4. Capital Cost Factors f
- Page 219 and 220:
5.4-31
- Page 221 and 222:
electricity, sludge disposal, waste
- Page 223 and 224:
Figura 5.4-16. Impiggemennt Scrubbe
- Page 225 and 226:
Table 5.4-6. Annual Cost Parameters
- Page 227 and 228:
5.4.7 References for Section 5.4 1.
- Page 229 and 230:
5.5 INCINERATORS ..................
- Page 231 and 232:
For particles smaller than 100 µm
- Page 233 and 234:
enhanced via vanes or other physica
- Page 235 and 236:
premixing chamber fitted with a (au
- Page 237 and 238:
5.5-8
- Page 239 and 240:
limited only by cost. On the basis
- Page 241 and 242:
C Petroleum and Coal Production C C
- Page 243 and 244:
5.5.5.1 Capital Costs The total cap
- Page 245 and 246:
Total Capital Investment ($) 700,00
- Page 247 and 248:
operate 8,000 hours per year, at a
- Page 249 and 250:
Table 5.5-5. Annual Cost Factors fo
- Page 251 and 252:
1. Control Techniques for Particula
- Page 253 and 254:
6. INDUSTRIAL FUGITIVE EMISSION CON
- Page 255 and 256:
enefication, such as crushing, scre
- Page 257 and 258:
6-4
- Page 259 and 260:
fugitive PM is greater than 90 perc
- Page 261 and 262:
C Changing from a cupola to an elec
- Page 263 and 264:
For information on the control of f
- Page 265 and 266:
6.5 REFERENCES FOR SECTION 6 1. Est
- Page 267 and 268:
7. EMERGING TECHNOLOGIES This secti
- Page 269 and 270:
Table 7-1. Summary of Emerging PM C
- Page 271 and 272:
more filter surface area. This enab
- Page 273 and 274:
C Less sensitive to changes in fuel
- Page 275 and 276:
7.6.2 Dry Fog A device to control f
- Page 277 and 278:
14. Miller, R.L. "Combining ESPs an
- Page 279 and 280:
AMMONIA ApSimon, H.M., D. Cowell, a
- Page 281 and 282:
Control of Volatile Organic Emissio
- Page 283 and 284:
APPENDIX B VATAVUK AIR POLLUTION CO
- Page 285 and 286:
Devices, Fine Particulate Matter, C