Centrifugal Pumps Design and Application 2nd ed - Val S. Lobanoff, Robert R. Ross (Butterworth-Heinemann, 1992)
Double-Case Pumps 213 ally by split rings on the suction side of each impeller hub. This is the preferred mounting. An alternative mounting employs a stack with sliding fits along the shaft. A spacer sleeve is fit snugly between each pair of impellers and an outside locknut is used to secure the impellers and sleeves. Great care is required to assure that all spacer sleeve and impeller faces are parallel to each other, perpendicular to the shaft, and smooth. Small errors in parallelism or perpendicularity will misalign the stack, Impeller Wear Rings Impeller wear rings are generally specified for refinery pumps [1], but must be secured with great care on high-speed, high-pressure pumps. Because boiler feedwater is a relatively clean liquid and rapid wear or seizure is unusual, impeller wear rings are seldom used in large, high-speed double-case boiler feed pumps. These boiler feed pump impellers are designed with extra stock on the wearing surfaces. When worn, impellers are skim cut true, and the pump then fitted with case wear rings that are undersized to match the impeller wearing surfaces, Shaft Seals Shaft seal failure is the most common cause of unscheduled outage for double-case pumps. Selection of a shaft seal system designed for the application is therefore critical to reliable pump operation. Face-Type Mechanical Seals. Oil refinery pumps almost universally use mechanical seals. Reliable seals for high temperature oil and light hydrocarbons now exist. New federal air quality laws limiting hydrocarbon emissions encourage the use of tandem-type seal systems. Figure 12-7 shows a tandem seal assembly with bellows-type seals for hot oil service. In the United States, only small to medium-size (up to 7,000 hp and 5,000 rpm) boiler feed pumps use mechanical seals. In Europe, they are also used in medium to large boiler feed pumps. A typical boiler feed pump seal is shown in Figure 12-8. Most waterflood pumps have mechanical seals, operating at ambient temperatures, but in corrosive liquid. Mechanical seals are described in detail in Chapter 17. Throttle Bushings. The most reliable shaft sealing system for large boiler-feed pumps consists of throttle bushings with a custom designed, cold (90°-120°F) condensate injection system. Pumps have operated for 40 years or more with their original throttle bushings.
214 Centrifugal Pumps: Design and Application Figure 12-7. Tandem seal assembly for hot oil service (courtesy BW/IP international, Inc. Seal Division, manufacturer of BW Seals). Figure 12-8. Shaft seal for boiler feed pump service (courtesy BW/IP International, Inc. Seal Division, manufacturer of BW Seals).
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- Page 188 and 189: 11 By Edward Gravelle Sundstrand Fl
- Page 190 and 191: High Speed Pumps 175 History and De
- Page 192 and 193: High Speed Pumps 177 Figure 11-2. (
- Page 194 and 195: High Speed Pumps 179 some portion o
- Page 196 and 197: High Speed Pumps 181 This is to say
- Page 198 and 199: High Speed Pumps 183 This expressio
- Page 200 and 201: High Speed Pumps 185 Figure 11-3. P
- Page 202 and 203: High Speed Pumps 187 As an aside, p
- Page 204 and 205: High Speed Pumps 189 Figure 11-5. I
- Page 206 and 207: High Speed Pumps 191 Figure 11-7. I
- Page 208 and 209: High Speed Pumps 193 Figure 11-9. R
- Page 210 and 211: High Speed Pumps 195 Figure 11-10.
- Page 212 and 213: High Speed Pumps 19? Figure 11-11.
- Page 214 and 215: High Speed Pumps 199
- Page 216 and 217: High Speed Pumps 201 Figure 11-13.
- Page 218 and 219: High Speed Pumps 203 nal bearings a
- Page 220 and 221: High Speed Pumps 205 Barske, U, M.,
- Page 222 and 223: Double-Case Pumps 207 jected to ext
- Page 224 and 225: Double-Case Pumps 209 Figure 12-3.
- Page 226 and 227: Double-Case Pumps 211 Figure 12-4.
- Page 230 and 231: Double-Case Pumps 215 The throttle
- Page 232 and 233: Figure 12-11. pump for 4,000 psi In
- Page 234 and 235: Double-Case Pumps 219 so that the t
- Page 236 and 237: Double-Case Pumps 221 Figure 12-12.
- Page 238 and 239: Doubte-Case Pumps 223 Volute Casing
- Page 240 and 241: Double-Case Pumps 225 5. Survey of
- Page 242 and 243: Slurry Pumps 227 An approximate com
- Page 244 and 245: Slurry Pumps 229 Figure 13-2. Nomog
- Page 246 and 247: Slurry Pumps 231 Table 13-2 Alloys
- Page 248 and 249: Slurry Pumps 233 Figure 13-3. Class
- Page 250 and 251: Figure 13-4, (A) (B) (C)
- Page 252 and 253: Slurry Pumps 237 There is little to
- Page 254 and 255: Figyre 13-7, (courtesy Pumps, Inc.)
- Page 256 and 257: Flgyr« 13-8, with (courtesy Goulds
- Page 258 and 259: Slurry Pumps 243 ing the pump speed
- Page 260 and 261: Slurry Pumps 245 Where there exists
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214 <strong>Centrifugal</strong> <strong>Pumps</strong>: <strong>Design</strong> <strong>and</strong> <strong>Application</strong><br />
Figure 12-7. T<strong>and</strong>em seal assembly for hot oil service (courtesy BW/IP international,<br />
Inc. Seal Division, manufacturer of BW Seals).<br />
Figure 12-8. Shaft seal for boiler fe<strong>ed</strong> pump service (courtesy BW/IP International,<br />
Inc. Seal Division, manufacturer of BW Seals).