Centrifugal Pumps Design and Application 2nd ed - Val S. Lobanoff, Robert R. Ross (Butterworth-Heinemann, 1992)
Pipeline, Waterflood and CO 2 Pumps 165 Figure 10-33. Performance coverage for typical waterflood applications.
166 Centrifugal Pumps: Design and Application pump conditions range in capacity up to 5,000 GPM and heads up to 11,000 feet (Figure 10-33). Pumps are normally multi-stage with horizontal-split or double-case construction. As many applications use corrosive formation water as the pump fluid, special precautions must be taken in material selection. Among the major factors that must be considered in liquid analysis are: • Salinity. » Aeration. » Particulate matter. » Hydrogen sulfide (sour gas) content. »Inhibiting additives. « pH. • Continuous or intermittent service. • Composition of attached piping. Some materials used successfully in waterflood applications are shown in Table 10-1. The groupings are listed in order of increasing corrosion resistance, CO 2 Pumps When waterflood production is no longer effective, injection of CO 2 and other gases (enhanced recovery) can recover up to 70% of the remaining oil. CO 2 can be transported as a gas, using compressors or as a liquid using centrifugal pumps. Due to the questionable lubricating properties of liquid CO 2 , special precautions must be taken where the possibility of internal metal-to- Table 10-1 Materials for Waterflood Service Pressure Wear Group Casing Impeller Shaft Parts 1 Steel CA-6NM* 410 SS* 410 hardened 2 CA-6NM* CA-6NM* 410 SS* 410 hardened 3 316SS 316SS Monel 316LWith or K-500 stellite 17-4 PH or overlay 17-4PH 4 Duplex Duplex Monel Duplex alloy SS SS K-500 with stellite overlay • When # Z S & present or suspected, hardness shall not exceed R
- Page 130 and 131: Vertical Pumps 115 Figure 9-2. Well
- Page 132 and 133: Vertical Pumps 117 Figure 9-4. Subm
- Page 134 and 135: Vertical Pumps 119 Figure 9-6. Inst
- Page 136 and 137: Vertical Pumps 121 Figure 9-8. Barr
- Page 138 and 139: Vertical Pumps 123 • Loading pump
- Page 140 and 141: Vertical Pumps 125 Wet Pit Pumps Th
- Page 142 and 143: Vertical Pumps 127 • Fresh water
- Page 144 and 145: Vertical Pumps 129 Condensate and H
- Page 146 and 147: Vertical Pumps 131 mally insulate w
- Page 148 and 149: Vertical Pumps 133 Figure 9-15. Imp
- Page 150 and 151: Vertical Pumps 135 checked for corr
- Page 152 and 153: Vertical Pumps 137 crating paramete
- Page 154 and 155: 10 Pipeline Pipe line, Waterflood,
- Page 156 and 157: Pipeline, Waterflood and CO 2 Pumps
- Page 158 and 159: Pipeline, Waterflood and CO 2 Pumps
- Page 160 and 161: Pipeline, Waterflood and CO 2 Pumps
- Page 162 and 163: Pipeline, Waterfiood and CO 2 Pumps
- Page 164 and 165: Figure 10-11. Performance change wi
- Page 166 and 167: Figure 10-13. Seven-stage pump dest
- Page 168 and 169: Pipeline, Waterflood and CO 2 Pumps
- Page 170 and 171: Pipeline, Waterflood and CO 2 Pumps
- Page 172 and 173: Pipeline, Waterflood and CO 2 Pumps
- Page 174 and 175: Pipeline, Waterflood and CO 2 Pumps
- Page 176 and 177: Pipeline, Waterflood and CO 2 Pumps
- Page 178 and 179: Pipeline, Waterflood and COa Pumps
- Page 182 and 183: Pipeline, Waterflood and COa Pumps
- Page 184 and 185: Pipeline, Waterflood and COa Pumps
- Page 186 and 187: Pipeline, Waterflood and CO 2 Pumps
- 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 228 and 229: Double-Case Pumps 213 ally by split
166 <strong>Centrifugal</strong> <strong>Pumps</strong>: <strong>Design</strong> <strong>and</strong> <strong>Application</strong><br />
pump conditions range in capacity up to 5,000 GPM <strong>and</strong> heads up to<br />
11,000 feet (Figure 10-33). <strong>Pumps</strong> are normally multi-stage with horizontal-split<br />
or double-case construction. As many applications use corrosive<br />
formation water as the pump fluid, special precautions must be taken<br />
in material selection. Among the major factors that must be consider<strong>ed</strong> in<br />
liquid analysis are:<br />
• Salinity.<br />
» Aeration.<br />
» Particulate matter.<br />
» Hydrogen sulfide (sour gas) content.<br />
»Inhibiting additives.<br />
« pH.<br />
• Continuous or intermittent service.<br />
• Composition of attach<strong>ed</strong> piping.<br />
Some materials us<strong>ed</strong> successfully in waterflood applications are shown<br />
in Table 10-1. The groupings are list<strong>ed</strong> in order of increasing corrosion<br />
resistance,<br />
CO 2 <strong>Pumps</strong><br />
When waterflood production is no longer effective, injection of CO 2<br />
<strong>and</strong> other gases (enhanc<strong>ed</strong> recovery) can recover up to 70% of the remaining<br />
oil. CO 2 can be transport<strong>ed</strong> as a gas, using compressors or as a<br />
liquid using centrifugal pumps.<br />
Due to the questionable lubricating properties of liquid CO 2 , special<br />
precautions must be taken where the possibility of internal metal-to-<br />
Table 10-1<br />
Materials for Waterflood Service<br />
Pressure<br />
Wear<br />
Group Casing Impeller Shaft Parts<br />
1 Steel CA-6NM* 410 SS* 410 harden<strong>ed</strong><br />
2 CA-6NM* CA-6NM* 410 SS* 410 harden<strong>ed</strong><br />
3 316SS 316SS Monel 316LWith<br />
or K-500 stellite<br />
17-4 PH or overlay<br />
17-4PH<br />
4 Duplex Duplex Monel Duplex alloy<br />
SS SS K-500 with stellite<br />
overlay<br />
• When # Z S & present or suspect<strong>ed</strong>, hardness shall not exce<strong>ed</strong> R