Oilfield Processing of Petroleum: Crude oilCovers process descriptions, design method, operating procedures, and troubleshooting in great detail. This text is the definitive source on its topic and contains numerous diagrams and appendices, as well as case histories and review questions with numerical problems. |
What people are saying - Write a review
User Review - Flag as inappropriate
Oilfield Processing of Petroleum: Crude oil Vol. 02
User Review - Flag as inappropriate
this book is perfect for understandig this system at first place
recommand for new process employee in this industry
Contents
TURBINE METERS | 217 |
ORIFICE METERS | 219 |
METER PROVING | 221 |
MASS FLOWMETERS | 227 |
MULTIPHASE FLOW METERING | 229 |
METER SELECTION | 231 |
METERING ERROR | 232 |
Review Questions | 234 |
| 27 | |
| 29 | |
| 35 | |
| 36 | |
| 39 | |
| 41 | |
| 44 | |
| 45 | |
| 52 | |
| 56 | |
| 57 | |
| 58 | |
| 61 | |
| 63 | |
| 65 | |
| 73 | |
| 76 | |
| 77 | |
| 79 | |
| 80 | |
COMPARISON OF SEPARATORS | 90 |
PHASE SEPARATION THEORY | 91 |
DESIGN CONSIDERATIONS | 95 |
DESIGN EXAMPLES | 101 |
MAINTENANCE AND TROUBLESHOOTING | 108 |
Review Questions | 109 |
Nomenclature | 110 |
References | 111 |
Dehydration of Crude Oil | 113 |
TERMINOLOGY | 114 |
TREATING METHODS | 115 |
DESIGN CONSIDERATIONS | 131 |
DESIGN EXAMPLES | 136 |
OPERATION AND MAINTENANCE | 138 |
Review Questions | 140 |
Problems | 141 |
References | 142 |
Desalting of Crude Oil | 145 |
PROCESS DESCRIPTION | 146 |
DESIGN CONSIDERATIONS | 149 |
DESIGN PROCEDURES | 150 |
OPERATION | 154 |
TROUBLESHOOTING | 155 |
Problems | 156 |
References | 157 |
APPENDIX 82 | 158 |
Stabilization and Sweetening of Crude Oil | 159 |
MULTISTAGE SEPARATION | 160 |
CONDENSATE | 165 |
MORECOMPLEX PROCESSING | 167 |
SWEETENING | 168 |
SUMMARY | 172 |
Review Questions | 173 |
References | 174 |
Pumps | 175 |
CENTRIFUGAL PUMPS | 176 |
POSITIVE DISPLACEMENT PUMPS | 182 |
DRIVERS | 184 |
PUMP SELECTION | 185 |
PUMP DESIGN THEORY | 188 |
DESIGN PROCEDURE | 191 |
INSTALLATION AND OPERATION | 195 |
TROUBLESHOOTING | 197 |
Problems | 199 |
Nomenclature | 200 |
Measurement of Crude Oil | 203 |
STORAGE TANKS | 206 |
LEASE AUTOMATIC CUSTODY TRANSFER LACT UNITS | 213 |
Problems | 235 |
References | 237 |
Firetube Heaters | 239 |
COMBUSTION | 240 |
FIRETUBE HEATERS | 244 |
DESIGN | 254 |
OPERATION | 263 |
Review Questions | 265 |
Problems | 266 |
References | 267 |
Transportation of Crude Oil | 269 |
HEAVY OIL TRANSPORT | 281 |
PIPELINE PUMP SELECTION | 285 |
PIPELINE OPERATION | 286 |
PIPELINE CONSTRUCTION | 288 |
Problems | 289 |
Nomenclature | 290 |
References | 291 |
Energy Conservation | 293 |
ENERGY AUDITS | 295 |
FIRED HEATERS | 297 |
PRIME MOVERS | 300 |
WASTE HEAT RECOVERY | 302 |
DEHYDRATION OF CRUDE OIL | 303 |
OPERATING PRESSURE AND VAPOR RECOVERY | 304 |
ELECTRICAL POWER | 306 |
MISCELLANEOUS | 311 |
SUMMARY | 313 |
Review Questions | 314 |
Nomenclature | 315 |
References | 316 |
Instrumentation and Process Control | 319 |
FEEDBACK CONTROL | 321 |
ADVANCED CONTROL LOOPS | 322 |
SENSING DEVICES | 324 |
CONTROLLERS AND CONTROL ACTION | 331 |
SAFETY AND CONTROL APPLICATIONS | 334 |
CONTROL OF PROCESSING PLANTS | 338 |
Review Questions | 347 |
Problems | 348 |
References | 349 |
Pressure Relief and Flaring | 351 |
DEPRESSURING EMERGENCY RELIEF AND FLARE SYSTEMS | 352 |
GENERAL CONSIDERATIONS | 354 |
PRESSURE RELIEF DEVICES | 356 |
FLARING | 365 |
Review Questions | 374 |
Problems | 375 |
References | 376 |
Case Studies | 379 |
CASE STUDY NO 2 | 384 |
Review Questions | 388 |
References | 390 |
GLOSSARY OF TERMS | 391 |
MATERIAL BALANCES | 399 |
ENERGY BALANCES | 403 |
OPSIM | 406 |
OPSIM Execution | 409 |
Example Problems | 411 |
Description of the Modules | 416 |
Structure of OPSIM | 422 |
References | 423 |
CONVERSION OF UNITS | 424 |
CONVERSION FACTORS | 425 |
PHYSICAL PROPERTIES OF FLUIDS | 426 |
Index | 430 |
Common terms and phrases
allowable applications burner calculations capacity cause centrifugal Chapter Check Chemical component compressor constant contains correction cost crude oil density desalting described devices diameter discharge discussed drop effect efficiency electric emulsion energy Engineering equation equipment Estimate Example excess factor feed field Figure firetube flame flare flow rate fluid fraction fuel given gravity head heat heater horizontal hydrocarbons increases inlet installed internal Journal liquid loss maximum measured meter method natural operating outlet Petroleum phase pipe pipeline present pressure problems production psia psig pump recommended reduced References relief removed safety selection separator shown shows sizing Source specific stabilization stack stage standard stream suction surface Table tank temperature tion treating Typical units usually valve vapor vary vertical vessel viscosity volume
Popular passages
Page 395 - SPECIFIC GRAVITY, the ratio of the mass of a given volume of a substance to the mass of an equal volume of a standard substance.
Page 19 - Test Method for Density, Specific Gravity, or API Gravity of Crude Petroleum and Liquid Petroleum Products by Hydrometer Method4 3.
Page 366 - The curve above shows that up to and including 25-percent overpressure, capacity is affected by the change in lift, the change in the orifice discharge coefficient, and the change in overpressure. Above 25 percent, capacity is affected only by the change in overpressure. Valves operating at low overpressures tend to chatter; therefore, overpressures of less than 10 percent should be avoided.
Page 142 - Recommended Practice for Analysis, Design, Installation and Testing of Basic Surface Safety Systems on Offshore Production Platforms...
Page 59 - Effect of pH on Interfacial Films and Stability of Crude Oil-Water Emulsions," JPT (March 1968) 303-12; Trans.
Page 143 - Sulfide Stress Cracking Resistant Metallic Material for Oil Field Equipment," NACE Standard MR-01-75 (1980 Revision).
Page 366 - Kw = correction factor due to back pressure. 8, = back pressure, in pounds per square inch gauge. PS = set pressure, in pounds per square inch gauge. Note: The curve above represents values recommended by various manufacturers. This curve may be used when the manufacturer is not known. Otherwise, the manufacturer should be consulted for the applicable correction factor. Figure 16-4.
Page 274 - In general, the friction factor is a function of the Reynolds number, Re, and the relative roughness of the pipe, e/D.
Page 58 - Emulsions Fundamentals and Applications in the Petroleum Industry.





