Oilfield Processing of Petroleum: Crude oil

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Covers 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.

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Oilfield Processing of Petroleum: Crude oil Vol. 02

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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

EQUILIBRIUM CALCULATIONS
27
THERMODYNAMICS OF VAPORLIQUID EQUILIBRIA
29
Nomenclature
35
Review Questions
36
WaterinCrude Oil Emulsions
39
WELLHEAD EMULSIONS
41
EMULSION STABILITY
44
SETTLINGRISING VELOCITIES
45
POTENTIAL EMULSIFICATION TENDENCIES OF PRODUCTION PRACTICES
52
Review Questions
56
Problems
57
References
58
Field Processing of Crude Oil
61
PROCESSING OPERATIONS
63
PROCESSING SCOPE
65
ENVIRONMENTAL CONSIDERATIONS
73
Review Questions
76
Nomenclature
77
Phase Separation of Gas Oil and Water
79
PHYSICAL DESCRIPTION
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
Copyright

Common terms and phrases

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.