240,99 €
PETROLEUM REFINING With no new refineries having been built in decades, companies continue to build onto or reverse engineer and re-tool existing refineries. With so many changes in the last few years alone, books like this are very much in need. There is truly a renaissance for chemical and process engineering going on right now across multiple industries. This fifth and final volume in the "Petroleum Refining Design and Applications Handbook" set, this book continues the most up-to-date and comprehensive coverage of the most significant and recent changes to petroleum refining, presenting the state-of-the-art to the engineer, scientist, or student. Besides the list below, this groundbreaking new volume describes blending of products from the refinery, applying the ternary diagrams and classifications of crude oils, flash point blending, pour point blending, aniline point blending, smoke point and viscosity blending, cetane and diesel indices. The volume further reviews refinery operational cost, cost allocation of actual usage, project and economic evaluation involving cost estimation, cash flow involving return on investment, net present values, discounted cash flow rate of return, net present values, payback period, inflation and sensitivity analysis, and so on. It reviews global effects on the refining economy, carbon tax, carbon foot print, global warming potential, carbon dioxide equivalent, carbon credit, carbon offset, carbon price, and so on. It reviews sustainability in petroleum refining and alternative fuels (biofuels and so on), impact of the overall greenhouse effects, carbon capture and storage in refineries, process intensification in biodiesel, biofuel from green diesel, acid-gas removal and emerging technologies, carbon capture and storage, gas heated reformer unit, pressure swing adsorption process, steam methane reforming for fuel cells, grey, blue and green hydrogen production, new technologies for carbon capture and storage, carbon clean process design, refinery of the future, refining and petrochemical industry characteristics. The text is packed with Excel spreadsheet calculations and Honeywell UniSim Design software in some examples, and it includes an invaluable glossary of petroleum and petrochemical technical terminologies. Useful as a textbook, this is also an excellent, handy go-to reference for the veteran engineer, a volume no chemical or process engineering library should be without. Written by one of the world's foremost authorities, this book sets the standard for the industry and is an integral part of the petroleum refining renaissance. It is truly a must-have for any practicing engineer or student in this area.
Sie lesen das E-Book in den Legimi-Apps auf:
Seitenzahl: 1575
Veröffentlichungsjahr: 2023
Cover
Series Page
Title Page
Copyright
Companion Web Page
Dedication
Preface
Acknowledgments
23 Pressure Relieving Devices and Emergency Relief System Design
23.0 Introduction
23.1 Types of Positive Pressure Relieving Devices (See Manufacturers’ Catalogs for Design Details)
23.2 Types of Valves/Relief Devices
23.3 Materials of Construction
23.4 General Code Requirements [1]
23.5 Relief Mechanisms
23.6 Pressure Settings and Design Basis
23.7 Unfired Pressure Vessels Only, But Not Fired or Unfired Steam Boilers
23.8 Relieving Capacity of Combinations of Safety Relief Valves and Rupture Disks or Non-Reclosure Devices (Reference ASME Code, Par. UG-127, U-132)
23.9 Establishing Relieving or Set Pressures
23.10 Selection and Application
23.11 Capacity Requirements Evaluation for Process Operation (Non-Fire)
23.12 Piping Design
23.13 Selection Features: Safety, Safety-Relief Valves, and Rupture Disks
23.14 Calculations of Relieving Areas: Safety and Relief Valves
23.15 Standard Pressure Relief Valves Relief Area Discharge Openings
23.16 Sizing Safety Relief Type Devices for Required Flow Area at Time of Relief
23.17 Effects of Two-Phase Vapor-Liquid Mixture on Relief Valve Capacity
23.18 Sizing for Gases or Vapors or Liquids for Conventional Valves with Constant Backpressure Only
23.19 Orifice Area Calculations [42]
23.20 Sizing Valves for Liquid Relief: Pressure-Relief Valves Requiring Capacity Certification [5D]
23.21 Sizing Valves For Liquid Relief: Pressure Relief Valves Not Requiring Capacity Certification [5D]
23.22 Reaction Forces
23.23 Calculations of Orifice Flow Area using Pressure Relieving Balanced Bellows Valves, with Variable or Constant Backpressure
23.24 Sizing Valves for Liquid Expansion (Hydraulic Expansion of Liquid Filled Systems/Equipment/Piping)
23.25 Sizing Valves for Subcritical Flow: Gas or Vapor But Not Steam [5d]
23.26 Emergency Pressure Relief: Fires and Explosions Rupture Disks
23.27 External Fires
23.28 Set Pressures for External Fires
23.29 Heat Absorbed
23.30 Surface Area Exposed to Fire
23.31 Relief Capacity for Fire Exposure
23.32 Code Requirements for External Fire Conditions
23.33 Design Procedure
23.34 Pressure Relief Valve Orifice Areas on Vessels Containing Only Gas, Unwetted Surface
23.35 Rupture Disk Sizing Design and Specification
23.36 Specifications to Manufacturer
23.37 Size Selection
23.38 Calculation of Relieving Areas: Rupture Disks for Non-Explosive Service
23.39 The Manufacturing Range (MR)
23.40 Selection of Burst Pressure for Disk, P
b
(Table 23.3)
23.41 Effects of Temperature on Disk
23.42 Rupture Disk Assembly Pressure Drop
23.43 Gases and Vapors: Rupture Disks [5a, Par, 4.8]
23.44 API for Subsonic Flow: Gas or Vapor (Not Steam)
23.45 Liquids: Rupture Disk
23.46 Sizing for Combination of Rupture Disk and Pressure Relief Valve in Series Combination
23.47 Pressure-Vacuum Relief for Low-Pressure Storage Tanks
23.48 Basic Venting For Low-Pressure Storage Vessels
23.49 Non-Refrigerated Above Ground Tanks; API-Std. 2000
23.50 Boiling Liquid Expanding Vapor Explosions (BLEVEs)
23.51 Managing Runaway Reactions
23.52 Hazard Evaluation in the Chemical Process Industries
23.53 Hazard Assessment Procedures
23.54 Thermal Runaway Chemical Reaction Hazards
23.55 Two-Phase Flow Relief Sizing for Runaway Reaction
23.56 Discharge System
23.57 Sizing for Two-Phase Fluids
23.58 Flares/Flare Stacks
23.59 Compressible Flow for Discharge Piping
23.60 Vent Piping
References
24 Process Safety and Energy Management in Petroleum Refinery
24.1 Introduction
24.2 Process Safety
24.3 General Process Safety Hazards in a Refinery
24.4 Example of Process Safety Incidents and Hazards
24.5 Process Safety Hazards
24.6 Hazards Relating to Equipment Failure
24.7 Columns and Other Process Pressure Vessels and Piping
24.8 Inadequate Design and Construction
24.9 Inadequate Material of Construction Specification
24.10 Material Failures and Process Safety Prevention Programs
24.11 Hazard and Operability Studies (HAZOP)
24.12 HAZAN
24.13 Fault Tree Analysis
24.14 Failure Mode and Effect Analysis (FMEA)
24.15 The Swiss Cheese Model
24.16 Bowtie Analysis
24.17 Inherently Safer Plant Design
24.18 Energy Management in Petroleum Refinery
24.19 Benchmarking in Refinery
Glossary
Acronyms and Abbreviations
References
25 Product Blending
25.0 Introduction
25.1 Blending Processes
25.2 Ternary Diagram of Crude Oils
25.3 Reid Vapor Pressure Blending
25.4 Flash Point Blending
25.5 Alternative Methods for Determining the Blend Flash Point
25.6 Pour Point Blending
25.7 Cloud Point Blending
25.8 Aniline Point Blending
25.9 Smoke Point Blending
25.10 Viscosity Blending
25.11 Regular Gasoline
25.12 Product Blending
25.13 Viscosity Prediction From the Crude Assay
25.14 Gasoline Octane Number Blending
25.15 Other Blending Correlations
25.16 Fluidity of Residual Fuel Oils
25.17 Conversion of Kinematic Viscosity to Saybolt Universal
25.18 Determination of Molecular-Type Composition
25.19 Determination of Viscosity From Viscosity/Temperature Data at Two Points
25.20 Linear Programming (LP) for Blending
25.21 Environmental Concern of Gasoline Blending
References
Bibliography
26 Cost Estimation and Economic Evaluation
26.1 Introduction
26.2 Refinery Operating Cost
26.3 Capital Cost Estimation
26.4 Equipment Cost Estimations by Capacity Ratio Exponents
26.5 Yearly Cost Indices
26.6 Factored Cost Estimate
26.7 Detailed Factorial Cost Estimates
26.8 Bare Module Cost for Equipment
26.9 Summary of the Factorial Method
26.10 Computer Cost Estimating
26.11 Project Evaluation
26.12 Cash Flows
26.13 Refining Economics
26.14 Global Effects on Refining Economy
26.15 Economic Terminologies on Sustainability
References
Bibliography
27 Sustainability in Engineering, Petroleum Refining and Alternative Fuels
27.0 Introduction
27.1 Impacts on the Overall Greenhouse Effect
27.2 Carbon Capture and Storage in Refineries
27.3 Sustainability in the Refinery Industries
27.4 Sustainability in Engineering Design Principles
27.5 Alternative Fuels (Biofuels)
27.6 Process Intensification (PI) in Biodiesel
27.7 Biofuel from Green Diesel
27.8 Fast Pyrolysis
27.9 Acid Gas Removal
27.10 Alkaline Salt Process (Hot Carbonate)
27.11 Ionic Liquids
27.12 Advanced Modeling
27.13 Carbon Capture and Storage (CCS)
27.14 Risk Management
27.15 The Institution of Chemical Engineers (IChemE, U.K.) Position on Climate Change
27.16 Oil & Gas and Petrochemical Companies with Zero Carbon Emissions Targets by 2050
27.17 Offshore Petroleum Regulator for Environment and Decommissioning (OPRED), UK
27.18 Gas Heated Reformer (GHR)
27.19 Pressure Swing Adsorption (PSA)
27.20 Distribution and Storage
27.21 Steam Methane Reforming (SMR) for Fuel Cells
27.22 New Technologies of Carbon Capture Storage
27.23 Carbon Clean Process Design (CC)
27.24 Electrochemically Mediated Amine Regeneration (EMAR)
27.25 Refinery of the Future
27.26 The Crude Oil to Chemical Strategy (COC)
27.27 Available Crude to Chemicals Processing Routes
27.28 Chemical Looping
27.29 Conclusions
Glossary
References
Bibliography
Appendix D
Glossary of Petroleum and Petrochemical Technical Terminologies
About the Author
Index
Also of Interest
End User License Agreement
Cover
Table of Contents
Title Page
Copyright
Companion Web Page
Dedication
Preface
Acknowledgments
Begin Reading
Appendix D
Glossary of Petroleum and Petrochemical Technical Terminologies
About the Author
Index
Also of Interest
End User License Agreement
x
ii
iii
iv
v
vi
vii
viii
xxiv
xxv
xxvi
xxvii
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
70
71
72
73
74
75
76
77
78
79
80
81
82
83
84
85
86
87
88
89
90
91
92
93
94
95
96
97
98
99
100
101
102
103
104
105
106
107
108
109
110
111
112
113
114
115
116
117
118
119
120
121
122
123
124
125
126
127
128
129
130
131
132
133
134
135
136
137
138
139
140
141
142
143
144
145
146
147
148
149
150
151
152
153
154
155
156
157
158
159
160
161
162
163
164
165
166
167
168
169
170
171
172
173
174
175
176
177
178
179
180
181
182
183
184
185
186
187
188
189
190
191
192
193
194
195
196
197
198
199
200
201
202
203
204
205
206
207
208
209
210
211
212
213
214
215
216
217
218
219
220
221
222
223
224
225
226
227
228
229
230
231
232
233
234
235
236
237
238
239
240
241
242
243
244
245
246
247
248
249
250
251
252
253
254
255
256
257
258
259
260
261
262
263
264
265
266
267
268
269
270
271
272
273
274
275
276
277
278
279
280
281
282
283
284
285
286
287
288
289
290
291
292
293
294
295
296
297
298
299
300
301
302
303
304
305
306
307
308
309
310
311
312
313
314
315
316
317
318
319
320
321
322
323
324
325
326
327
328
329
330
331
332
333
334
335
336
337
338
339
340
341
342
343
344
345
346
347
348
349
350
351
352
353
354
355
356
357
358
359
360
361
362
363
364
365
366
367
368
369
370
371
372
373
374
375
376
377
378
379
380
381
382
383
384
385
386
387
388
389
390
391
392
393
394
395
396
397
398
399
400
401
402
403
404
405
406
407
408
409
410
411
412
413
414
415
416
417
418
419
420
421
422
423
424
425
426
427
428
429
430
431
432
433
434
435
436
437
438
439
440
441
442
443
444
445
446
447
448
449
450
451
452
453
454
455
456
457
458
459
460
461
462
463
464
465
466
467
468
469
470
471
472
473
474
475
476
477
478
479
480
481
482
483
484
485
486
487
488
489
490
491
492
493
494
495
496
497
498
499
500
501
502
503
504
505
506
507
508
509
510
511
512
513
514
515
516
517
518
519
520
521
522
523
524
525
526
527
528
529
530
531
532
533
534
535
536
537
538
539
540
541
542
543
544
545
546
547
548
549
550
551
552
553
554
555
556
557
558
559
560
561
562
563
564
565
566
567
568
569
570
571
572
573
574
575
576
577
578
579
580
581
582
583
584
585
586
587
588
589
590
591
592
593
594
595
596
597
598
599
600
601
602
603
604
605
606
607
608
609
610
611
612
613
614
615
616
617
618
619
620
621
622
623
624
625
626
627
628
629
630
631
632
633
634
635
636
637
638
639
640
641
642
643
644
645
646
647
648
649
650
651
652
653
654
655
656
657
658
659
660
661
662
663
664
665
666
667
668
669
670
671
672
673
674
675
676
677
678
679
680
681
682
683
684
685
686
687
688
689
690
691
692
693
694
695
696
697
698
699
700
701
702
703
704
705
706
707
708
709
710
711
712
713
714
715
716
717
718
719
720
721
722
723
724
725
726
727
728
729
730
731
732
733
734
735
736
737
738
739
740
741
742
743
744
745
746
747
748
749
750
751
752
753
754
755
756
757
758
759
760
761
762
763
764
765
766
767
768
769
770
771
772
773
774
775
776
777
778
779
780
781
782
783
784
785
786
787
788
789
790
791
792
793
794
795
796
797
798
799
800
801
802
803
804
805
806
807
808
809
810
811
812
813
814
815
816
817
818
819
820
821
822
823
824
825
826
827
828
829
830
831
832
833
834
835
836
837
838
839
840
841
842
843
844
845
846
847
848
849
850
851
852
853
854
855
856
857
858
859
860
861
862
863
864
865
866
867
868
869
870
871
872
873
874
875
876
877
878
879
880
881
882
883
884
885
886
887
888
889
890
891
892