Handbook of Corrosion Engineering Episode 2 Part 14 ppt
Handbook of Corrosion Engineering Episode 1 Part 14 pps
... 4.6 Ϫ0 .1 1.7 2.8 5.7 7.0 6.3 3.5 3.5 4.6 0 .1 1.8 2.9 6.0 7.0 6.3 3.5 3.5 4.7 0.2 2.0 3 .1 6.0 7 .1 6.7 3.7 3.8 4.8 0.4 2 .1 3.4 6 .1 7.2 6.8 3.8 3.9 4.9 0.5 2.5 3.4 6.2 7.3 6.9 5 .1 4.3 5.0 1. 1 2.9 ... apparatus. 076 516 2_Ch07_Roberge 9 /1/ 99 5: 41 Page 5 01 485 Acceleration and Amplification of Corrosion Damage 7 .1 Introduction 486 7.2 Corrosion Testing 488 7.2 .1 Co...
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Handbook of Corrosion Engineering Episode 1 Part 14 ppsx
... Amplification of Corrosion Damage 489 076 516 2_Ch07_Roberge 9 /1/ 99 5: 41 Page 489 References 1. Moreland, P. J., and Hines, J. G., Hydrocarbon Processing, 17 (1) :1 31 (19 78). 2. Timmins, P. F., Predictive Corrosion ... CANMET, 19 92, pp. 17 -1 17 -7. 34. Agarwala, V. S., “Chemical Sensors for Integrity of Coatings,” Tri-Service Conference on Corrosion, 19 92, pp. 315 –32...
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Handbook of Corrosion Engineering Episode 2 Part 1 ppt
... Ni -16 Cr -16 Mo (C276) 16 . Ni -20 Cr -16 Mo-4 W (686) 17 . Ni -22 Cr -16 Mo (C 22/ 59) 18 . Ni -23 Cr -16 Mo -1 Cu (C20000) 19 . Ni-30 Mo (B -2) 20 . Nickel (20 0) 21 . Nickel cast iron (15 -35Ni) 22 . Nickel-chromium-iron ... g /15 00 h g /10 years g /15 00 h g /10 years LM1M† 0.87 0.43 0.06 0.09 LM4M 0.34 0 .18 0. 02 0.09 LM5M 0 .19 0.06 0 0 .10 LM6M 0.05 0. 12 0 0.04 LM14WP 0...
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Handbook of Corrosion Engineering Episode 2 Part 1 pot
... 0. 01 1 at% 1 10 nm Yes 10 m 2 mm HFS H, D — 0. 01 at% 50 nm No 2 mm ϫ 10 mm RBS Li–U — 1 10 at% (Z Ͻ 20 ) 2 mm Yes 0. 01 1 at% (20 Ͻ Z Ͻ 70) 0.0 01 0. 01 at% (Z Ͼ 70) SEM/EDS B–U — 0 .1 1 at% 1 5 ... (Ͼ 15 Zn) 9. Cast iron, gray/ductile 10 . Copper/bronze/Low brass 11 . Copper-nickel 12 . Duplex (25 -6-3) 13 . Gold/platinum 14 . Lead 15 . Ni -16 Cr -16 Mo (C276) 16 ....
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Handbook of Corrosion Engineering Episode 2 Part 2 pptx
... D D 20 24 T3 L A A A LT B D B ST D D D 20 24 T4 L A A A LT B D B ST D D D 20 24 T6 L A A LT B A ST B D 20 24 T8 L A A A A LT A A A A ST B A B C 20 48 T851 L A LT A ST B 21 24 T851 L A LT A ST B 22 19 ... A LT A ST B 22 19 T351X L A A LT B B ST D D 22 19 T37 L A A LT B B ST D D 22 19 T6 L A A A A LT A A A A ST A A A A 22 19 T85XX L A A A LT A A A ST A A A 22 19 T87 L A A A LT A A A...
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Handbook of Corrosion Engineering Episode 2 Part 2 pptx
... D 20 24 T8 L A A A A LT A A A A ST B A B C 20 48 T851 L A LT A ST B 21 24 T851 L A LT A ST B 22 19 T351X L A A LT B B ST D D 22 19 T37 L A A LT B B ST D D 22 19 T6 L A A A A LT A A A A ST A A A A 22 19 ... Forging 20 11 T3 L B LT D ST D 20 11 T4 L B LT D ST D 20 11 T8 L A LT A ST A 20 14 T6 L A A A B LT B D B B ST D D D D 20 24 T3 L A A A LT B D B ST D D D 20 24 T4 L A A A LT B D...
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Handbook of Corrosion Engineering Episode 2 Part 3 pot
... Given) ISO BS UNS DIN CuNi30MnlFe CN 107 C71500 CuNi30Fe 2. 08 82 Copper Minimum Rem. Rem. Rem. Rem. Maximum Nickel Minimum 29 .0 30 .0 29 .0 30 .0 Maximum 32 . 0 32 . 0 33 .0 32 . 0 Iron Minimum 0.4 0.4 0.4 ... TABLE 8. 13 Corrosion- Resistance Ratings * for Coppers (C11000, C 122 00), Brasses (C 220 00, C 230 00, C26000, 28 000), Leaded Brasses (C36000, C38500), and Tin Brasses (C...
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Handbook of Corrosion Engineering Episode 2 Part 5 ppt
... 450 690 25 S3 126 0 DP-3 450 690 25 S3 150 0 3RE60 440 630 30 S31803 22 05 450 620 25 S 3 25 50 Ferralium 25 5 550 760 15 S 329 50 7-Mo PLUS. 4 85 690 15 0 5 10 15 20 25 30 0 5 10 15 20 25 30 35 40 Ferrite ... 483 310 25 B80 S41000 410 483 310 25 B80 S41400 414 827 724 15 B98 S43000 416 51 7 27 6 30 B 82 Bar S 420 00 416Se 51 7 27 6 30 B 82 Bar S 422 00...
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Handbook of Corrosion Engineering Episode 2 Part 6 ppt
... grades R697 02 7 02 379 20 7 16 R69704 704 413 24 1 14 R69705 705 5 52 379 16 R697 06 7 06 510 345 20 Nuclear grades R60001 (annealed) Unalloyed 29 6 20 7 18 R608 02 (annealed) Zircalloy -2 3 86 303 25 R60804 ... exchanger S3 160 0 3 16 1 1 1 1 R50400 Ti, grade 2 2.0 2. 25 2. 0 1.5 R53400 Ti, grade 12 3.1 9 .6 2. 2 1.7 N 066 00 Inconel 60 0 3 .6 4.0 3.0 1.8 R 524...
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Handbook of Corrosion Engineering Episode 2 Part 9 ppt
... resistance of the Cathodic Protection 90 3 -2. 5 -2 -1.5 -1 -0.5 0 0.5 1 361 1081 1441 1801 21 61 25 21 28 81 324 1 3601 721 Time (seconds) Potential (Volts) Pipe - Side B Pipe - Side A Figure 11 .20 Potential ... criteria for protection against corrosion are based on the potential of the pipeline at the interface Cathodic Protection 90 9 07651 62_ Ch11_Roberge 9/ 1 /99 6:37 P...
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Handbook of Corrosion Engineering Episode 2 Part 10 ppt
... maintain, H 2 SO Temperature, °C Alloy mAиcm 2 Aиcm 2 1 M 24 S31600 2. 3 12 15% 24 S30400 0. 42 72 30% 24 S30400 0.54 24 45% 65 S30400 180 890 67% 24 S30400 5.1 3.9 67% 24 S31600 0.51 0 .10 67% 24 N08 020 ... 0.43 0.9 93% 24 Mild steel 0 .28 23 99.9% (oleum) 24 Mild steel 4.7 12 H 3 PO 4 75% 24 Mild steel 41 20 ,000 115% 82 S30400 3 .2 ϫ 10 Ϫ5 1.5 ϫ 10 Ϫ4 NaOH...
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Handbook of Corrosion Engineering Episode 2 Part 11 pptx
... (6. 02 ϫ 10 23 atoms of an element or 6. 02 ϫ 10 23 molecules of Glossary 979 07651 62_ AppB_Roberge 9/1/99 6:51 Page 979 passivator A type of inhibitor which appreciably changes the potential of ... Page 9 62 a chemical compound) as there are atoms of carbon in 0.0 12 kg of the pure nuclide C 12 . The weight of one mole of an element is equal to its atomic weight i...
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Handbook of Corrosion Engineering Episode 2 Part 12 ppt
... reaction, atoms of the elements involved gain electrons. Example Zn 2 (aq) ϩ 2e Ϫ → Zn (s) 10 12 Appendix D 07651 62_ AppD_Roberge 9/1/99 8: 12 Page 10 12 2AlO 2 Ϫ ϩ 2H 2 O → Al 2 O 3 и H 2 O ϩ 2OH Ϫ (D.41) There ... u, 10 Ϫ8 m 2 иs Ϫ1 иV Ϫ1 H ϩ 36 .28 OH Ϫ 20 .56 Al 3ϩ 6.53 Br Ϫ 8.10 Ag ϩ 6. 42 CH 3 CO 2 Ϫ 4 .24 Ba 2 6.59 C 2 H 5 CO 2 Ϫ 3.71 Ca 2 6.17 C 6 H 5...
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Handbook of Corrosion Engineering Episode 2 Part 14 ppt
... 1HCuO 2 Ϫ ϭ 2H 2 Oϩ1Cu 16. 2 e Ϫ ϩ 4H ϩ ϩ 1CuO 2 2Ϫ ϭ 2H 2 Oϩ1Cu 17. 2 e Ϫ ϩ 1H 2 Oϩ2Cu 2 ϭ 2H ϩ ϩ 1Cu 2 O 18. 2 e Ϫ ϩ 4H ϩ ϩ 2HCuO 2 Ϫ ϭ 3H 2 Oϩ1Cu 2 O 19. 2 e Ϫ ϩ 6H ϩ ϩ 2CuO 2 2Ϫ ϭ 3H 2 Oϩ1Cu 2 O 20 . ... 10 Ϫ5 O 2 0 20 5 29 .96 4.184 Ϫ1.674 H 2 0 131 27 .28 3 .26 3 0.5 02 H 2 O 23 7,000 69.9 75 .27 0 0 Cu 0 33 .2 22. 635 6 .27 6 0 Cu 2 O 147...
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Handbook of Corrosion Engineering Episode 2 Part 14 pot
... 0 .2 0.5 26 –30 8–11 Rem. J 926 03 HF 0 .2 0.4 19 23 9– 12 Rem. J93503 HH 0 .2 0.5 24 28 11 14 Rem. J94003 HI 0 .2 0.5 26 –30 14 18 Rem. J9 422 4 HK 0 .2 0.6 24 28 18 22 Rem. J94604 HL 0 .2 0.6 28 – 32 18 22 ... 1HCuO 2 Ϫ ϭ 2H 2 Oϩ1Cu 16. 2 e Ϫ ϩ 4H ϩ ϩ 1CuO 2 2Ϫ ϭ 2H 2 Oϩ1Cu 17. 2 e Ϫ ϩ 1H 2 Oϩ2Cu 2 ϭ 2H ϩ ϩ 1Cu 2 O 18. 2 e Ϫ ϩ 4H ϩ ϩ 2HCuO 2 Ϫ ϭ 3H 2 Oϩ1Cu...
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