Corrosion in Fertiliser and Petroleum Industry: Proceedings of Short Course on "Corrosion in Fertiliser and Petroleum Industry" Organised by the Corrosion Advisory Bureau at Udyogamandal from 20th to 24th December 1968 |
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Page 31
... scrubbing solution , fitted to a mild steel shell operating at around 125°C , may
probably be by galvanic effect . The remedy would be either to provide complete
insulation between aluminium and mild steel or to change over completely to ...
... scrubbing solution , fitted to a mild steel shell operating at around 125°C , may
probably be by galvanic effect . The remedy would be either to provide complete
insulation between aluminium and mild steel or to change over completely to ...
Page 32
Table 3 gives the operating conditions at which several failures took place . Table
3 Data of Stress Corrosion Failure : Case Histories pH of Thickness 0 . 016 "
Operating Temp . °F Pressure psi 780 310 Corrodent Chloride Corrodent conc .
Table 3 gives the operating conditions at which several failures took place . Table
3 Data of Stress Corrosion Failure : Case Histories pH of Thickness 0 . 016 "
Operating Temp . °F Pressure psi 780 310 Corrodent Chloride Corrodent conc .
Page 95
... steel cannot be used in the separation systems . If batch operations , i . e . ,
settling , water washing , and sometimes caustic neutralization , are all done in
the same vessel , treating tanks of monel or monel - lined steel are commonly
used .
... steel cannot be used in the separation systems . If batch operations , i . e . ,
settling , water washing , and sometimes caustic neutralization , are all done in
the same vessel , treating tanks of monel or monel - lined steel are commonly
used .
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Contents
INTRODUCTION | 3 |
CHEMICAL CORROSION AND ITS PREVENTION | 13 |
DISCUSSION | 22 |
9 other sections not shown
Common terms and phrases
addition alloys aluminium ammonia ammonium amount anodic application attack bottom carbon steel cast iron cathodic protection cause chemical chloride chromium coatings concentration construction containing cooling corrosion problems corrosion rate cracking crude developed distillation effective environment epoxy equipment exchangers failure fertiliser flow give given handling heat hydrogen hydrogen sulphide increase industry inhibitor iron lead less material metal method mild steel Monel months natural observed occurred operating organic oxide oxygen paint petroleum phosphate pipe pitting plant plates potential practice presence pressure prevent pumps range reaction reduced refinery removal resistance rubber severe shell showing solution specially stainless steel steam storage tanks stress corrosion structure suitable sulphuric acid surface Table tanks temperature tests thickness tower treatment tubes unit various welding zinc