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 1968K. N. P. Rao, A. K. Lahiri |
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Page 3
... readily available and their use cannot be economically justified , in many cases . Our aim , therefore , should be to have a compromise selection of the best material one can obtain , reinforced by the best protective scheme one can ...
... readily available and their use cannot be economically justified , in many cases . Our aim , therefore , should be to have a compromise selection of the best material one can obtain , reinforced by the best protective scheme one can ...
Page 19
... readily as carbon steels . Carbon content has also been shown to have quite a marked effect in carbon steels . The maximum tendency to cracking is found at carbon content of 0.1-0.15 % . With increase or de- crease in carbon content the ...
... readily as carbon steels . Carbon content has also been shown to have quite a marked effect in carbon steels . The maximum tendency to cracking is found at carbon content of 0.1-0.15 % . With increase or de- crease in carbon content the ...
Page 136
... readily oxidise nitrite to nitrate which has no inhibitive action . Nitrite has practically no inhibiting action on the corrosion of brass . Stress corrosion cracking of brass may take place in the presence of nitrite because of the ...
... readily oxidise nitrite to nitrate which has no inhibitive action . Nitrite has practically no inhibiting action on the corrosion of brass . Stress corrosion cracking of brass may take place in the presence of nitrite because of the ...
Contents
INTRODUCTION | 3 |
CHEMICAL CORROSION AND ITS PREVENTION | 13 |
CORROSION PROBLEMS IN THE MANUFACTURE OF NITROGEN BASED FERTILIZER | 27 |
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 formation give given handling heat higher hydrogen hydrogen sulphide increase industry inhibitor iron lead 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