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 5
As a general rule , corrosion cannot be completely arrested without the
expenditure of energy ( cathodic protection ) because of the energy relationship
between metal and its corrosion products . Fortunately , the corrosion rate can be
lowered ...
As a general rule , corrosion cannot be completely arrested without the
expenditure of energy ( cathodic protection ) because of the energy relationship
between metal and its corrosion products . Fortunately , the corrosion rate can be
lowered ...
Page 36
Proceedings of Short Course on "Corrosion in Fertiliser and Petroleum Industry"
Organised by the Corrosion Advisory ... But during the next several months
corrosion occurred at an alarming rate in several areas e . g . in amine to amine ...
Proceedings of Short Course on "Corrosion in Fertiliser and Petroleum Industry"
Organised by the Corrosion Advisory ... But during the next several months
corrosion occurred at an alarming rate in several areas e . g . in amine to amine ...
Page 38
corrosion of reboiler and heat exchanger tube bundles where the temperature
was highest and the uninhibited corrosion rate was also the highest . In the
temperature range of 220°F to 280°F , it is probable that the mechanism of
passivation is ...
corrosion of reboiler and heat exchanger tube bundles where the temperature
was highest and the uninhibited corrosion rate was also the highest . In the
temperature range of 220°F to 280°F , it is probable that the mechanism of
passivation is ...
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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
Bibliographic information
| Title | 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 |
| Editors | K. N. P. Rao, A. K. Lahiri |
| Contributor | Corrosion Advisory Bureau |
| Publisher | Corrosion Advisory Bureau, 1969 |
| Original from | the University of Wisconsin - Madison |
| Digitized | 27 Feb 2008 |
| Length | 159 pages |
| Export Citation | BiBTeX EndNote RefMan |