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 46
The best tank for 83 % ammonium nitratc would be with a bottom of purest
aluminium probably 3003 with sides of 5052 because of its superior tensile
strength . Gachenbach42 has described the use of reinforced plastics for the
flooring in a ...
The best tank for 83 % ammonium nitratc would be with a bottom of purest
aluminium probably 3003 with sides of 5052 because of its superior tensile
strength . Gachenbach42 has described the use of reinforced plastics for the
flooring in a ...
Page 74
I would like to know if you have got any experience in the use of aluminium
anode for protection in such case . Mr . Landucci ( Cominco Binani Zinc Ltd . ,
Udyogamandal ) I do not have any practical experience in the use of aluminium
anodes ...
I would like to know if you have got any experience in the use of aluminium
anode for protection in such case . Mr . Landucci ( Cominco Binani Zinc Ltd . ,
Udyogamandal ) I do not have any practical experience in the use of aluminium
anodes ...
Page 116
COMPOSITE ALUMINIUM PRIMER the ideal choice for protection of steel
Aluminium paste for primers and finishing paints is made by Indal . Ask Indal for
application instructions . Composite aluminium primer to Indian Standard
Specification ...
COMPOSITE ALUMINIUM PRIMER the ideal choice for protection of steel
Aluminium paste for primers and finishing paints is made by Indal . Ask Indal for
application instructions . Composite aluminium primer to Indian Standard
Specification ...
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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