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 |
From inside the book
Results 1-3 of 31
Page 33
Failure occurred within two weeks . Surging of the drum level carried over drum
solids into the flex hoses . Case B : Flex hose sheathing . Stress corrosion failure
of the sheathing occurred as a consequence of atmospheric conditions .
Failure occurred within two weeks . Surging of the drum level carried over drum
solids into the flex hoses . Case B : Flex hose sheathing . Stress corrosion failure
of the sheathing occurred as a consequence of atmospheric conditions .
Page 44
As the failures had mostly occurred near - about the welds it was apparent that
welding stresses and the corrosive environment containing chloride were
responsible for the failure . It may also be noted that evaporator ' U ' bends had to
bear ...
As the failures had mostly occurred near - about the welds it was apparent that
welding stresses and the corrosive environment containing chloride were
responsible for the failure . It may also be noted that evaporator ' U ' bends had to
bear ...
Page 51
Hastelloy alloy D was not found suitable and all the failures occurred near the
tank liquid level . It was found that the heat of dilution resulting from the mixing of
the acids was responsible for the attack . Temperature rose to about 260 F , and ...
Hastelloy alloy D was not found suitable and all the failures occurred near the
tank liquid level . It was found that the heat of dilution resulting from the mixing of
the acids was responsible for the attack . Temperature rose to about 260 F , and ...
What people are saying - Write a review
We haven't found any reviews in the usual places.
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