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 37
Page 29
Hydrogen Sulphide removal In the processing of the coke oven or other gases , it
is essential that hydrogen sulphide and carbon dioxide from the gas be removed
before the gases are sent for reformation . For hydrogen sulphide removal ...
Hydrogen Sulphide removal In the processing of the coke oven or other gases , it
is essential that hydrogen sulphide and carbon dioxide from the gas be removed
before the gases are sent for reformation . For hydrogen sulphide removal ...
Page 30
Carbon dioxide removal Carbon dioxide is scrubbed from the coke oven gas by
ammonia liquor and the enriched gas is further regenerated by stripping with
steam at about 90°C . Severe corrosion of the equipment has been observed in
this ...
Carbon dioxide removal Carbon dioxide is scrubbed from the coke oven gas by
ammonia liquor and the enriched gas is further regenerated by stripping with
steam at about 90°C . Severe corrosion of the equipment has been observed in
this ...
Page 33
Carbon dioxide and trace amounts of hydrogen sulphide can be removed by
many scrubbing solutions , some of which are ... CO , removal by water washing
Several cases of corrosion attack and failures have been reported in removal of ...
Carbon dioxide and trace amounts of hydrogen sulphide can be removed by
many scrubbing solutions , some of which are ... CO , removal by water washing
Several cases of corrosion attack and failures have been reported in removal of ...
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