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 29
The processes of greatest current interest are non - catalytic partial oxidation and
catalytic steam hydrocarbon reforming . ... A case of corrosion in such systems is
described below : In the fertiliser factory at Sindri iron oxide is used for the ...
The processes of greatest current interest are non - catalytic partial oxidation and
catalytic steam hydrocarbon reforming . ... A case of corrosion in such systems is
described below : In the fertiliser factory at Sindri iron oxide is used for the ...
Page 98
( c ) Condensate Corrosion Carbon - di - oxide combined with water causes
corrosion in the refining processes . Carbondi - oxide may come from two
sources :i ) from the decomposition of bicarbonates contained in or added to the
crude oil , or ...
( c ) Condensate Corrosion Carbon - di - oxide combined with water causes
corrosion in the refining processes . Carbondi - oxide may come from two
sources :i ) from the decomposition of bicarbonates contained in or added to the
crude oil , or ...
Page 149
The most widely used pigments are aluminium , ironoxide , micaceous iron oxide
, graphite , leaded zinc oxide , zinc oxide , white lead and titanium dioxide . While
for the prime coat importance is given on pigments having corrosion inhibitive ...
The most widely used pigments are aluminium , ironoxide , micaceous iron oxide
, graphite , leaded zinc oxide , zinc oxide , white lead and titanium dioxide . While
for the prime coat importance is given on pigments having corrosion inhibitive ...
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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