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 16
Page 6
( 1 ) Corrosion in plants producing crude synthesis gas , e . g . , corrosion in
electrolysers in an electrolysis hydrogen plant , corrosion in reformation plants
prod ucing nitrogen hydrogen mixture by interaction of coke oven gas ( or
naphtha or ...
( 1 ) Corrosion in plants producing crude synthesis gas , e . g . , corrosion in
electrolysers in an electrolysis hydrogen plant , corrosion in reformation plants
prod ucing nitrogen hydrogen mixture by interaction of coke oven gas ( or
naphtha or ...
Page 87
Napthenic acid corrosion is encountered mainly in crude distilling plants and in
high vacuum distilling plants processing certain sour crudes or derivatives
thereof . The equipment chiefly affected include hot oil centrifugal pumps ,
furnaces ...
Napthenic acid corrosion is encountered mainly in crude distilling plants and in
high vacuum distilling plants processing certain sour crudes or derivatives
thereof . The equipment chiefly affected include hot oil centrifugal pumps ,
furnaces ...
Page 111
Air - fin type of condenser tubes Within a period of 2 years of operation , many of
the tubes in the crude overhead air - fin condensers developed leaks which are
still occurring . Hydrocarbon vapour and steam leave the top of crude fractionator
...
Air - fin type of condenser tubes Within a period of 2 years of operation , many of
the tubes in the crude overhead air - fin condensers developed leaks which are
still occurring . Hydrocarbon vapour and steam leave the top of crude fractionator
...
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