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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Results 1-3 of 16
Page 34
A 9 ft . to 11 ft . level of water was kept in the tower by an automatic control device
. The gas entered the tower at a pressure of 250 p . s . i ; the temperature varied
from 39°F to 87°F . The material of construction was ASTM - A70 ( ASTM - A ...
A 9 ft . to 11 ft . level of water was kept in the tower by an automatic control device
. The gas entered the tower at a pressure of 250 p . s . i ; the temperature varied
from 39°F to 87°F . The material of construction was ASTM - A70 ( ASTM - A ...
Page 50
Gas washers are lead lined with bricks to protect the metal from temperatures of
450 – 500°C . The tower top is water cooled to 80° - 90°C . Towers are made of
hardened steel to give them structural stability . The 65 % wash acid leaving the ...
Gas washers are lead lined with bricks to protect the metal from temperatures of
450 – 500°C . The tower top is water cooled to 80° - 90°C . Towers are made of
hardened steel to give them structural stability . The 65 % wash acid leaving the ...
Page 52
Another corrosion failure 59 of a 22 " pipe which connects two SO3 absorbers
occurred in the same plant . SO3 - rich gases were admitted to first tower down
which flowed oleum and the substantially exhausted gases passed through the
main ...
Another corrosion failure 59 of a 22 " pipe which connects two SO3 absorbers
occurred in the same plant . SO3 - rich gases were admitted to first tower down
which flowed oleum and the substantially exhausted gases passed through the
main ...
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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