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
Prior to 1950 reforming took place at essentially atmospheric pressure at the
outlet of the reaction zone . Although the equilibrium is favoured by low pressure ,
overall economics favour a high pressure by - product hydrogen . The processes
of ...
Prior to 1950 reforming took place at essentially atmospheric pressure at the
outlet of the reaction zone . Although the equilibrium is favoured by low pressure ,
overall economics favour a high pressure by - product hydrogen . The processes
of ...
Page 34
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 - 285
) fire box quality steel plate and the tower was packed with raschig rings .
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 - 285
) fire box quality steel plate and the tower was packed with raschig rings .
Page 35
2 , H2S - Traces is compressed to a pressure of 280 lbs / sq . inch and sent to
water scrubbers for the scrubbing of CO2 with water . In one of these scrubbers
some blisters were observed on the inside surface of the shell plate in an area ...
2 , H2S - Traces is compressed to a pressure of 280 lbs / sq . inch and sent to
water scrubbers for the scrubbing of CO2 with water . In one of these scrubbers
some blisters were observed on the inside surface of the shell plate in an area ...
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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