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 23
Page 42
Regarding the use of different constructional materials the author describes that
natural and synthetic rubber lined steel resist the corrosive action of ammonium
sulphate upto 75°C , butyl rubber upto 100°C and neoprene rubber upto 150°C ...
Regarding the use of different constructional materials the author describes that
natural and synthetic rubber lined steel resist the corrosive action of ammonium
sulphate upto 75°C , butyl rubber upto 100°C and neoprene rubber upto 150°C ...
Page 54
chloride or rubber lined steel piping . From the last reactor the crude phosphoric
acid is transfered to the filter by rubber - lined pumps and through vinylidene
chloride - lined steel piping . While natural rubber - linings were satisfactory
under ...
chloride or rubber lined steel piping . From the last reactor the crude phosphoric
acid is transfered to the filter by rubber - lined pumps and through vinylidene
chloride - lined steel piping . While natural rubber - linings were satisfactory
under ...
Page 76
AISI 304 Lined hard rubber 12 months 12 to 14 months P - 502 - Reclaim Water
Pump Casing Hard rubber lined AISI 316 12 to 14 months Shaft , sleeve and
impeller 3 Original material used Description Working period . months . P - 204
Flash ...
AISI 304 Lined hard rubber 12 months 12 to 14 months P - 502 - Reclaim Water
Pump Casing Hard rubber lined AISI 316 12 to 14 months Shaft , sleeve and
impeller 3 Original material used Description Working period . months . P - 204
Flash ...
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