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 22
Page 45
In tube sheet with top half cooled and bottom half heated to approximately 900°F
, the acid condenses in the top sector and runs down to the bottom , corrosion
zone being located in the area where the temperature of the metal is above the ...
In tube sheet with top half cooled and bottom half heated to approximately 900°F
, the acid condenses in the top sector and runs down to the bottom , corrosion
zone being located in the area where the temperature of the metal is above the ...
Page 88
As the alloys most resistant to acid corrosion are not frequently resistant to high
temperature attack , it is common practice to line the top and bottom portions of
distillation towers with different materials to obtain the most favourable
performance ...
As the alloys most resistant to acid corrosion are not frequently resistant to high
temperature attack , it is common practice to line the top and bottom portions of
distillation towers with different materials to obtain the most favourable
performance ...
Page 144
Despite provision for drainage at the bottom of the large tanks , the unevenness
of the bottom plate ensures the presence of water causing corrosion . The bottom
of the tank is generally cement lined , which is supplemented with cathodic ...
Despite provision for drainage at the bottom of the large tanks , the unevenness
of the bottom plate ensures the presence of water causing corrosion . The bottom
of the tank is generally cement lined , which is supplemented with cathodic ...
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
Bibliographic information
| Title | 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 |
| Editors | K. N. P. Rao, A. K. Lahiri |
| Contributor | Corrosion Advisory Bureau |
| Publisher | Corrosion Advisory Bureau, 1969 |
| Original from | the University of Wisconsin - Madison |
| Digitized | 27 Feb 2008 |
| Length | 159 pages |
| Export Citation | BiBTeX EndNote RefMan |