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 21
Page 71
DISCUSSION Mr . R . S . Raman ( E . I . D . Parry , Madras ) In our phosphoric
acid plant the rock phosphate and sulphuric acid of 70 % concentration are
agitated in vats . Due to the presence of the acid and chloride , the rotar vanes
made of ...
DISCUSSION Mr . R . S . Raman ( E . I . D . Parry , Madras ) In our phosphoric
acid plant the rock phosphate and sulphuric acid of 70 % concentration are
agitated in vats . Due to the presence of the acid and chloride , the rotar vanes
made of ...
Page 138
Phosphate - Organic Chromate — Soluble zinc organic . Polyphosphate complex
cyanide . Chromate - phosphate mixture . 1 and 6 are open market ... The pH
range required with the phosphate is of the order 5 . 8 to 6 . 3 . - cics toi I loro o ...
Phosphate - Organic Chromate — Soluble zinc organic . Polyphosphate complex
cyanide . Chromate - phosphate mixture . 1 and 6 are open market ... The pH
range required with the phosphate is of the order 5 . 8 to 6 . 3 . - cics toi I loro o ...
Page 153
Regarding mixed chromate / phosphate inhibitor I would like to mention that if
water is flowing the quantity of ... only important point is that the ratio of calcium
and phosphate is to be maintained and as long as the calcium content is not too
low ...
Regarding mixed chromate / phosphate inhibitor I would like to mention that if
water is flowing the quantity of ... only important point is that the ratio of calcium
and phosphate is to be maintained and as long as the calcium content is not too
low ...
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