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FERTILIZER INDUSTRY LECTURE 1
INTRODUCTION ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
The Manufacturing Process Nitrogen fertilizers ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
The NPK Manufacturing Process Nitrogen fertilizers (contd.) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
The NPK Manufacturing Process Phosphatic fertilizer:  ,[object Object],[object Object],[object Object],[object Object],[object Object],1) Superphosphate:
The NPK Manufacturing Process ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Composite fertilizer manufacture:
The NPK Manufacturing Process ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
AMMONIA  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Ammonia (mol%) in equilibrium synthesis gas; H 2 /N 2  =3mol/mol
AMMONIA SYNTHESIS REACTORS  ,[object Object],[object Object],[object Object]
ICI quench reactor Temperature-Concentration profile
Kellogg a) Vertical (left fig.)  b) Horizontal (right fig.) quench reactors
Haldor Topsoe radial flow reactors
Multi-bed converter with indirect cooling; (a) catalyst, (b) feed-effluent heat exchanger, (c) cold bypass, (f) product.
Integrated Ammonia Plant
Specific energy requirements of various ammonia processes *Lower heating value Process GJ (LHV)*/t ammonia Classical Haber-Bosch (coke) 80-90 Reformer pressure 5-10 bar (1953-1955) 47-53 Reformer pressure 30-35 bar (1965-1975) 33-42 Low-energy concepts  (1975-1984) 27-33 State of the art (since 1991) 24-26

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