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OVERVIEW OF THE
FERTILIZER INDUSTRY-
AMMONIA AND UREA
USMAN SULEIMAN UBAM
WHY FERTILIZER
 Plants needs nutrients to grow
 Nutrients have specific and essential functions in plant
metabolism
 Lack of nutrient limits plant growth.
WHY FERTILIZER
Plant Nutrients
PLANT NUTRITION
16%
23%
61%
Primary Benefit Nutrient Characterization
K
P
N
• Improve crop quality
• Annual application is not
required
Fewer Suppliers
• Improve crop size
• Most important and
commonly lacking
nutrients.
• Annual Application is
critical
• Industry are more
fragmented, under
consolidation.
• More dynamic prices but
stable volume.
• Improve crop quality
• Annual application is not
required
Fewer Suppliers
FERTILIZER INDUSTRIES
Ammonia Plant
Sulphuric Acid Plant
Phosphoric Acid Plant
Nitric Acid Plant
Nitrosphosphorous Plant
Natural Gas
Steam
Air
Urea
Ammonia Nitrate
Calcium Nitrate
NPK Fertilizer
DAP/MAP
NH3
CO2
HNO3
Rock
Air
Rock
Rock
H2SO4
Triple Super Phosphate
H2PO4
Salts of K, Mg, S
Rock
.
.
UREA FERTILIZER PRODUCTION
 Urea (NH2CONH2) is produced from the reaction of
Ammonia (NH3) and carbon dioxide (CO2).
 Blue Ammonia is produced from Natural Gas with CO2
as a byproduct.
BLUE AMMONIA PROCESS
REFORMING
WATER-GAS
SHIFT REACTION
CO2 REMOVAL
METHANATION
AMMONIA
SYNTHESIS
REFRIGERATION
Natural
Gas
Steam
Air
Syn-Gas Syn-Gas
CO2
CO2 to Urea Plant
Syn-Gas
Syn-Gas
NH3
NH3 to Urea Plant
DESULFURIZATION
H2
NG
Blue Ammonia Production Process
Desulfization
Converts organic sulfur from the natural gas to inorganic
sulfur and removes it from the natural gas feed.
CH4S(g) + H2(g) = CH4(g) + H2S(g). Hydrotreating
 H2S(g) + ZnO(g) = ZnS(g) + H2O(g). Desulfurization
Blue Ammonia Production Process
Reforming
Produces synthesis gas (syn-gas) from Natural Gas either by
steam reforming, partial oxidation, or authothermal reforming.
Nitrogen is also injected in the reforming section (Secondary
Reforming). Reforming reactions are carried out in the
presence of Nickel Catalyst.
CH4(g) + H2O(g) = CO(g) + 3H2(g). Steam Reforming
Reversible and Endothermic.
 CH4(g) + ½O2(g) = CO(g) + 2H2(g). Partial Oxidation
Reversible and Endothermic.
 Autothermal Reforming combines SMR and POX.
Blue Ammonia Production Process
Water Gas Shift Reaction
Produces synthesis gas (syn-gas) from carbon monoxide
and steam with CO2 as byproduct.
CO(g) + H2O(g) = CO2(g) + H2(g).
Water Gas shift reaction takes places at high and lower
temperature. The high temperature water gas shift
reaction is carried out in the presence of Iron catalyst,
while the low temperature shift is carried out in the
presence of Copper Catalyst.
Blue Ammonia Production Process
CO2 Removal
This process scrubs the CO2 from the synthesis gas.
CO2 absorption or CO2 adsorption are the predominant
methods adopted. CO2 absorption is predominantly
performed with the use of amines or potassium
carbonate (Belfing Solution). CO2 adsorption is
predominantly carried out by zeolites.
Blue Ammonia Production Process
Methanation
Methanation reaction converts the unreacted carbon
monoxide and carbon dioxide to methane.
CO2(g) + 3H2(g) = CH4(g) + H2O(g)
CO(g) + 4H2(g) = CH4(g) + 2H2O(g)
Blue Ammonia Production Process
Ammonia Synthesis
Ammonia synthesis reacts hydrogen with nitrogen to
produce ammonia at higher pressure. The reaction is
highly exothermic.
3H2 + N2 = 2NH3
Blue Ammonia Production Technologies
 KBR Purifier Ammonia
 Haldor Topsoe
Thyssenkrupp-Uhde Dual Pressure Ammonia
Casale
Linde Ammonia Concept
Blue Ammonia Production Technologies
KBR-Purifier Ammonia
Blue Ammonia Production Technologies
Haldor-Topsoe Ammonia Process
Blue Ammonia Production Technologies
Thyssenkrupp-Uhde Ammonia Synthesis Process
UREA PROCESS
SYNTHESIS
PURIFICATION
CONCENTRATION
GRANULATION
PRILLING
CO2 NH3
Urea + Ammonia Carbamate + Water
Urea + Water
Urea
Urea Product
Urea Production Process
 Synthesis Section
Urea is synthesized from CO2 and NH3 at a very high
pressure (150 bar).
CO2(g) + 2NH3(l) = NH3COONH3(l)
CO2(g) + 2NH3(l) = NH2CONH2(l) + H2O(l)
Urea Production Process
 Purification
Purification decomposes the Ammonium Carbamate to Urea
and Water. Decomposition is carried out at high pressure
and at lower pressure.
NH3COONH3(l) = NH2CONH2+ H2O(l)
Urea Production Process
 Concentration
To concentrate the Urea, the water is evaporated from an
evaporator. Concentration is carried out at vacuum
condition.
Blue Ammonia Production Technologies
 Granulation/Prilling
The concentrated Urea is solidified either by granulation
(crystallizes to granules), or by prilling (crystallizes to
prilling).
Urea Production Technologies
 Stami Carbon (CO2 Stripping)
 Snam Progetti (NH3 Stripping)
Advanced Cost & Energy Saving Process (ACES21)-CO2
stripping
 Isobaric Double Recycle Process (IDR)
Urea Production Technologies
ACES21 Process (CO2 Stripping)
Urea Production Technologies
Snam Progetti Process (Ammonia Stripping)
QUESTIONS

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Fertilizer production by indorama fertilizer co.pptx

  • 1. OVERVIEW OF THE FERTILIZER INDUSTRY- AMMONIA AND UREA USMAN SULEIMAN UBAM
  • 2. WHY FERTILIZER  Plants needs nutrients to grow  Nutrients have specific and essential functions in plant metabolism  Lack of nutrient limits plant growth.
  • 4. PLANT NUTRITION 16% 23% 61% Primary Benefit Nutrient Characterization K P N • Improve crop quality • Annual application is not required Fewer Suppliers • Improve crop size • Most important and commonly lacking nutrients. • Annual Application is critical • Industry are more fragmented, under consolidation. • More dynamic prices but stable volume. • Improve crop quality • Annual application is not required Fewer Suppliers
  • 5. FERTILIZER INDUSTRIES Ammonia Plant Sulphuric Acid Plant Phosphoric Acid Plant Nitric Acid Plant Nitrosphosphorous Plant Natural Gas Steam Air Urea Ammonia Nitrate Calcium Nitrate NPK Fertilizer DAP/MAP NH3 CO2 HNO3 Rock Air Rock Rock H2SO4 Triple Super Phosphate H2PO4 Salts of K, Mg, S Rock . .
  • 6. UREA FERTILIZER PRODUCTION  Urea (NH2CONH2) is produced from the reaction of Ammonia (NH3) and carbon dioxide (CO2).  Blue Ammonia is produced from Natural Gas with CO2 as a byproduct.
  • 7. BLUE AMMONIA PROCESS REFORMING WATER-GAS SHIFT REACTION CO2 REMOVAL METHANATION AMMONIA SYNTHESIS REFRIGERATION Natural Gas Steam Air Syn-Gas Syn-Gas CO2 CO2 to Urea Plant Syn-Gas Syn-Gas NH3 NH3 to Urea Plant DESULFURIZATION H2 NG
  • 8. Blue Ammonia Production Process Desulfization Converts organic sulfur from the natural gas to inorganic sulfur and removes it from the natural gas feed. CH4S(g) + H2(g) = CH4(g) + H2S(g). Hydrotreating  H2S(g) + ZnO(g) = ZnS(g) + H2O(g). Desulfurization
  • 9. Blue Ammonia Production Process Reforming Produces synthesis gas (syn-gas) from Natural Gas either by steam reforming, partial oxidation, or authothermal reforming. Nitrogen is also injected in the reforming section (Secondary Reforming). Reforming reactions are carried out in the presence of Nickel Catalyst. CH4(g) + H2O(g) = CO(g) + 3H2(g). Steam Reforming Reversible and Endothermic.  CH4(g) + ½O2(g) = CO(g) + 2H2(g). Partial Oxidation Reversible and Endothermic.  Autothermal Reforming combines SMR and POX.
  • 10. Blue Ammonia Production Process Water Gas Shift Reaction Produces synthesis gas (syn-gas) from carbon monoxide and steam with CO2 as byproduct. CO(g) + H2O(g) = CO2(g) + H2(g). Water Gas shift reaction takes places at high and lower temperature. The high temperature water gas shift reaction is carried out in the presence of Iron catalyst, while the low temperature shift is carried out in the presence of Copper Catalyst.
  • 11. Blue Ammonia Production Process CO2 Removal This process scrubs the CO2 from the synthesis gas. CO2 absorption or CO2 adsorption are the predominant methods adopted. CO2 absorption is predominantly performed with the use of amines or potassium carbonate (Belfing Solution). CO2 adsorption is predominantly carried out by zeolites.
  • 12. Blue Ammonia Production Process Methanation Methanation reaction converts the unreacted carbon monoxide and carbon dioxide to methane. CO2(g) + 3H2(g) = CH4(g) + H2O(g) CO(g) + 4H2(g) = CH4(g) + 2H2O(g)
  • 13. Blue Ammonia Production Process Ammonia Synthesis Ammonia synthesis reacts hydrogen with nitrogen to produce ammonia at higher pressure. The reaction is highly exothermic. 3H2 + N2 = 2NH3
  • 14. Blue Ammonia Production Technologies  KBR Purifier Ammonia  Haldor Topsoe Thyssenkrupp-Uhde Dual Pressure Ammonia Casale Linde Ammonia Concept
  • 15. Blue Ammonia Production Technologies KBR-Purifier Ammonia
  • 16. Blue Ammonia Production Technologies Haldor-Topsoe Ammonia Process
  • 17. Blue Ammonia Production Technologies Thyssenkrupp-Uhde Ammonia Synthesis Process
  • 18. UREA PROCESS SYNTHESIS PURIFICATION CONCENTRATION GRANULATION PRILLING CO2 NH3 Urea + Ammonia Carbamate + Water Urea + Water Urea Urea Product
  • 19. Urea Production Process  Synthesis Section Urea is synthesized from CO2 and NH3 at a very high pressure (150 bar). CO2(g) + 2NH3(l) = NH3COONH3(l) CO2(g) + 2NH3(l) = NH2CONH2(l) + H2O(l)
  • 20. Urea Production Process  Purification Purification decomposes the Ammonium Carbamate to Urea and Water. Decomposition is carried out at high pressure and at lower pressure. NH3COONH3(l) = NH2CONH2+ H2O(l)
  • 21. Urea Production Process  Concentration To concentrate the Urea, the water is evaporated from an evaporator. Concentration is carried out at vacuum condition.
  • 22. Blue Ammonia Production Technologies  Granulation/Prilling The concentrated Urea is solidified either by granulation (crystallizes to granules), or by prilling (crystallizes to prilling).
  • 23. Urea Production Technologies  Stami Carbon (CO2 Stripping)  Snam Progetti (NH3 Stripping) Advanced Cost & Energy Saving Process (ACES21)-CO2 stripping  Isobaric Double Recycle Process (IDR)
  • 24. Urea Production Technologies ACES21 Process (CO2 Stripping)
  • 25. Urea Production Technologies Snam Progetti Process (Ammonia Stripping)