Fertiliser Technology
Prilling of urea should be accomplished (in a sprayer) just above the melting point of urea with minimum of retention time, otherwise it will result in

Substantially wet non-flowing and sticky product
Non-spherical prills
Low bulk density product
Biuret formation

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Fertiliser Technology
Multistage operation (as in the case of catalytic oxidation of SO₂) is not carried out for NH₃ synthesis, because of

Chances of entrainment and disturbance of catalyst bed
Higher pumping cost
High cost of the high pressure vessel used for the reactor
Comparatively higher pressure drop

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