Process and plant for urea production
View Patent ↗A process for producing urea is disclosed, wherein liquid ammonia and carbon dioxide are reacted in a high-pressure synthesis section ( 100 ), and at least part of the carbon dioxide is fed to said synthesis section ( 100 ) in liquid phase. A plant operating according to said process and a method for modernizing existing plants accordingly are also disclosed.
1. A process for producing urea, comprising the steps of:
feeding liquid ammonia and carbon dioxide to a synthesis section comprising at least a reactor, a stripper and a condenser forming a high-pressure loop; and
reacting said liquid ammonia and carbon dioxide in said synthesis section to produce urea,
wherein at least part of said carbon dioxide is fed to said synthesis section in liquid phase.
2. The process according to claim 1 , wherein a part of said carbon dioxide is fed to the synthesis section in liquid phase and the remaining part is fed to the synthesis section in gaseous phase.
3. The process according to claim 1 , wherein the full carbon dioxide input to said synthesis section is in liquid state.
4. The process according to claim 1 , wherein said synthesis section comprises a reactor, a stripper and a condenser, and said liquid carbon dioxide is fed either to said reactor or to said condenser.
5. The process according to claim 1 , wherein said synthesis section comprises a reactor, a stripper and a condenser; a part of said liquid carbon dioxide is fed to the reactor, and a part of the liquid carbon dioxide is fed to the condenser.
6. The process according to claim 1 , wherein said liquid carbon dioxide is mixed with at least part of said liquid ammonia, obtaining a liquid mixture which is fed to said synthesis section.
7. A plant for producing urea with a process according to claim 1 , said plant comprising at least:
a synthesis section comprising at least a reactor, a stripper and a condenser forming a high-pressure loop; and
feeding means providing an input of fresh ammonia and an input of fresh carbon dioxide to said synthesis section;
wherein said feeding means are adapted to feed at least part of said fresh carbon dioxide input to said synthesis section in liquid phase.
8. The plant according to claim 7 , further comprising mixing means disposed to mix said input of liquid carbon dioxide with at least part of said input of liquid ammonia.
9. The plant according to claim 8 , wherein said mixing means comprise a nozzle comprising a first portion with separate coaxial ducts for liquid carbon dioxide and liquid ammonia, and a second mixing portion wherein liquid carbon dioxide and ammonia are mixed.
10. The plant according to claim 9 , wherein said nozzle comprises an external duct and an internal, coaxial duct; the internal duct has a convergent outlet substantially corresponding to a convergent portion of the external duct, obtaining a mixing zone with decreasing cross section in the axial direction, said mixing zone of the nozzle being followed by a constant cross-section portion and a divergent to slow down the liquid mixture.
11. A method for improving efficiency of a plant for producing urea, said plant being a self-stripping or CO 2 -stripping plant comprising at least a synthesis section comprising a reactor, a stripper and a condenser in a high-pressure loop, connected to ammonia feeding means and gaseous carbon dioxide feeding means, said method comprising providing liquid carbon dioxide feeding means connected to said synthesis section.
12. The method according to claim 11 , further comprising mixing means adapted to mix an input of liquid ammonia with an input of liquid carbon dioxide and feed the resulting liquid mixture to said synthesis section.
13. The method according to claim 11 , wherein liquid carbon dioxide feeding means are provided to feed liquid carbon dioxide to said reactor and/or said condenser.