Urea stripping process for the production of urea

Patent metadata

Field	Value
Publication number	US-9447032-B2
Application number	US-201113504121-A
Country	US
Kind code	B2
Filing date	Jan 7, 2011
Priority date	Jan 7, 2010
Publication date	Sep 20, 2016
Grant date	Sep 20, 2016

Abstract

The invention relates to a process for producing urea wherein an aqueous urea solution, leaving a urea reaction zone is fed to a stripper, where a part of the non-converted ammonia and carbon dioxide is separated from the aqueous urea solution, which solution leaves the stripper to a first recovery section of one or more serial recovery sections and is subsequently fed to one or more urea concentration sections, wherein the urea solution leaving the stripper is subjected to an adiabatic expansion, thus creating a vapor and a liquid, which are separated before the liquid enters a first recovery section and the vapor is condensed. The invention further relates to a urea plant comprising a stripper and a first recovery section, wherein an adiabatic expansion valve and a liquid/gas separator is provided between the stripper and the first recovery section.

First claim

The invention claimed is:

1. A process for producing urea by converting ammonia and carbon dioxide to urea wherein an aqueous urea solution containing non converted ammonia and carbon dioxide, leaving a urea reaction zone is fed to a stripper,
wherein in said stripper part of the non-converted ammonia and carbon dioxide is separated from the aqueous urea solution, which urea solution leaves the stripper to a first recovery section of one or more serial recovery sections and is subsequently fed to one or more urea concentration sections,
wherein the urea solution leaving the stripper is subjected to an adiabatic expansion, thus creating a vapor and a liquid, which are separated before the liquid enters a first recovery section and the vapor is condensed, and
wherein the heat released from the condensation of the vapor resulting from said expansion is used for heating downstream in the process,
wherein the first recovery section is operated at a pressure of 0.1-1 MPa; and/or
wherein the pressure of the vapor after the adiabatic expansion is at least 0.2 MPa higher than the pressure in the first recovery system.

2. A process according to claim 1 , wherein the first recovery section is operated at a pressure of 0.1-1 MPa.

3. A process according to claim 1 , wherein the adiabatic expansion results in a pressure drop of at least 0.5 MPa.

4. A process according to claim 1 , wherein the pressure of the vapor after the adiabatic expansion is at least 0.2 MPa higher than the pressure in the first recovery system.

5. A process according to claim 1 , wherein the heat released during condensation of the vapor is used for concentrating a urea solution in one or more of the urea concentration sections.

6. A process according to claim 1 , wherein the released condensation heat of the formed vapor by the adiabatic expansion step is used for heating the urea solution in one or more downstream urea recovery sections.

7. A process according to claim 1 , wherein the heating downstream in the process is selected from the group consisting of
heating in one downstream recovery section,
heating in a plurality of downstream recovery sections,
for concentrating the urea solution in one of the urea concentration sections,
for concentrating the urea solution in a plurality of urea concentration sections, and combinations thereof.

8. An improved method for preparing urea by increasing the capacity of an existing urea process wherein said process comprises
converting ammonia and carbon dioxide to urea wherein an aqueous urea solution containing non converted ammonia and carbon dioxide, leaving a urea reaction zone is fed to a stripper,
wherein in said stripper part of the non-converted ammonia and carbon dioxide is separated from the aqueous urea solution,
which urea solution leaves the stripper to a first recovery section of one or more serial recovery sections and is subsequently fed to one or more urea concentration sections, and
wherein the improvement comprises subjecting the urea solution leaving the stripper to an adiabatic expansion, thus creating a vapor and a liquid, which are separated before the liquid enters a first recovery section and the vapor is condensed, whereby heat is released; and
wherein the first recovery section is operated at a pressure of 0.1-1 MPa.

9. A method according to claim 8 , wherein the heat released from the condensation of the vapor resulting from said expansion is used for heating downstream in the process.

10. A urea plant comprising a stripper and a recovery section, which recovery section comprises a condensor, wherein an adiabatic expansion valve and a liquid/gas separator are provided between the stripper and the recovery section, and wherein a gas outlet of the liquid/gas separator is connected, by means of a gas transport line, to the condensor comprised in the recovery section.

11. The process of claim 2 wherein the first recovery section is operated at a pressure of 0.2-0.6 Pa.

12. The process of claim 3 wherein the adiabatic expansion results in a pressure drop of at least 1 MPa.

13. The process of claim 4 wherein the pressure of the vapor after the adiabatic expansion is at least 0.3 MPa higher than the pressure in the first recovery system.

14. The method of claim 8 wherein the first recovery section is operated at a pressure of 0.2-0.6 Pa.

Assignees

• Mennen Johannes Henricus
• Stamicarbon

Inventors

• Mennen Johannes Henricus

Classifications

• C07C273/04 Primary

  from carbon dioxide and ammonia · CPC title