Method for treating offgases from a melamine plant
Disclosed is a method for treating or using offgases obtained in a melamine plant comprising at least one melamine synthesis reactor and at least one washing unit in an integrated process for urea and melamine production, wherein the offgases leaving the melamine synthesis reactor are fed into the washing section and the washed offgases leaving the washing section are transferred from the washing section via at least one pipeline connecting the washing section and the at least one urea synthesis plant to the at least one urea synthesis plant. The washed offgases leaving the washing section are mixed with at least one carbamate solution immediately downstream of the washing section by feeding the carbamate solution into the pipeline connecting the washing section to the urea plant.
1. A method for using offgases obtained in a melamine plant comprising at least one melamine synthesis reactor and at least one washing section in an integrated process for urea and melamine production, wherein the offgases leaving the melamine synthesis reactor are fed into the washing section and the washed offgases leaving the washing section are transferred from the washing section via at least one pipeline, which connects the washing section to at least one urea plant, wherein the washed offgases leaving the washing section are mixed with at least one carbamate solution downstream of the washing section by feeding the carbamate solution into the pipeline connecting the washing section to the urea plant,
wherein the volume ratio of offgases to carbamate solution fed to the pipeline and is between 2:1 and 10:1 such that a two phase mixture of offgases and carbamate solution is obtained within the pipeline.
2. The method according to claim 1 , wherein the volume ratio of offgases to carbamate solution fed to the pipeline is between 2:1 and 8:1.
3. The method according to claim 1 , wherein the at least one carbamate solution is fed into the pipeline connecting the washing section to the urea plant at at least one inlet having a distance of ⅓ of the overall length of the connecting pipeline.
4. The method according to claim 1 , wherein the pipeline continues at first vertically from said expansion valve or pressure valve of the vertical washing section for a predetermined distance to a point where the pipeline is bent by a predetermined angle and continues subsequently horizontal or with a predetermined decline towards the urea plant for connecting the washing section and the urea plant, and wherein the at least one carbamate solution is fed into the pipeline within a distance of at least 5 m after said bending point of the pipeline.
5. The method according to claim 1 , wherein the at least one carbamate solution stems from the urea plant.
6. The method according to claim 1 , wherein the carbamate solution is fed into the pipeline connecting the washing section to the urea plant at more than one location along the pipeline.
7. The method according to claim 1 , wherein at least 20% of the total amount of carbamate solution is fed into the pipeline connecting the washing section to the urea plant after leaving the washing section.
8. The method according to claim 1 , wherein the mixture of offgases and carbamate solution obtained in the pipeline is fed to at least one condenser unit before entering the urea plant, and wherein in the at least one condenser unit a complete or partial condensation of the offgases takes place.
9. The method according to claim 1 , wherein the mixture of offgases and carbamate solution obtained in the at least one pipeline is fed after mixing the offgases and the carbamate solution into at least one condenser unit, and wherein a complete or partial condensation of offgases takes place.
10. The method according to claim 1 , wherein the mixture of offgases and carbamate solution obtained in the pipeline is fed to at least two condenser units, and wherein in a first condenser unit a partial condensation of offgases takes place and in the second condenser unit a complete condensation of offgases takes place.
11. The method according to claim 1 , wherein the volume ratio of offgases to carbamate solution fed to the pipeline is between 2.3:1 and 5:1.
12. The method according to claim 1 , wherein the at least one carbamate solution is fed into the pipeline connecting the washing section to the urea plant at at least one inlet having a distance of ¼ of the overall length of the connecting pipeline.
13. The method according to claim 1 , wherein the pipeline continues at first vertically from said expansion valve or pressure valve of the vertical washing section for a predetermined distance to a point where the pipeline is bent by a predetermined angle and continues subsequently horizontal or with a predetermined decline towards the urea plant for connecting the washing section and the urea plant, and wherein the at least one carbamate solution is fed into the pipeline within a distance of at least 3 m after said bending point of the pipeline.
14. The method according to claim 1 , wherein the pipeline continues at first vertically from said expansion valve or pressure valve of the vertical washing section for a predetermined distance to a point where the pipeline is bent by a predetermined angle and continues subsequently horizontal or with a predetermined decline towards the urea plant for connecting the washing section and the urea plant, and wherein the at least one carbamate solution is fed into the pipeline within a distance of at least 1 m after said bending point of the pipeline.
15. The method according to claim 6 , wherein the carbamate solution is fed into the pipeline connecting the washing section to the urea plant at up to four locations along the pipeline.