Process for the separation of ammonia and carbon dioxide from mixtures containing ammonia, carbon dioxide and water

• US 4,256,471 A
• Filed: 04/16/1979
• Issued: 03/17/1981
• Est. Priority Date: 04/16/1979
• Status: Expired due to Term

• Current Assignee: Stamicarbon B.V. (Maire Tecnimont SpA)
• Original Assignee: Stamicarbon B.V. (Maire Tecnimont SpA)
• Inventors: Goorden, Josephus J. P. M.
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US06/030,374
• Time in Patent Office: 701 Days
• Field of Search: 55/48, 55/68, 55/70, 55/89, 55/93, 423/352, 423/437
• US Class Current: 95/171
• CPC Class Codes: B01D 19/0068 General arrangements, e.g. flowsheets B01D19/0063 takes precedence
• CPC Class Codes: C01B 32/50 Carbon dioxide
• CPC Class Codes: C01C 1/12 Separation of ammonia from gases and vapours as part of the ammonia synthesis process C01C1/04
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

An improved process for the separate recovery of substantially pure ammonia and substantially pure carbon dioxide from mixtures containing ammonia and carbon dioxide, and possibly water, such as are obtained as by-products in the manufacture of melamine from urea or the synthesis of urea from ammonia and carbon dioxide. The by-product mixture is introduced into a process loop having an ammonia separation zone, a carbon dioxide separation zone and a desorption zone, the zone to which the mixture is initially fed being dependent upon its composition. The separation is effected by maintaining a system pressure differential between the ammonia and carbon dioxide separation zones, or adding diluting water to the carbon dioxide separation zone. The efficiency of the separation is enhanced by introducing a carbon dioxide containing gaseous phase, and preferably an excess of an inert gas, into the bottom of the ammonia separation zone.

Claims

1. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, in which process:

an ammonia off-gas substantially free of carbon dioxide and water is separated by rectification in an ammonia separation zone, and the resulting residual liquid phase containing ammonia, carbon dioxide and water is removed therefrom and introduced into a carbon dioxide separation zone;

a carbon dioxide off-gas substantially free of ammonia and water is separated by rectification in a carbon dioxide separation zone and the resulting residual liquid phase containing ammonia, carbon dioxide and water is removed therefrom and introduced into a desorption zone; and

an off-gas containing ammonia, carbon dioxide and water vapor is separated from a liquid phase of desorption water substantially free of ammonia and carbon dioxide, and at least a portion of said off-gas is introduced into said ammonia separation zone;

said improvement comprising introducing into the portion of said ammonia separation zone from which said residual liquid phase is removed, a carbon dioxide containing gaseous phase in an amount sufficient to make the residual liquid phase removed therefrom lean with respect to ammonia.

2. The process of claim 1 wherein a portion of the carbon dioxide off-gas from the carbon dioxide separation zone is used as said carbon dioxide containing gaseous phase introduced into said ammonia separation zone.

3. The process of claim 1 wherein the amount of carbon dioxide introduced into said gaseous phase ranges between about 0.2 and 0.01 times by weight the amount of residual liquid phase removed from the ammonia separation zone.

4. The process of claim 3 wherein said amount of carbon dioxide ranges between about 0.1 and 0.02 by weight the amount of said liquid phase.

5. The process of claim 1 wherein an amount of inert gas is also introduced into the portion of the ammonia separation zone from which said residual liquid phase is removed.

6. The process of claim 5 wherein the weight ratio of said carbon dioxide containing gaseous phase to said inert gas is within the range of between 30:

70 and 70;

30.

7. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, which mixture is rich with respect to ammonia, said process comprising the steps of:

introducing said mixture into an ammonia separation zone and separately removing therefrom an ammonia off-gas substantially free of carbon dioxide and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said ammonia separation zone into a carbon dioxide separation zone and separately removing therefrom a carbon dioxide off-gas substantially free of ammonia and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said carbon dioxide separation zone into a desorption zone and separately removing therefrom a desorption zone off-gas containing ammonia, carbon dioxide and water vapor, and a liquid phase of desorption water substantially free of ammonia and carbon dioxide; and

introducing at least a portion of said desorption zone off-gas into said ammonia separation zone;

wherein diluting water is introduced into said carbon dioxide separation zone in an amount of between about 0.2 and 6 times, by weight, the total weight of said residual liquid phase from said ammonia separation zone introduced into said carbon dioxide separation zone, said improvement comprising introducing into the portion of said ammonia separation zone from which said said residual liquid phase is removed, a carbon dioxide containing gaseous phase is an amount sufficient to make said residual liquid phase removed therefrom lean with respect to ammonia.

10. The process of claims 7, 8 or 9 wherein the system pressure in said carbon dioxide separation zone is no greater than twice the system pressure in said ammonia separation zone.

11. The process of claim 10 wherein the system pressure in said carbon dioxide separation zone is substantially the same as the system pressure in said ammonia separation zone.

8. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, which mixture is lean with respect to ammonia, said process comprising the steps of:

introducing said mixture into a carbon dioxide separation zone and separately removing therefrom a carbon dioxide off-gas substantially free of ammonia and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said carbon dioxide separation zone into a desorption zone and separately removing therefrom a desorption zone off-gas containing ammonia, carbon dioxide and water vapor, and a liquid phase of desorption water substantially free of ammonia and carbon dioxide;

introducing at least a portion of said desorption zone off-gas into an ammonia separation zone and separately removing therefrom an ammonia off-gas substantially free of carbon dioxide and water, and a residual liquid phase containing ammonia, carbon dioxide and water; and

introducing said residual liquid phase from said ammonia separation zone into said carbon dioxide separation zone;

wherein diluting water is introduced into said carbon dioxide separation zone in an amount of between about 0.2 and 6 times, by weight, the combined total weight of said mixture and said residual liquid phase from said mixture and said residual liquid phase from said ammonia separation zone introduced into said carbon dioxide separation zone, said improvement comprising introducing into the portion of said ammonia separation zone from which said residual liquid phase is removed, a carbon dioxide containing gaseous phase in an amount sufficient to make said residual liquid phase removed therefrom lean with respect to ammonia.

9. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, which mixture is rich with respect to ammonia and additionally contains a substantial amount of water, said process comprising the steps of:

introducing said mixture into a desorption zone and separately removing therefrom a desorption zone off-gas containing ammonia, carbon dioxide and water vapor, and a liquid phase of desorption water substantially free of ammonia and carbon dioxide;

introducing at least a portion of said desorption zone off-gas into an ammonia separation zone and separately removing therefrom an ammonia off-gas substantially free of carbon dioxide and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said ammonia separation zone into a carbon dioxide separation zone and separately removing therefrom a carbon dioxide off-gas substantially free of ammonia and water and a residual liquid phase containing ammonia, carbon dioxide and water; and

introducing said residual liquid phase from said carbon dioxide separation zone into said desorption zone;

wherein diluting water is introduced into said carbon dioxide separation zone in an amount of between about 0.2 and 6 times, by weight, the total weight of said residual liquid phase from said ammonia separation zone introduced into said carbon dioxide separation zone, said improvement comprising introducing into the portion of said ammonia separation zone from which said residual liquid phase is removed, a carbon dioxide containing gaseous phase in an amount sufficient to make said residual liquid phase removed therefrom lean with respect to ammonia.

12. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, which mixture is rich with respect to ammonia, said process comprising the steps of:

introducing said mixture into an ammonia separation zone and separately removing therefrom an ammonia off-gas substantially free of carbon dioxide and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said ammonia separation zone into a carbon dioxide separation zone and separately removing therefrom a carbon dioxide off-gas substantially free of ammonia and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said carbon dioxide separation zone into a desorption zone and separately removing therefrom a desorption zone off-gas containing ammonia, carbon dioxide and water vapor, and a liquid phase of desorption water substantially free of ammonia and carbon dioxide; and

introducing at least a portion of said desorption zone off-gas into said ammonia separation zone;

wherein the system pressure in said carbon dioxide separation zone is greater than twice the system pressure in said ammonia separation zone, said improvement comprising introducing into the portion of said ammonia separation zone from which said residual liquid phase is removed, a carbon dioxide containing gaseous phase in an amount sufficient to make said residual liquid phase removed therefrom lean with respect to ammonia.

15. The process of claim 12, 13 or 14 wherein the ratio between the respective system pressures in said ammonia separation zone and in said carbon dioxide separation zone is between about 1:

5 and 1;

20.

16. The process of claim 12, 13 or 14 wherein diluting water is introduced into said carbon dioxide separation zone.

13. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, which mixture is lean with respect to ammonia, said process comprising the steps of:

introducing said mixture into a carbon dioxide separation zone and separately removing therefrom a carbon dioxide off-gas substantially free of ammonia and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said carbon dioxide separation zone into a depression zone and separately removing therefrom a desorption zone off-gas containing ammonia, carbon dioxide and water vapor, and a liquid phase of desorption water substantially free of ammonia and carbon dioxide;

introducing at least a portion of said desorption zone off-gas into an ammonia separation zone and separately removing therefrom an ammonia off-gas substantially free of carbon dioxide and water, and a residual liquid phase containing ammonia, carbon dioxide and water; and

introducing said residual liquid phase from said ammonia separation zone into said carbon dioxide separation zone;

wherein the system pressure in said carbon dioxide separation zone is greater than twice the system pressure in said ammonia separation zone, said improvement comprising introducing into the portion of said ammonia separation zone from which said residual liquid phase is removed, a carbon dioxide containing gaseous phase in an amount sufficient to make said residual liquid phase removed therefrom lean with respect to ammonia.

14. An improved process for the separate recovery of ammonia substantially free of carbon dioxide and water, and carbon dioxide substantially free of ammonia and water, from a mixture essentially containing ammonia and carbon dioxide, which mixture is rich with respect to ammonia and additionally contains a substantial amount of water, said process comprising the steps of:

introducing said mixture into a desorption zone and separately removing therefrom a desorption zone off-gas containing ammonia, carbon dioxide amd water vapor, and a liquid phase of desorption water substantially free of ammonia and carbon dioxide;

introducing at least a portion of said desorption zone off-gas into an ammonia separation zone and separately removing therefrom an ammonia off-gas substantially free of carbon dioxide and water, and a residual liquid phase containing ammonia, carbon dioxide and water;

introducing said residual liquid phase from said ammonia separation zone into a carbon dioxide separation zone and separately removing therefrom a carbon dioxide off-gas substantially free of ammonia and water and a residual liquid phase containing ammonia, carbon dioxide and water; and

introducing said residual liquid phase from said carbon dioxide separation zone into said desorption zone;

wherein the system pressure in said carbon dioxide separation zone is greater than twice the system pressure in said ammonia separation zone, said improvement comprising introducing into the portion of said ammonia separation zone from which said residual liquid phase is removed, a carbon dioxide containing gaseous phase in an amount sufficient to make said residual liquid phase removed therefrom lean with respect to ammonia.