Method for improved distillation of ammonia from weak ammonia liquor

• US 4,108,735 A
• Filed: 06/14/1976
• Issued: 08/22/1978
• Est. Priority Date: 06/14/1976
• Status: Expired due to Term

• Current Assignee: Bethlehem Steel Corporation (ArcelorMittal SA)
• Original Assignee: Bethlehem Steel Corporation (ArcelorMittal SA)
• Inventors: Rudzki, Eugene M., Burcaw, Kenneth R. Jr., Kwasnoski, Daniel
• Primary Examiner(s): Bascomb, Jr., Wilbur L.
• Application Number:
  US05/695,685
• Time in Patent Office: 799 Days
• Field of Search: 203/36, 203/33, 203/37, 203/7, 203/47, 203/96, 203/97, 203/95, 203/92, 203/93, 423/357, 423/356
• US Class Current: 203/7
• CPC Class Codes: C01C 1/10 Separation of ammonia from ammonia liquors, e.g. gas liquors as part of the ammonia synthesis process C01C1/04

Abstract

Fouling of an ammonia still, used for removal of ammonia from weak ammonia liquor derived from a coal coking operation, is alleviated by pre-precipitating insoluble calcium salts from the ammonia liquor by treatment of the liquor with lime prior to introduction into a single-leg still.

Claims

1. An improved method of distilling weak ammonia liquor containing both free and fixed ammonia derived from a coal coking operation with decreased fouling of the still apparatus comprising:

(a) premixing ammonia liquor which contains both substantial free ammonia as ammonium carbonate, ammonium sulfide and ammonium cyanide and fixed ammonia as ammonium chloride, ammonium thiocyanate and ammonium sulfate prior to initiating any distillation with sufficient lime to pre-precipitate at least most of the principal components of precipitation fouling from the undistilled weak ammonia liquor, and

(b) passing the ammonia liquor subsequent to pre-precipitation with said lime through an ammonia still countercurrently with steam to distill the ammonia liquor and release ammonia from the liquor.

2. The improved method according to claim 1 wherein sufficient lime is premixed with the ammonia liquor to pre-precipitate both substantially all of the precipitatable lime compounds from the undistilled ammonia liquor and to free the fixed ammonia content of the liquor.

3. The improved method according to claim 2 wherein the weak ammonia liquor is passed through a single direct contact steam distillation operation.

4. The improved method according to claim 3 in which the ammonia still through which the ammonia liquor is passed has a range of molar liquid to gas ratios of approximately 5 to 10.

5. The improved method according to claim 4 in which the ammonia still through which the ammonia liquor is passed has a range of molar liquid to gas ratios of approximately 6 to 9.

6. The improved method according to claim 5 in which the ammonia liquor passed to the still subsequent to pre-precipitation with said lime has a pH value which is within a range of 10.6 to 11.0.

7. The improved method according to claim 5 wherein the lime is combined with the weak ammonia liquor as a milk of lime suspension.

18. The improved method according to claim 1 wherein sufficient lime is premixed with the ammonia liquor to precipitate substantially all of the precipitatable lime compounds from the undistlled ammonia liquor.

8. An improved method of distilling weak ammonia liquor derived from a coal coking operation to remove both free and fixed ammonia from the liquor with minimal precipitation fouling of the still apparatus comprising:

(a) premixing the ammonia liquor which contains both free and fixed ammonia in the form of the free ammonia compounds ammonium carbonate, ammonium sulfide and ammonium cyanide and in the form of fixed ammonia compounds ammonium chloride, ammonium thiocyanate and ammonium sulfate prior to initiating any distillation with a calcium ion containing material to pre-precipitate calcium components of precipitation fouling from the undistilled weak ammonia liquor, sufficient calcium material being added to the liquor to free substantial fixed ammonia in addition to pre-precipitating calcium components of precipitation fouling, and

(b) passing the pre-precipitated ammonia liquor subsequent to premixing with the calcium ion containing material through an ammonia distillation operation countercurrently with steam to distill the ammonia liquor and expel ammonia from the liquor.

9. An improved method of removing free and fixed ammonia from weak ammonia liquor according to claim 8 wherein sufficient calcium ion containing material is premixed with the weak ammonia liquor to both pre-precipitate substantialy all precipitatable calcium components of precipitation fouling from the weak ammonia liquor and to free substantially all the fixed ammonia from the weak ammonia liquor whereby said free ammonia can be expelled from the weak ammonia liquor by distillation.

10. An improved method of removing free and fixed ammonia from weak ammonia liquor according to claim 9 wherein the weak ammonia liquor after pre-mixing with the calcium ion containing material is passed through a single direct contact steam distillation operation.

11. An improved method of removing free and fixed ammonia from weak ammonia liquor according to claim 10 wherein the ammonia still through which the ammonia liquor is passed has a range of molar liquor to gas ratios of approximately 5 to 10.

12. An improved method of removing free and fixed ammonia from weak ammonia liquor according to claim 11 wherein the ammonia still through the ammonia liquor is passed has a range of molar liquid to gas ratios of approximately 6 to 9.

13. An improved method of removing free and fixed ammonia from weak ammonia liquor according to claim 12 wherein the ammonia liquor passed to the still subsequent to pre-precipitation with said calcium ion containing material has a pH value which is within a range of 10.6 to 11.0.

14. A method of alleviating deleterious fouling of a still column with solid calcium compounds during distillation of weak ammonia liquor containing both free and fixed ammonia and including in particular carbonates and fluorides derived from a coal coking operation comprising:

(a) premixing the weak ammonia liquor which contains both substantial free ammonia as the compounds ammonium carbonate, ammonium sulfide and ammonium cyanide and fixed ammonia as the compounds ammonium chloride, ammonium thiocyanate and ammonium sulfate prior to initiating any distillation with sufficient lime to pre-precipitatable calcium fluoride and calcium carbonate and reduce the fluoride ion concentration in the weak ammonia liquor to a point where no substantial calcium fluoride salts will precipitate during distllation, and

(b) passing the weak ammonia liquor subsequent to said pre-precipitation through an ammonia distillation operation counter-currently with steam to distill the ammonia liquor and expel ammonia from the liquor.

15. A method of alleviating fouling of a still column according to claim 14 wherein sufficient lime is premixed with the weak ammonia liquor to pre-precipitate both calcium fluoride and calcium carbonate and reduce the fluoride and carbonate ion concentration in the weak ammonia liquor to a point where no substantial calcium fluoride or calcium carbonate salts will precipitate during distillation.

16. A method of alleviating fouling of a still column according to claim 15 wherein sufficient lime is premixed with the weak ammonia liquor to pre-precipitate substantially all precipitatable calcium compounds from the weak ammonia liquor.

17. A method of alleviating fouling of a still column according to claim 16 wherein sufficient lime is premixed with the weak ammonia liquor to pre-precipitate all precipitatable calcium compounds from the weak ammonia liquor and to free substantially all fixed ammonia in the ammonia liquor.