Process for recovery and recycle of ammonia from an acrylonitrile reactor effluent stream using an ammonium phosphate quench system

• US 20010006614A1
• Filed: 12/18/2000
• Published: 07/05/2001
• Est. Priority Date: 12/23/1998
• Status: Abandoned Application

• Current Assignee: Linda L. Nero, Loring A. Weisenberger
• Original Assignee: Linda L. Nero, Loring A. Weisenberger
• Inventors: Weisenberger, Loring A., Nero, Linda L.
• Application Number:
  US09/740,077
• Publication Number:
  US 20010006614A1
• Time in Patent Office: Days
• US Class Current: 423/238
• CPC Class Codes: B01D 53/346 Controlling the process
• CPC Class Codes: B01D 53/58 Ammonia
• 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
• CPC Class Codes: C01C 3/0212 from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process
• CPC Class Codes: C07C 253/34 Separation; Purification
• CPC Class Codes: C07C 255/03 Mononitriles
• CPC Class Codes: C07C 255/08 Acrylonitrile; Methacrylonitrile

Abstract

The present invention provides a process for the recovery of unreacted ammonia from the effluent obtained from a reaction zone wherein oxygen, ammonia and a hydrocarbon are reacted at an elevated temperature in the presence of an ammoxidation catalyst to produce an unsaturated nitrile is provided, including the steps of:

quenching the effluent containing the nitrile and unreacted ammonia with an aqueous ammonium phosphate solution having an initial ratio R of ammonium ions to phosphate ions to absorb substantially all of the unreacted ammonia present in the reactor effluent to form an ammonium phosphate solution having an increased ratio R of ammonium ions to phosphate ions;

heating the solution to an elevated temperature sufficient to reduce the ratio R of ammonium ions to phosphate ions and to generate a vaporous stream containing ammonia;

passing the heated solution through a ³¹P nuclear magnetic resonance detector to detect a chemical shift of a ³¹P nuclear magnetic resonance peak;

determining the ratio R of ammonium ions to phosphate ions in the solution based on the chemical shift; and

controlling the heating step to maintain the initial ratio within a desired range.

Claims

1. A process for the recovery of unreacted ammonia from the effluent obtained from a reaction zone wherein oxygen, ammonia and a hydrocarbon are reacted at an elevated temperature in the presence of an ammoxidation catalyst to produce an unsaturated nitrile comprising the steps of:

quenching the effluent containing the nitrile and unreacted ammonia with an aqueous ammonium phosphate solution having an initial ratio R of ammonium ions to phosphate ions to absorb substantially all of the unreacted ammonia present in the reactor effluent to form an ammonium phosphate solution having an increased ratio R of ammonium ions to phosphate ions;

heating the solution to an elevated temperature sufficient to reduce the ratio R of ammonium ions to phosphate ions and to generate a vaporous stream containing ammonia;

passing the heated solution through a ³¹P nuclear magnetic resonance detector to detect a chemical shift of a ³¹P nuclear magnetic resonance peak;

determining the ratio R of ammonium ions to phosphate ions in the solution based on the chemical shift; and

controlling the heating step to maintain the initial ratio R within a desired range.

2. A process as in

claim 1

, further comprising the step of recycling at least a portion of the solution to the quenching step.

3. A process as in

claim 1

, further comprising the steps of passing the ammonium phosphate solution having an increased ratio of ammonium ions to phosphate ions through a detector prior to the heating step, determining the ratio of ammonium ions to phosphate ions ammonium phosphate solution having an increased ratio of ammonium ions to phosphate ions.

4. A process as in

claim 3

, further comprising the step of controlling the heating step to maintain both the initial and increased ratios within desired ranges.

5. A process as in

claim 1

, further comprising a wet oxidation step.

6. A process as in

claim 1

, further comprising a step of increasing the concentration of the phosphate ion.

7. A process as in

claim 1

, further comprising the step of recycling the recovered ammonia to the reaction zone.

8. A process as in

claim 1

, further comprising a step of purifying the recovered ammonia.

9. A process as in

claim 1

, further comprising a step of concentrating the recovered ammonia.

10. A process as in

claim 1

, further comprising a step of contacting the quench solution with a stripping gas subsequent to the quenching step.

11. A process as in

claim 9

, further comprising treating the stripping gas to recover useful co-products or by-products of the ammoxidation reaction.

12. A process as in

claim 1

, wherein the step of determining the ratio R includes preparation of a calibration curve from at least two solutions containing a known ratio of ammonium ion to phosphate ion.

13. A process as in

claim 11

, wherein the calibration curve is prepared from solutions containing substantially the same total solids content as in the ammonium phosphate solution.

14. A process as in

claim 1

, wherein the initial ratio is in the range from about 0.7 to about 1.3.

15. A process as in

claim 1

, wherein the hydrocarbon is selected from propane and isobutane.

16. A process for the recovery of unreacted ammonia from the effluent obtained from a reaction zone wherein oxygen, ammonia and a hydrocarbon are reacted at an elevated temperature in the presence of an ammoxidation catalyst to produce an unsaturated nitrile comprising the steps of:

quenching the effluent containing the nitrile and unreacted ammonia with an ammonium phosphate solution having an initial ratio R of ammonium ions to phosphate ions to absorb substantially all of the unreacted ammonia present in the reactor effluent whereby the ammonium phosphate solution has an increased ratio R of ammonium ions to phosphate ions;

heating the solution to an elevated temperature sufficient to reduce the ratio R and to generate a vaporous stream containing ammonia for recycling to the reaction zone;

passing the solution through a ³¹P nuclear magnetic resonance detector to detect a chemical shift of a ³¹P nuclear magnetic resonance peak;

determining the ratio of ammonium ions to phosphate ions in the solution based on the chemical shift; and

controlling the heating step to maintain the first ratio within a desired range.

17. A process as in

claim 16

, further comprising a step of increasing the concentration of the phosphate ion.

18. A process as in

claim 16

, further comprising a step of contacting the quench solution with a stripping gas subsequent to the quenching step.

19. A process as in

claim 16

, wherein the initial ratio is in the range from about 0.7 to about 1.3.

20. A process for the recovery of unreacted ammonia from the effluent obtained from a reaction zone wherein oxygen, ammonia and a hydrocarbon selected from propane and isobutane are reacted at an elevated temperature in the presence of an ammoxidation catalyst to produce a corresponding unsaturated nitrile, comprising the steps of:

quenching the effluent containing the corresponding nitrile and unreacted ammonia with an ammonium phosphate solution wherein the ratio R of ammonium ions to phosphate ions is between about 0.7 to about 1.3 to absorb substantially all of the unreacted ammonia present in the reactor effluent to form an ammonium phosphate solution having an increased ratio R ammonium ions to phosphate ions;

heating the solution to an elevated temperature sufficient to reduce the amount of ammonium ions in the solution to substantially the initial ratio R present in the solution and to generate a vaporous stream containing ammonia for recycling to the fluid bed reactor;

passing the ammonium phosphate solution through a ³¹P nuclear magnetic resonance detector to detect a chemical shift of a ³¹P nuclear magnetic resonance peak;

determining the ratio of ammonium ions to phosphate ions in the solution based on the chemical shift; and

controlling the heating step to maintain the ratio R within a desired range.