Process for synthesizing ammonia from hydrocarbons

• US 4,376,758 A
• Filed: 01/06/1981
• Issued: 03/15/1983
• Est. Priority Date: 01/08/1980
• Status: Expired due to Fees

• Current Assignee: Montedison S.p.A. (Government of France)
• Original Assignee: Montedison S.p.A. (Government of France)
• Inventors: Pagani, Giorgio, Bosco, Dino, Brambilla, Lorenzo
• Primary Examiner(s): Vertiz, O. R.
• Assistant Examiner(s): Langel, Wayne A.
• Application Number:
  US06/222,988
• Time in Patent Office: 798 Days
• Field of Search: 423/359, 423/360, 423/361, 203/36, 203/74, 203/75, 252/373, 252/376, 252/375
• US Class Current: 423/359
• CPC Class Codes: C01B 3/025 Preparation or purification of gas mixtures for ammonia synthesis
• CPC Class Codes: C01C 1/0405 from N2 and H2 in presence of a catalyst
• CPC Class Codes: C01C 1/0464 by absorption in liquids, e.g. water
• CPC Class Codes: C01C 1/047 by condensation
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts

Abstract

A process for synthesizing ammonia is disclosed comprising the steps of generating the synthesis gas from hydrocarbons by the primary reforming of said hydrocarbon with steam and by the secondary reforming of the resulting gaseous mixture with oxygen; subjecting a portion of the starting hydrocarbon mixed with the steam to a tertiary reforming in which the necessary heat is provided by the gaseous reaction mixture leaving the secondary reforming; causing the ammonia synthesis to occur at low pressure with drying of the gas sent to the synthesis reactor by employing a molecular sieve; causing the ammonia contained in the reacted gas to be absorbed by water; and subjecting the ammonia solution so obtained to a distillation which may be a conventional distillation step or one effected by means of two distillation columns operating at different pressures.

Claims

1. An ammonia synthesis process comprising the generation of synthesis gas from hydrocarbons by the primary reforming of said gases with steam and by the secondary reforming of the resulting gaseous mixture with oxygen, characterized in that it comprises the steps of subjecting a part, not passed through the primary reforming, of the starting hydrocarbon mixed with the steam to a tertiary reforming in which the necessary heat is supplied, by means of indirect heat exchange, by the gaseous reaction mixture leaving the secondary reforming;

said tertiary reforming being of the mixing type in which the reformed gaseous mixture, which forms by flowing inside pipes containing the catalyst of said tertiary reformer, directly mixes, before said heat exchange occurs, with the gaseous reaction mixture leaving the secondary reforming, such mixture providing, from outside the pipes, the heat necessary for said tertiary reforming;

causing the ammonia synthesis to occur at an absolute pressure lower than 100 kg/cm² with drying of the gas conveyed to the synthesis reactor by employing molecular sieves;

absorbing the ammonia contained in the reacted gas with water; and

subjecting the ammonia solution so obtained to distillation to obtain a relatively concentrated ammonia product.

2. A process according to claim 1, characterized in that the gas sent to the synthesis reactor is dried by molecular sieves, the regeneration of which is carried out by at least a part of the reacted gas flowing from the ammonia synthesis reactor, such gas leaving the regeneration being then sent to the absorption of ammonia with water.

3. A process according to claim 2, characterized in that said drying is obtained by employing four molecular sieves which individually, and alternately in each operation cycle, are one in the regeneration stage, one in the heating stage, one in the cooling stage, and one in the adsorption stage.

4. A process according to claim 3, characterized that the heating of the molecular sieve in the heating stage is effected by using the heat withdrawn from the molecular sieve in the cooling stage.

5. A process according to claim 4, characterized that a part of the dried gas coming from the molecular sieve in the adsorption stage is sent to the molecular sieve in the cooling stage and then to the molecular sieve in the heating stage, thereby transferring to this last molecular sieve heat withdrawn from the preceding molecular sieve.

6. A process according to claim 5, characterized in that said gas, flowing from the molecular sieve in the heating stage, is conveyed to the ammonia absorber.

7. A process according to claim 3, characterized in that the reacted gas leaving the ammonia synthesis reactor, before being sent to the molecular sieve in the regeneration stage, is cooled down by preheating the dried gas coming from the molecular sieve in the adsorption stage.

8. A process according to claim 3, characterized in that the reacted gas leaving the molecular sieve in the regeneration stage, before being sent to the absorption of ammonia with water, preheats the dried gas flowing from the molecular sieve in the adsorption stage.

9. A process according to claim 3, characterized in that the gas leaving the absorption of ammonia with water is conveyed, after compression and after addition of the fresh synthesis mixture, to the molecular sieve in the adsorption stage.

10. A process according to claim 1, characterized in that the ammonia synthesis is conducted at an absolute pressure of from 40 to 80 kg/cm².

11. A process according to claim 1, characterized in that the ammoniacal solution obtained from the absorption of ammonia with water is subjected to distillation by using two columns operating at different pressures, in which said solution to be distilled, after being mixed with the ammoniacal vapors flowing from the top of the column operating at the lower pressure, is conveyed to the column operating at the higher pressure, from the bottom of which the partially-distilled ammoniacal solution is sent to the column operating at the lower pressure;

liquid ammonia is recovered at the top of the column operating at the higher pressure while the residual ammonia solution is withdrawn from the bottom of the column operating at the lower pressure.