Process for refining an ammonia synthesis gas

• US 4,624,841 A
• Filed: 01/22/1985
• Issued: 11/25/1986
• Est. Priority Date: 01/23/1984
• Status: Expired due to Term

• Current Assignee: TOYO Engineering Corporation
• Original Assignee: TOYO Engineering Corporation
• Inventors: Hidaki, Morihisa
• Primary Examiner(s): Doll, John
• Assistant Examiner(s): Langel, Wayne A.
• Application Number:
  US06/693,491
• Time in Patent Office: 672 Days
• Field of Search: 423/359, 55/68, 55/25, 55/33, 55/70, 252/377
• US Class Current: 423/359
• CPC Class Codes: C01B 3/025 Preparation or purification of gas mixtures for ammonia synthesis

Abstract

The synthesis gas for an ammonia synthesis process is refined by treating same in an adsorption-desorption unit to remove nitrogen either during the carbon oxide removal step or in the ammonia synthesis loop.

Claims

1. In a process for refining an ammonia synthesis gas comprising the steps of:

(a) subjecting a hydrocarbon raw material to a primary steam reforming reaction under pressure;

(b) subjecting the resulting gas from the step (a) to a secondary steam reforming reaction by feeding air into said resulting gas;

(c) subjecting carbon monoxide in the resulting gas from the step (b) to a catalytic carbon monoxide shift conversion reaction;

(d) removing carbon oxides from the gas obtained by the step (c) to produce an ammonia synthesis gas containing nitrogen and hydrogen;

(e) subjecting said ammonia synthesis gas to an ammonia synthesis reaction to produce ammonia and feeding the ammonia synthesis gas that contains produced ammonia to an ammonia separator unit to separate ammonia from the remaining ammonia synthesis gas; and

(f) circulating said remaining ammonia synthesis gas separated from ammonia to the step (e), the improvement which comprises;

(A) in step (b), feeding said air in excess of the amount of air equivalent to the nitrogen stoichiometrically required for the synthesis of ammonia;

(B) in either step (d) or step (e), treating the ammonia synthesis gas in an adsorption-desorption unit to remove excess nitrogen as well as non-ammonia-producing gaseous components and, in the case of the synthesis gas of step (e), ammonia, from the ammonia synthesis gas, the amount of nitrogen that is removed being so regulated that the hydrogen-to-nitrogen ratio in the ammonia synthesis gas is the stoichiometric ratio required for the synthesis of ammonia and wherein the treatment in said adsorption-desorption unit comprises;

(i) feeding said ammonia synthesis gas to a first adsorption bed which is saturated with adsorbed nitrogen, thereby causing said first bed to adsorb water vapor, carbon dioxide, carbon monoxide, methane and argon contained in said ammonia synthesis gas and to desorb the nitrogen previously adsorbed on said first bed while allowing gases of hydrogen and nitrogen to flow out of said first bed;

(ii) feeding a portion of the gas flowing out of said first bed into a succeeding downstream second adsorption bed which has undergone desorption and repressurization steps, thereby to adsorb nitrogen contained in said portion of said gas fed therein and flowing substantially pure hydrogen from said second bed; and

(iii) when said succeeding downstream second adsorption bed becomes saturated with adsorbed nitrogen, switching said first bed undergoing the step (i) to undergo a subsequent desorption step, switching said succeeding downstream second bed to simultaneously undergo the step (i), and simultaneously switching a further succeeding adsorbent bed which has undergone desorption and repressurization to undergo the step (ii), thereby cyclically continuing adsorption;

(iv) combining the gas discharged from said further succeeding downstream bed undergoing the step (ii) with the portion of the gas which has been discharged from said bed undergoing the step (i) but has not been sent to said further succeeding downstream bed undergoing the step (ii) whereby to form an ammonia synthesis gas, while controlling the flow rates of both said gases so that the hydrogen-to-nitrogen ratio in the ammonia synthesis gas can be adjusted to a predetermined value nearest to the stoichiometric ratio required for the synthesis of ammonia.

2. A process for refining an ammonia synthesis gas as claimed in claim 1, wherein the ammonia synthesis gas is treated in an adsorption-desorption unit within the step (d).

3. A process for refining an ammonia synthesis gas as claimed in claim 2 wherein said adsorption-desorption unit is a pressure swing adsorption-desorption unit which comprises from four to six adsorbent beds operated through a cycle of steps which comprises:

(I) a nitrogen-adsorption step comprising, when a preceding bed is switched to undergo a replacement-adsorption step, feeding a portion of the gas discharged from said preceding bed to one of said adsorbent beds, said preceding bed being positioned upstream of said one bed;

(II) a replacement-adsorption step comprising, when said one bed is saturated with nitrogen, feeding fresh ammonia synthesis gas to said one bed, a portion of the gas discharged from said one bed being fed to a succeeding adsorbent bed downstream from said one bed while the remainder is discharged directly to the outside of said unit;

(III) a desorption step comprising, when said succeeding adsorbent bed undergoing the nitrogen-absorption step is saturated, relieving pressure in said one bed thereby sequentially desorbing adsorbed components therefrom;

(IV) a repressurization step comprising, when said one bed has completed the desorption step, repressurizing said one bed; and

cyclically repeating said steps (I)-(IV) for said one bed.

4. A process for refining ammonia synthesis gas as claimed in claim 3 which further comprises:

in said step (III), before said one bed undergoes pressure relief, feeding a gas containing almost no hydrogen into said one bed thereby replacing a gas present in the voids in said one bed;

discharging the replaced gas from the adsorption-desorption unit; and

then feeding the gas evolved from said one bed in the early stage of said pressure relief into an adsorbent bed undergoing the repressurization step.

5. A process for refining an ammonia synthesis gas as claimed in claim 3 which further comprises:

in said step, (III) relieving pressure in said one bed to a medium pressure;

then feeding a gas containing almost no hydrogen into said one bed thereby replacing a gas present in the voids in said one bed;

discharging the gas evolved by said pressure relief and the replaced gas from the adsorption-desorption unit;

further relieving pressure in said one bed;

feeding the gas evolved from said one bed in the early stage of said further pressure relief into an adsorbent bed undergoing the repressurization step.

6. A process for refining an ammonia synthesis gas as claimed in claim 4 which further comprises:

in said step (III), subsequent to the feeding of the evolved gas by pressure relief to a bed undergoing the repressurization step, feeding the gas evolved from said one bed by further pressure relief to a pressurizing apparatus at a medium pressure; and

pressurizing said gas in said apparatus to a pressure higher than the replacing pressure thereby preparing the replacing gas to be used in the replacing operation.

7. A process for refining an ammonia synthesis gas as claimed in claim 3 which further comprises:

feeding a portion of the hydrogen gas that flows out of a bed undergoing the nitrogen-adsorption step (I) into a vessel at a constant flow rate to store said portion of the gas in said vessel as a primary filling gas for use for the repressurization of said one bed in the step (IV);

feeding said portion of hydrogen gas through said vessel to said one bed in the early stage of the repressurization; and

then feeding said portion of hydrogen gas directly to said one bed via a hydrogen gas line with the inlet and outlet valves of said vessel being closed in the later stage of the repressurization.

8. A process for refining an ammonia synthesis gas as claimed in claim 3 which further comprises:

feeding first a desorbing gas heated to a high temperature and then a desorbing gas cooled to a low temperature to said one bed, both of the said desorbing gases having been evolved by pressure relief from a bed undergoing the desorption step, at the position of the adsorption front of strongly adsorbable components adsorbed on said one bed during the adsorption step (II), in the final stage of the desorption step (III).

9. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

in the step (d) of claim 1, after carbon dioxide is removed from fresh ammonia synthesis gas by absorption at a temperature lower than 0°

C., feeding said synthesis gas into said pressure swing adsorption-desorption unit, while keeping the temperature and pressure of said gas the same as in said absorption.

10. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

when the removal of ammonia is incomplete in the step (e), as the treatment in an adsorption-desorption unit within the step (e), feeding the synthesis gas sequentially first to an adsorption-desorption unit using type 3A zeolite as an adsorbent thereby primarily separating ammonia and water and then to a pressure swing adsorption unit using an adsorbent different than said type 3A zeolite thereby separating nitrogen and non-ammonia-producing gaseous components according to their relative tendencies to be adsorbed and the relative amount of the component gases thereof.

11. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

when the removal of ammonia is almost complete in the step (e), as the treatment in an adsorption-desorption unit within the step (e), feeding the synthesis gas to a pressure swing adsorption-desorption unit thereby separating nitrogen and non-ammonia-producing gaseous components according to their relative tendencies to be adsorbed and the relative amount of the component gases thereof.

12. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

before said synthesis gas is treated in the adsorption-desorption unit in step (e), feeding said synthesis gas into a liquefaction-separation unit utilizing cooling thereby separating ammonia from the synthesis gas so that not more than 3% of ammonia remains in said synthesis gas;

combining the resulting synthesis gas discharged from the liquefaction-separation unit with a fresh synthesis gas obtained in the step (d); and

feeding the combined synthesis gas to said adsorption-desorption unit.

13. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

before said synthesis gas is treated in the adsorption-desorption unit, in step (e) feeding said synthesis gas into a water absorption-separation unit thereby separating ammonia from the synthesis gas;

combining the resulting synthesis gas discharged from the water absorption-separation unit with a fresh synthesis gas obtained in the step (d); and

feeding the combined synthesis gas to said adsorption-desorption unit.

14. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

before said synthesis gas is treated in the adsorption-desorption unit, in step (e) feeding said synthesis gas into a water absorption-separation unit thereby separating ammonia from the synthesis gas;

feeding the synthesis gas discharged from said water absorption-separation unit to another adsorption-desorption unit packed with adsorbent thereby removing water and ammonia;

feeding a larger portion of the synthesis gas discharged from said another adsorption-desorption unit directly to the ammonia synthesis reactor;

combining the remaining smaller portion of said synthesis gas with a fresh synthesis gas obtained in the step (d); and

feeding the combined synthesis gas to the former adsorption-desorption unit.

15. A process tor refining an ammonia synthesis gas as claimed in claim 1 wherein said ammonia synthesis gas is treated in an adsorption-desorption unit within step (e) and wherein treatment in said adsorption-desorption unit comprises:

(i) feeding a synthesis gas comprising hydrogen, nitrogen, ammonia and non-ammonia-producing gaseous components to one adsorbent bed which has been saturated with nitrogen through adsorption, thereby allowing said one bed to adsorb all of water vapor, almost all of the carbon dioxide and carbon monoxide, most of the methane, and a considerable amount of argon contained therein by the replacement of the nitrogen previosuly adsorbed thereon, while allowing hydrogen and nitrogen to flow out of said one bed without being adsorbed;

(ii) feeding a portion of the gas flowed out of said one bed into a succeeding downstream adsorbent bed which has undergone desorption and repressurization steps, thereby separating almost all of the nitrogen contained in said portion of the gas through adsorption;

(iii) when said succeeding downstream adsorbent bed becomes saturated with nitrogen, switching said one bed undergoing the step (i) to undergo a subsequent desorption step, switching said succeeding downstream bed to simultaneously undergo the step (i), and simultaneously switching a further succeeding adsorbent bed which has undergone desorption and repressurization to undergo the step (ii), thereby cyclically continuing adsorption,

(iv) combining the gas discharged from the said succeeding downstream bed undergoing the step (ii) with the gas which has been discharged from said one bed undergoing the step (i) but has not been sent to said succeeding downstream bed undergoing the step (ii), while controlling the flow rates of both gases so that the hydrogen-to-nitrogen ratio in the synthesis gas can be adjusted to a desired value close to the stoichiometric ratio required for the synthesis of ammonia.

16. A process for refining an ammonia synthesis gas as claimed in claim 15 wherein said adsorption-desorption unit is a pressure swing adsorption-desorption unit which comprises four, five or six adsorbent beds operated by a cycle of steps which comprises:

(I) a nitrogen-adsorption step comprising, when a preceding bed is switched to undergo a replacement-adsorption step, feeding a portion of the gas discharged from said preceding bed to one of said adsorbent beds, said preceding bed being positioned upstream of said one bed;

(II) a replacement-adsorption step comprising, when said one bed is saturated with nitrogen, feeding a fresh synthesis gas to said one bed, a portion of the gas discharged from said one bed being fed to a succeeding adsorbent bed downstream of said one bed while the remainder is discharged directly to the outside of said unit;

(III) a desorption step comprising, when said succeeding adsorbent bed undergoing the nitrogen-adsorption step is saturated, relieving pressure in said one bed thereby sequentially desorbing adsorbed components therefrom;

(IV) a repressurization step comprising, when said one bed has finished the desorption step, repressurizing said one bed; and

cyclically repeating said steps (I)-(IV) for said one bed.

17. A process for refining an ammonia synthesis gas as claimed in claim 16 which further comprises:

in the desorption step (III), using a pressure swing adsorption-desorption unit which effects desorption of said one bed by pressure relief and heating by a hot gas.

18. A process for refining an ammonia synthesis gas as claimed in claim 16 which further comprises:

in said step (III), before said one bed undergoes pressure relief, feeding a gas containing almost no hydrogen into said one bed thereby replacing a gas present in the voids in said one bed; and

feeding the replaced gas into an adsorbent bed undergoing the repressurization step or discharging the replaced gas from the adsorption-desorption unit.

19. A process for refining an ammonia synthesis gas as claimed in claim 16 which further comprises:

in said step (III), relieving pressure in said one bed to a medium pressure;

then feeding a gas containing almost no hydrogen into said one bed thereby replacing a gas present in the voids in said one bed; and

feeding the gas evolved by said pressure relief and the replaced gas into an adsorbent bed undergoing the repressurization step or discharging said both gases from the adsorption-desorption unit.

20. A process for refining an ammonia synthesis gas as claimed in claim 16 which further comprises:

in said step (III), relieving pressure in said one bed to a medium pressure;

feeding the gas evolved by the pressure relief to an adsorbent bed undergoing the repressurization step;

then further relieving pressure in said one bed;

then feeding a gas containing almost no hydrogen into said one bed thereby replacing a gas present in the voids in said one bed;

feeding the gas evolved by said further pressure relief and the replaced gas into an intermediate tank, thereby using the resulting gas as a filling gas for the repressurization step.

21. A process for refining an ammonia synthesis gas as claimed in claim 18 which further comprises:

in said step (III), subsequent to the feeding of the evolved gas by pressure relief to a bed undergoing the repressurization step or to an intermediate tank, or the discharge of said gas from the adsorption-desorption unit, feeding the gas evolved from said one bed by further pressure relief to a pressurizing apparatus at a medium pressure; and

pressurizing said gas in said apparatus to a pressure higher than the replacing pressure thereby preparing the gas to be used in the replacing operation.

22. A process for refining an ammonia synthesis gas as claimed in claim 18 which further comprises:

in said step (III), in the desorption by pressure relief subsequent to the replacing operation, feeding a portion of the gas evolved by said pressure relief through one or more depressurization apparatuses each comprising a buffer tank and an expander in accordance with the degree of pressure relief thereby generating power which drives a compressor that draws a portion of said evolved gas at a pressure lower than the pressure of the gas discharged from the adsorption-desorption unit and pressurizes it to the pressure of the said discharged gas.

23. A process for refining an ammonia synthesis gas as claimed in claim 1 which further comprises:

in the step (d), after carbon dioxide is removed from the synthesis gas by absorption at a temperature lower than 0°

C., merging said synthesis gas, while keeping its temperature and pressure as in the absorption, with the circulating synthesis gas.

24. A process for refining an ammonia synthesis gas as claimed in claim 16 which further comprises:

washing with water the gas evolved from said one bed undergoing desorption in the desorption step (III);

distilling the resulting aqueous ammonia solution; and

liquefying the distilled ammonia through cooling thereby obtaining liquid ammonia.

25. A process for refining an ammonia synthesis gas as claimed in claim 5 which further comprises:

in said step (III), subsequent to the feeding of the evolved gas by pressure relief to a bed undergoing the repressurization step, feeding the gas evolved from said one bed by further pressure relief to a pressurizing apparatus at a medium pressure; and

pressurizing said gas in said apparatus to a pressure higher than the replacing pressure thereby preparing the replacing gas to be used in the replacing operation.

26. A process for refining an ammonia synthesis gas as claimed in claim 19 which further comprises:

in said step (III), subsequent to the feeding of the evolved gas by pressure relief to a bed undergoing the repressurization step or to an intermediate tank, or the discharge of said gas from the adsorption-desorption unit, feeding the gas evolved from said one bed by further pressure relief to a pressurizing apparatus at a medium pressure; and

pressurizing said gas in said apparatus to a pressure higher than the replacing pressure thereby preparing the gas to be used in the replacing operation.

27. A process for refining an ammonia synthesis gas as claimed in claim 20 which further comprises:

in said step (III), subsequent to the feeding of the evolved gas by pressure relief to a bed undergoing the repressurization step or to an intermediate tank, or the discharge of said gas from the adsorption-desorption unit, feeding the gas evolved from said one bed by further pressure relief to a pressurizing apparatus at a medium pressure; and

pressurizing said gas in said apparatus to a pressure higher than the replacing pressure thereby preparing the gas to be used in the replacing operation.

28. A process for refining an ammonia synthesis gas as claimed in claim 19 which further comprises:

in said step (III) the desorption by pressure relief subsequent to the replacing operation, feeding a portion of the gas evolved by said pressure relief through one or more depressurization apparatuses each comprising a buffer tank and an expander in accordance with the degree of pressure relief thereby generating power which drives a compressor that draws a portion of said evolved gas at a pressure lower than the pressure of the gas discharged from the adsorption-desorption unit and pressurizes it to the pressure of the said discharge gas.

29. A process for refining an ammonia synthesis gas as claimed in claim 20 which further comprises:

in said step (III) the desorption by pressure relief subsequent to the replacing operation, feeding a portion of the gas evolved by said pressure relief through one or more depressurization apparatuses each comprising a buffer tank and an expander in accordance with the degree of pressure relief thereby generating power which drives a compressor that draws a portion of said evolved gas at a pressure lower than the pressure of the gas discharged from the adsorption-desorption unit and pressurizes it to the pressure of the said discharge gas.