Low energy process for synthesis of ammonia

Claim 2

A process for the synthesis of ammonia, comprising: passing a synthesis feed gas consisting essentially of hydrogen and nitrogen in approximately a 3 to 1 ratio through at least one heat exchanger to heat said synthesis feed gas to a first reaction temperature; passing said heated synthesis gas at said first reaction temperature through a first ammonia synthesis catalyst bed wherein an exothermic reaction occurs to produce a first effluent containing ammonia; passing a portion of said first catalyst bed effluent through a heat exchanger to cool said effluent portion and mixing said cooled first effluent portion with the remainder of said first catalyst bed effluent to adjust the temperature of said first catalyst bed effluent to a second reaction temperature; passing said first catalyst bed effluent at said second reaction temperature through a second ammonia synthesis catalyst bed for exothermic reaction to produce a second catalyst bed effluent containing further ammonia; passing a portion of said second catalyst bed effluent through another heat exchanger to cool said second effluent portion and mixing said cooled second effluent portion with the remainder of said second catalyst bed effluent to adjust the temperature of said second catalyst bed effluent to a third reaction temperature; and passing said second catalyst bed effluent at said third reaction temperature through a third ammonia synthesis catalyst bed wherein an exothermic reaction occurs to produce a third effluent containing further ammonia.

Claim 3

The process of claim 1, including: exchanging said portion of first catalyst bed effluent with said synthesis feed gas in order to at least partially heat said synthesis feed gas to said first reaction temperature simultaneously with the cooling of said first catalyst bed effluent portion.

Claim 4

The process of claim 1, including: exchanging said portion of second catalyst bed effluent with said synthesis feed gas in order to at least partially heat said synthesis feed gas to said first reaction temperature simultaneously with the cooling of said second catalyst bed effluent portion.

Claim 5

The process of claim 1, including: passing said synthesis feed gas at said first reaction temperature, said first catalyst effluent at said second reaction temperature and said second catalyst bed effluent at said third reaction temperature in a radial direction through said first, second and third catalyst beds, respectively.

Claim 6

The process of claim 1, wherein: the pressure of said synthesis feed gas and said effluents of said first, second and third catalyst beds is within a range of 20 to 95 atmospheres.

Claim 7

The process of claim 1, wherein: the pressure drops between said synthesis feed gas at said first reaction temperature and said third effluent from said third catalyst bed is within a range of 0.5 to 3 atmospheres.

Claim 8

The process of claim 1, wherein: all of the synthesis gas is passed through said first catalyst bed, all of the effluent of the first catalyst bed is passed through said second catalyst bed and all of the effluent of said second catalyst bed is passed through said third catalyst bed.

Claim 9

The process of claim 1, wherein: The portion of said second catalyst bed effluent passing through said heat exchanger is changed to adjust the temperature of said second catalyst bed effluent to a third reaction temperature.

Claim 10

The process of claim 1, wherein: The second reaction temperature and the third reaction temperature are adjusted by changing the portion of first catalyst bed effluent passing through said heat exchanger and changing the portion of second catalyst bed effluent passing through said another heat exchanger, respectively.

Claim 11

A synthesis process for producing ammonia, comprising: passing a synthesis gas consisting essentially of hydrogen and nitrogen in approximately a 3 to 1 ratio at a pressure within the range of 25 to 90 atmospheres through a series of indirect heat exchangers to heat said synthesis gas to reaction temperature; passing said heated synthesis gas radially through a first ammonia synthesis catalyst bed, the thickness of said bed being such that the pressure drop is less than 1 atmosphere, wherein an exothermic reaction occurs to produce a first effluent containing ammonia; passing a portion of said first effluent through one of said indirect heat exchangers to heat said synthesis gas and cool said first effluent and bypassing the remaining portion of said first effluent from passage through said indirect heat exchanger and combining said portions to control the temperature of said first effluent; passing said cooled first effluent radially through a second ammonia synthesis catalyst bed, the thickness of said bed being such that the pressure drop is less than 1 atmosphere, wherein an exothermic reaction occurs to produce a second effluent containing ammonia; passing a portion of said second effluent through one of said indirect heat exchangers to heat said synthesis gas and cool said second effluent and bypassing the remaining portion of said second effluent from passage through said indirect heat exchanger and combining said portions to control the temperature of said second effluent; and passing said cooled second effluent radially through a third ammonia synthesis catalyst bed, the thickness of said bed being such that the pressure drop is less than 1 atmosphere, wherein an exothermic reaction occurs to produce a third effluent containing ammonia.

Claim 12

A synthesis process for producing ammonia, comprising: passing a synthesis gas consisting essentially of hydrogen and nitrogen in approximately a 3 to 1 ratio at a pressure within the range of 25 to 90 atmospheres through a series of indirect heat exchangers to heat said synthesis gas to reaction temperature; passing said heated synthesis gas radially through a first ammonia synthesis catalyst bed, the thickness of said bed being such that the pressure drop is less than 1 atmosphere, wherein an exothermic reaction occurs to produce a first effluent containing ammonia; passing a portion of said first effluent through one of said indirect heat exchangers to heat said synthesis gas and cool said first effluent and bypassing the remaining portion of said first effluent from passage through said indirect heat exchanger and combining said portions to control the temperature of said first effluent; passing said cooled first effluent radially through a second ammonia synthesis catalyst bed, the thickness of said bed being such that the pressure drop is less than 1 atmosphere, wherein an exothermic reaction occurs to produce a second effluent containing ammonia; passing a portion of said second effluent through one of said indirect heat exchangers to heat said synthesis gas and cool said second effluent and bypassing the remaining portion of said second effluent from passage through said indirect heat exchanger and combining said portions to control the temperature of said second effluent; and passing said cooled second effluent radially through a third ammonia synthesis catalyst bed, the thickness of said bed being such that the pressure drop is less than 1 atmosphere, wherein an exothermic reaction occurs to produce a third effluent containing ammonia.

Claim 13

The process of claim 10, including: bypassing a portion of said synthesis gas passed through at least one of said indirect heat exchangers to control the temperature of synthesis gas entering said first ammonia synthesis bed.